Figura 1 โ€“ Mapa de localizaรงรฃo da PCH Salto Paraopeba

ํ•˜์ฒœ ์ €์ˆ˜์ง€ ๋ฌผ๋ฆฌ์  ๋ชจ๋ธ์˜ ์นจ์  ๊ณผ์ •์— ๋Œ€ํ•œ ์ „์‚ฐ ์œ ์ฒด ์—ญํ•™ ๋ชจ๋ธ๋ง(CFD) ๊ธฐ์ค€

Natรกlia Melo da Silva1 1; Jorge Luis Zegarra Tarqui2,Edna Maria de Faria Viana 3

Abstract

์ €์ˆ˜์ง€ ์นจ์ „์€ ์ˆ˜๋ ฅ ๋ฐœ์ „์˜ ์ง€์† ๊ฐ€๋Šฅํ•œ ๋ฐœ์ „์„ ์œ„ํ•œ ์ฃผ์š” ๋ฌธ์ œ ์ค‘ ํ•˜๋‚˜์ด๋ฉฐ ๋ธŒ๋ผ์งˆ์— ๋งค์šฐ ์ค‘์š”ํ•ฉ๋‹ˆ๋‹ค. ๋ธŒ๋ผ์งˆ์˜ ์ฃผ์š” ์—๋„ˆ์ง€์›์€ ์ˆ˜๋ ฅ๋ฐœ์ „์†Œ์—์„œ ๋‚˜์˜ต๋‹ˆ๋‹ค. ์†Œ๊ทœ๋ชจ ์ˆ˜๋ ฅ ๋ฐœ์ „์†Œ(SHP)๋Š” ์žฌ์ƒ ์—๋„ˆ์ง€์˜ ๋ณด์™„์  ๋ฐœ์ „์„ ์œ„ํ•œ ์ค‘์š”ํ•œ ๋Œ€์•ˆ์ž…๋‹ˆ๋‹ค.

์ด๋“ค์˜ ์„ค๊ณ„, ๊ฑด์„ค, ์šด์˜ ๋ฐ ์žฌ๋™๋ ฅ์„ ์ตœ์ ํ™”ํ•˜๊ธฐ ์œ„ํ•ด ์ €์ˆ˜์ง€ ๋‚ด ํ‡ด์ ๋ฌผ์˜ ์œ ์ฒด ์—ญํ•™ ๋ฐ ์ด๋™์„ ์—ฐ๊ตฌํ•˜๋Š” ๊ฒƒ์ด ๋งค์šฐ ์ค‘์š”ํ•ฉ๋‹ˆ๋‹ค.

3์ฐจ์› ์ „์‚ฐ์œ ์ฒด์—ญํ•™ – CFD 3D ๋ชจ๋ธ๋ง์€ ๋ณต์žกํ•œ ํ๋ฆ„ ๋ฌธ์ œ์— ๊ฐ€์žฅ ์ ํ•ฉํ•œ ๋ฐฉ๋ฒ•์ž…๋‹ˆ๋‹ค. ์ œ์•ˆ๋œ ๋ฐฉ๋ฒ•์€ MG Jeceaba ์ž์น˜๊ตฌ์— ์œ„์น˜ํ•œ PCH Salto Paraopeba์˜ ์œ ์ฒด ์—ญํ•™ ๋ฐ ํ‡ด์ ๋ฌผ ์ด๋™ ํ˜„์ƒ์„ ์žฌํ˜„ํ•˜๊ณ  ํ‰๊ฐ€ํ•˜๋Š” ๊ฒƒ์„ ๋ชฉํ‘œ๋กœ ํ•˜๋ฉฐ, ์ทจ์ˆ˜๊ตฌ์˜ ์™„์ „ํ•œ ์นจ์ „์œผ๋กœ ์ธํ•ด ์ž‘๋™์ด ์ค‘๋‹จ๋˜์—ˆ์Šต๋‹ˆ๋‹ค.

๋ชจ๋ธ์˜ ๊ฒ€์ฆ์€ ๋ฏธ๋‚˜์Šค์ œ๋ผ์ด์Šค ์—ฐ๋ฐฉ๋Œ€ํ•™๊ต์˜ ์ˆ˜๋ ฅํ•™ ์—ฐ๊ตฌ ์„ผํ„ฐ(CPH)์— ๊ตฌ์ถ•๋œ ์ถ•์†Œ๋œ ๋ฌผ๋ฆฌ์  ๋ชจ๋ธ์˜ ์‹คํ—˜ ๋ฐ์ดํ„ฐ๋ฅผ ์‚ฌ์šฉํ•˜์—ฌ ์ˆ˜ํ–‰๋ฉ๋‹ˆ๋‹ค.

Abstract: The reservoir silting is one of the main problems for sustainable development in the
generation of hydroelectric energy and it is of great significance for Brazil. The main source of energy
in Brazil comes from hydroelectric power plant. The Small Hydroelectric Power Plant (SHP) are an
important alternative for complementary generation of renewable energy.
Seeking to optimize the design, construction, operation, and repowering of these, it is extremely
important to study the hydrodynamics and transport of sediments in their reservoirs. Threedimensional Computational Fluid Dynamics – CFD 3D modeling is the most appropriate method for
complex flow problems. The proposed method aims to reproduce and evaluate the hydrodynamic and
sediment transport phenomena of the PCH Salto Paraopeba, located in the municipality of Jeceaba,
MG, which stopped working due to the complete silting up of its water intake. The validation of the
model will be done using experimental data from the reduced physical model, built at the Hydraulic
Research Center (CPH) at the Federal University of Minas Gerais.

Keywords

ํ‡ด์ ๋ฌผ ์ˆ˜์†ก, ๋ฌผ๋ฆฌ์  ๋ชจ๋ธ, ์†Œ๊ทœ๋ชจ ์ˆ˜๋ ฅ ๋ฐœ์ „์†Œ, Sediment transport, physical model, Small Hydroelectric Power Plant.

Figura 1 โ€“ Mapa de localizaรงรฃo da PCH Salto Paraopeba
Figura 1 โ€“ Mapa de localizaรงรฃo da PCH Salto Paraopeba
Figura 2 โ€“ PCH Salto Paraopeba e modelo reduzido.
Figura 2 โ€“ PCH Salto Paraopeba e modelo reduzido.

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๋น„์„ ํ˜• ํŒŒ๋ ฅ์˜ ์˜ํ–ฅ์— ๋”ฐ๋ฅธ ์ž”ํ•ด ์–ธ๋• ๋ฐฉํŒŒ์ œ ํ˜•์ƒ์˜ ํšจ๊ณผ์— ๋Œ€ํ•œ ์ˆ˜์น˜ ๋ถ„์„

๋น„์„ ํ˜• ํŒŒ๋ ฅ์˜ ์˜ํ–ฅ์— ๋”ฐ๋ฅธ ์ž”ํ•ด ์–ธ๋• ๋ฐฉํŒŒ์ œ ํ˜•์ƒ์˜ ํšจ๊ณผ์— ๋Œ€ํ•œ ์ˆ˜์น˜ ๋ถ„์„

Numerical Analysis of the Effects of Rubble Mound Breakwater Geometry Under the Effect of Nonlinear Wave Force

Arabian Journal for Science and EngineeringAims and scopeSubmit manuscript

Cite this article

Abstract

Assessing the interaction of waves and porous offshore structures such as rubble mound breakwaters plays a critical role in designing such structures optimally. This study focused on the effect of the geometric parameters of a sloped rubble mound breakwater, including the shape of the armour, method of its arrangement, and the breakwater slope. Thus, three main design criteria, including the wave reflection coefficient (Kr), transmission coefficient (Kt), and depreciation wave energy coefficient (Kd), are discussed. Based on the results, a decrease in wavelength reduced the Kr and increased the Kt and Kd. The rubble mound breakwater with the Coreloc armour layer could exhibit the lowest Kr compared to other armour geometries. In addition, a decrease in the breakwater slope reduced the Kr and Kd by 3.4 and 1.25%, respectively. In addition, a decrease in the breakwater slope from 33 to 25ยฐ increased the wave breaking height by 6.1% on average. Further, a decrease in the breakwater slope reduced the intensity of turbulence depreciation. Finally, the armour geometry and arrangement of armour layers on the breakwater with its different slopes affect the wave behaviour and interaction between the wave and breakwater. Thus, layering on the breakwater and the correct use of the geometric shapes of the armour should be considered when designing such structures.

ํŒŒ๋„์™€ ์ž”ํ•ด ๋”๋ฏธ ๋ฐฉํŒŒ์ œ์™€ ๊ฐ™์€ ๋‹ค๊ณต์„ฑ ํ•ด์–‘ ๊ตฌ์กฐ๋ฌผ์˜ ์ƒํ˜ธ ์ž‘์šฉ์„ ํ‰๊ฐ€ํ•˜๋Š” ๊ฒƒ์€ ์ด๋Ÿฌํ•œ ๊ตฌ์กฐ๋ฌผ์„ ์ตœ์ ์œผ๋กœ ์„ค๊ณ„ํ•˜๋Š” ๋ฐ ์ค‘์š”ํ•œ ์—ญํ• ์„ ํ•ฉ๋‹ˆ๋‹ค. ๋ณธ ์—ฐ๊ตฌ๋Š” ๊ฒฝ์‚ฌ์ง„ ์ž”ํ•ด ๋‘”๋• ๋ฐฉํŒŒ์ œ์˜ ๊ธฐํ•˜ํ•™์  ๋งค๊ฐœ๋ณ€์ˆ˜์˜ ํšจ๊ณผ์— ์ดˆ์ ์„ ๋งž์ถ”์—ˆ๋Š”๋ฐ, ์—ฌ๊ธฐ์—๋Š” ๊ฐ‘์˜ท์˜ ํ˜•ํƒœ, ๋ฐฐ์น˜ ๋ฐฉ๋ฒ•, ๋ฐฉํŒŒ์ œ ๊ฒฝ์‚ฌ ๋“ฑ์ด ํฌํ•จ๋œ๋‹ค. ๋”ฐ๋ผ์„œ ํŒŒ๋™ ๋ฐ˜์‚ฌ ๊ณ„์ˆ˜(Kr), ํˆฌ๊ณผ ๊ณ„์ˆ˜(Kt) ๋ฐ ๊ฐ๊ฐ€์ƒ๊ฐํŒŒ ์—๋„ˆ์ง€ ๊ณ„์ˆ˜(Kd)์— ๋Œ€ํ•ด ๋…ผ์˜ํ•ฉ๋‹ˆ๋‹ค. ๊ฒฐ๊ณผ์— ๋”ฐ๋ฅด๋ฉด ํŒŒ์žฅ์ด ๊ฐ์†Œํ•˜๋ฉด K๊ฐ€ ๊ฐ์†Œํ•ฉ๋‹ˆ๋‹ค.r๊ทธ๋ฆฌ๊ณ  K๋ฅผ ์ฆ๊ฐ€์‹œ์ผฐ์Šต๋‹ˆ๋‹คt ๋ฐ Kd. Coreloc ์žฅ๊ฐ‘ ์ธต์ด ์žˆ๋Š” ์ž”ํ•ด ์–ธ๋• ๋ฐฉํŒŒ์ œ๋Š” ๊ฐ€์žฅ ๋‚ฎ์€ K๋ฅผ ๋‚˜ํƒ€๋‚ผ ์ˆ˜ ์žˆ์Šต๋‹ˆ๋‹ค.r ๋‹ค๋ฅธ ๊ฐ‘์˜ท ํ˜•์ƒ๊ณผ ๋น„๊ตํ–ˆ์Šต๋‹ˆ๋‹ค. ๋˜ํ•œ ๋ฐฉํŒŒ์ œ ๊ฒฝ์‚ฌ๊ฐ€ ๊ฐ์†Œํ•˜์—ฌ K๊ฐ€ ๊ฐ์†Œํ–ˆ์Šต๋‹ˆ๋‹ค.r ๋ฐ Kd ๊ฐ๊ฐ 3.4%, 1.25% ์ฆ๊ฐ€ํ–ˆ๋‹ค. ๋˜ํ•œ ๋ฐฉํŒŒ์ œ ๊ฒฝ์‚ฌ๊ฐ€ 33ยฐ์—์„œ 25ยฐ๋กœ ๊ฐ์†Œํ•˜์—ฌ ํŒŒ๋„ ํŒŒ์‡„ ๋†’์ด๊ฐ€ ํ‰๊ท  6.1% ์ฆ๊ฐ€ํ–ˆ์Šต๋‹ˆ๋‹ค. ๋˜ํ•œ, ๋ฐฉํŒŒ์ œ ๊ฒฝ์‚ฌ์˜ ๊ฐ์†Œ๋Š” ๋‚œ๋ฅ˜ ๊ฐ๊ฐ€์ƒ๊ฐ์˜ ๊ฐ•๋„๋ฅผ ๊ฐ์†Œ์‹œ์ผฐ๋‹ค. ๋งˆ์ง€๋ง‰์œผ๋กœ, ๊ฒฝ์‚ฌ๊ฐ€ ๋‹ค๋ฅธ ๋ฐฉํŒŒ์ œ์˜ ์žฅ๊ฐ‘ ํ˜•์ƒ๊ณผ ์žฅ๊ฐ‘ ์ธต์˜ ๋ฐฐ์—ด์€ ํŒŒ๋„ ๊ฑฐ๋™๊ณผ ํŒŒ๋„์™€ ๋ฐฉํŒŒ์ œ ์‚ฌ์ด์˜ ์ƒํ˜ธ ์ž‘์šฉ์— ์˜ํ–ฅ์„ ๋ฏธ์นฉ๋‹ˆ๋‹ค. ๋”ฐ๋ผ์„œ ์ด๋Ÿฌํ•œ ๊ตฌ์กฐ๋ฅผ ์„ค๊ณ„ ํ•  ๋•Œ ๋ฐฉํŒŒ์ œ์— ์ธต์„ ์Œ“๊ณ  ๊ฐ‘์˜ท์˜ ๊ธฐํ•˜ํ•™์  ๋ชจ์–‘์„ ์˜ฌ๋ฐ”๋ฅด๊ฒŒ ์‚ฌ์šฉํ•˜๋Š” ๊ฒƒ์„ ๊ณ ๋ คํ•ด์•ผํ•ฉ๋‹ˆ๋‹ค.

Keywords

  • Rubble mound breakwater
  • Computational fluid dynamics
  • Armour layer
  • Wave reflection coefficient
  • Wave transmission coefficient
  • Wave energy dissipation coefficient

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Open Channels Flow์—์„œ์˜ ์ฝ˜ํฌ๋ฆฌํŠธ ์บ”๋ฒ„์Šค ๊ฑฐ๋™ ์—ฐ๊ตฌ

Study of Concrete Canvas Behavior in Open Channels Flow

Document Type : Research Paper

Authors

1 Imam Hosein Uni

2 Researcher of Imam Hossein University, Faculty of Engineering and Passive Defense

3 Ivanki University, Iran.

 10.22124/JCR.2023.24324.1618

Abstract

๊ฐœ๋ฐฉ ์ˆ˜๋กœ์˜ ์‹ฌํ•œ ์ˆ˜๋ ฅ ๊ตฌ๋ฐฐ๋Š” ์นจ์ „์œผ๋กœ ์ธํ•œ ์‹ฌ๊ฐํ•œ ์นจ์‹๊ณผ ๋ฌธ์ œ๋ฅผ ์ผ์œผํ‚ต๋‹ˆ๋‹ค. ํŒจ๋ธŒ๋ฆญ ์ฝ˜ํฌ๋ฆฌํŠธ๋Š” ๊ธฐ์กด์˜ ์ฝ˜ํฌ๋ฆฌํŠธ ํ‘œ๋ฉด์„ ๋Œ€์ฒดํ•  ์ˆ˜ ์žˆ๋Š” ๋†’์€ ์‹คํ–‰ ์†๋„๋ฅผ ๊ฐ€์ง„ ๋…ํŠนํ•œ ์ œํ’ˆ์ž…๋‹ˆ๋‹ค. ์ด ์ œํ’ˆ์˜ ๊ธฐ๊ณ„์  ์ €ํ•ญ ๋งค๊ฐœ๋ณ€์ˆ˜์— ๋”ฐ๋ฅด๋ฉด ๋ถ€์‹ ์š”์ธ์— ๋Œ€ํ•œ ์šฐ์ˆ˜ํ•œ ๋‚ด๊ตฌ์„ฑ ์™ธ์—๋„ ์ง๋ฌผ ์ฝ˜ํฌ๋ฆฌํŠธ์˜ ์‘์šฉ ๋ถ„์•ผ ์ค‘ ํ•˜๋‚˜๋Š” ์šดํ•˜ ๋ฐ ์ˆ˜๋กœ ์•”๊ฑฐ ํ‘œ๋ฉด์— ์‚ฌ์šฉํ•˜๋Š” ๊ฒƒ์ž…๋‹ˆ๋‹ค. ์ด ์—ฐ๊ตฌ์—์„œ๋Š” ๋จผ์ € ์‚ฌ๋‹ค๋ฆฌ๊ผด ๋‹จ๋ฉด์˜ ๊ฐœ๋ฐฉ ์ฑ„๋„ ํ๋ฆ„์„ ์ง์„  ๊ฒฝ๋กœ ์ƒํƒœ์˜ 3๊ฐ€์ง€ ๊ณตํ†ต ์ฑ„๋„ ํ˜•์ƒ, ๊ตด๊ณก ๋ฐ ํŽธ์ฐจ๊ฐ€ ์žˆ๋Š” ๊ฒฝ๋กœ, ๋งˆ์ง€๋ง‰์œผ๋กœ ์ฑ„๋„ ํ•˜๋‹จ์˜ ๋†’์ด๊ฐ€ ๋ณ€๊ฒฝ๋œ ์ฑ„๋„ ๊ฒฝ๋กœ๋ฅผ ํฌํ•จํ•˜๋Š” 9๊ฐ€์ง€ ์‹œ๋‚˜๋ฆฌ์˜ค์—์„œ ์‹œ๋ฎฌ๋ ˆ์ด์…˜ํ•ฉ๋‹ˆ๋‹ค. ๊ฐ ์ฃผ์—์„œ flow-3d ์†Œํ”„ํŠธ์›จ์–ด๋ฅผ ์‚ฌ์šฉํ•œ ํ๋ฆ„ ๋‚œ๋ฅ˜ ๋ชจ๋ธ๋ง๊ณผ ํ•จ๊ป˜ 3๊ฐœ์˜ ์„œ๋กœ ๋‹ค๋ฅธ ํ๋ฆ„ ์ฒด์ œ๊ฐ€ ์กฐ์‚ฌ๋˜์—ˆ์Šต๋‹ˆ๋‹ค.

FLOW-3D ์†Œํ”„ํŠธ์›จ์–ด๋ฅผ ์‚ฌ์šฉํ•œ ์œ ๋™ ๋‚œ๋ฅ˜ ๋ชจ๋ธ๋ง๊ณผ ํ•จ๊ป˜ ๋‹ค์–‘ํ•œ ์œ ๋™ ์ฒด์ œ๊ฐ€ ์กฐ์‚ฌ๋˜์—ˆ์Šต๋‹ˆ๋‹ค. ABAQUS ์†Œํ”„ํŠธ์›จ์–ด๋ฅผ ์‚ฌ์šฉํ•˜์—ฌ ํŒจ๋ธŒ๋ฆญ ์ฝ˜ํฌ๋ฆฌํŠธ ๊ตฌ์„ฑ์š”์†Œ์™€ ์—ฐ๊ฒฐ ์˜์—ญ์„ ๋ชจ๋ธ๋งํ•˜๊ณ , ์ฝ˜ํฌ๋ฆฌํŠธ ํ‘œ๋ฉด๊ณผ ์ทจ์•ฝํ•œ ์—ฐ๊ฒฐ ์˜์—ญ์— ๋™์ผํ•œ ํž˜์„ ๊ฐ€ํ•˜์—ฌ ์ƒ์„ฑ๋œ ์‘๋ ฅ์˜ ์–‘์„ ํ™•์ธํ–ˆ์Šต๋‹ˆ๋‹ค. ๊ฒฐ๊ณผ๋Š” ์ƒ์„ฑ๋œ ์‘๋ ฅ์ด ์ง๋ฌผ ์ฝ˜ํฌ๋ฆฌํŠธ์˜ ์ธ์žฅ ๋ฐ ์••์ถ• ์‘๋ ฅ ์šฉ๋Ÿ‰์— ๋น„ํ•ด ๋งค์šฐ ๋‚ฎ๋‹ค๋Š” ๊ฒƒ์„ ๋ณด์—ฌ์ค๋‹ˆ๋‹ค. ํ๋ฆ„๊ณผ ์ฝ˜ํฌ๋ฆฌํŠธ์˜ ์ˆ˜๋ ฅ ์—ฐ๊ตฌ๋ฅผ ๊ฒ€์ฆํ•˜๊ธฐ ์œ„ํ•ด ๊ด€๋ จ ์‹คํ—˜์‹ค ๊ฒฐ๊ณผ๊ฐ€ ์‚ฌ์šฉ๋˜์—ˆ์Šต๋‹ˆ๋‹ค.

Severe hydraulic gradients in open channels cause severe bed erosion and problems caused by sedimentation. Fabric concrete is a unique product with high execution speed that can replace traditional concrete surfaces. According to the mechanical resistance parameters of this product, in addition to its good durability against corrosive factors, one of the applications of fabric concrete is its use on the surface of canals and water course culverts. In this research, first, the flow of open channels in trapezoidal section is simulated under 9 scenarios, which include 3 common channel geometries in the state of a straight path, a path with bends and deviations, and finally, a channel path with a change in height at the bottom of the channel. In each of the states, 3 different flow regimes have been investigated along with flow turbulence modeling using flow-3d software.

Different flow regimes have been investigated along with flow turbulence modeling using flow-3d software. Using ABAQUS software, fabric concrete components and their connection areas have been modeled, and by applying forces equated to the concrete surface and vulnerable connection areas, the amount of created stresses has been checked. The results show that the created stresses are very low compared to the tensile and compressive stress capacity of fabric concrete. In order to validate the hydraulic studies of flow and concrete, the relevant laboratory results have been used.

Keywords

Main Subjects

Figure 4. Rectangular stepped spillway with (a) three baffle arrangement (b) five baffle arrangement

Prediction of Energy Dissipation over Stepped Spillwaywith Baffles Using Machine Learning Techniques

Saurabh Pujari*
, Vijay Kaushik, S. Anbu Kumar
Department of Civil Engineering, Delhi Technological University, India
Received February 23, 2023; Revised April 25, 2023; Accepted June 11, 2023
Cite This Paper in the Following Citation Styles
(a): [1] Saurabh Pujari, Vijay Kaushik, S. Anbu Kumar , “Prediction of Energy Dissipation over Stepped Spillway with
Baffles Using Machine Learning Techniques,” Civil Engineering and Architecture, Vol. 11, No. 5, pp. 2377 – 2391, 2023.
DOI: 10.13189/cea.2023.110510.
(b): Saurabh Pujari, Vijay Kaushik, S. Anbu Kumar (2023). Prediction of Energy Dissipation over Stepped Spillway with
Baffles Using Machine Learning Techniques. Civil Engineering and Architecture, 11(5), 2377 – 2391. DOI:
10.13189/cea.2023.110510.
Copyrightยฉ2023 by authors, all rights reserved. Authors agree that this article remains permanently open access under
the terms of the Creative Commons Attribution License 4.0 International License

Abstract

In river engineering, the stepped spillway of a dam is an important component that may be used in various ways. It is necessary to conduct research dealing with flood control in order to investigate the method, in which energy is lost along the tiered spillways. In the past, several research projects on stepped spillways without baffles have been carried out utilizing a range of research approaches. In the present study, machine learning techniques such as Support Vector Machine (SVM) and Regression Tree (RT) are used to analyze the energy dissipation on rectangular stepped spillways that make use of baffles in a variety of configurations and at a range of channel slopes. The results of many experiments indicate that the amount of energy that is lost increases with the number of baffles that are present in flat channels with slopes and rises. In order to evaluate the efficiency and usefulness of the suggested model, the statistical indices that were developed for the experimental research are used to validate the models that were created for the study. The findings indicate that the suggested SVM model properly predicted the amount of energy that was dissipated when contrasted with RT and the method that had been developed in the past. This study verifies the use of machine learning techniques in this industry, and it is unique in that it anticipates energy dissipation along stepped spillways utilizing baffle designs. In addition, this work validates the use of machine learning methods in this field.

Keywords

Rectangular Stepped Spillways, Baffle Arrangements, Channel Slope, Support Vector Machine (SVM), Regression Tree (RT)

Introduction

To regulate water flows downstream of a dam, a spillway structure is employed, with stepped spillways preventing water from overflowing and causing damage to the dam. These spillways consist of a channel with built-in steps or drops. Flow patterns observed include nappe flow, transition flow, and skimming flow [1]. Numerous scholars have looked at the energy dissipation in stepped spillways [2-4]. Boes and Hager [5] looked at the benefits of stepped spillways, such as their simplicity of construction, less danger of cavitation, and smaller stilling basins at downstream dam toes owing to considerable energy loss along the chute. Hazzab and Chafic [7] conducted an experimental study on energy dissipation in stepped spillways and reported on flow configurations. Additionally, the Manksvill dam spillway was examined using a 1:25 scale physical wooden model [6]. For moderately inclined stepped channels, Stefan and Chanson [8] explored air-water flow measurements. Daniel [9] discussed how the existence of steps and step heights affect stepped spillways’ ability to dissipate energy. A comparison of the smooth invert chute flow with the self aerated stepped spillway. The energy dissipation in stepped spillways was investigated using various methods. Katourany [10] compared experimental findings to conventional USBR outcomes to examine the effects of different baffle widths, spacing between baffle rows, and step heights of baffled aprons. Salmasi et al. [11] assessed the energy dissipation of through-flow and over-flow in gabion stepped spillways, discovering that gabion spillways with pervious surfaces dissipated energy more efficiently than those with concrete walls. Other forms of stepped spillways, such as inclined steps and steps with end sills, were also quantitatively studied for energy dissipation [12]. Saedi and Asareh [13] examined how the number of drop stairs affected energy dissipation in stepped drops and suggested using stepped drops to increase energy dissipation by providing flow path roughness. Al-Husseini [14] found that decreasing the number of steps and downstream slopes led to an increase in flow energy dissipation, and that the use of cascade spillways reduced energy dissipation compared to the original step spillway. MARS and ANN methods were used to estimate energy dissipation in flow across stepped spillways under skimming flow conditions, with both models proving reliable [15]. Frederic et al. [16] evaluated the energy dissipation effectiveness and stability of the Mekin Dam spillway by confirming that flow did not result in transitional flow and by calculating safety factors at various intervals. A numerical model was developed to validate a physical model examining the impact of geometrical parameters on the dissipation rate in flows through stepped spillways [17]. The regulation of the rates of dissipation is studied using a particular kind of fuzzy inference system (FIS). The findings are compared with a predefined numerical database to determine the predicted energy dissipation under various circumstances. The findings show that the suggested FIS may be a useful tool for the operational management of dissipator structures while taking various geometric characteristics into account. Nasralla [18] studied the four phases of the spillway and conducted eighteen runs to enhance energy dissipation through the contraction-stepped spillway. The study considered alternative baffle placements, heights, and widths. The results showed that downstream baffles on the stepped spillway of the stilling basin improve energy dissipation. Using the Flow 3D software, Ikinciogullari [19] quantitatively analyzed the energy dissipation capabilities of trapezoidal stepped spillways using four distinct models and three different discharges. The findings showed that trapezoidal stepped spillways are up to 30% more efficient in dissipating energy than traditional stepped spillways. In previous works, only a few machine learning algorithms were used to forecast energy dissipation across a rectangular stepped spillway without baffles. Therefore, this study used machine learning approaches such as Support Vector Machine (SVM) and Regression Tree (RT) to predict energy dissipation across a rectangular stepped spillway with varied rectangular-shaped baffle configurations at different channel slopes. The study compared these models using statistical analysis to assess their efficiency in predicting energy dissipation over rectangular stepped spillways with baffles. 2. Materials and Methods 2.1. Experimental Setup The experiments were carried out at the Hydraulics laboratory of Delhi Technological University. The tests were performed in a rectangular tilting flume of 8m long, 0.30m wide and 0.40m deep which has a facility to make it horizontal and sloping as well (shown in Figure 1). The flume consists of an inlet section, an outlet section, and a collecting tank at the downstream end which is used to measure the discharge. Figure 2 depicts the model of a rectangular stepped spillway prepared using an acrylic sheet having a width of 0.30m, a height of 0.20m and a base length of 0.40m. A total of four steps were designed with a step height of 0.05m, the step length is 0.10m and rectangular-shaped baffles of length 0.10m and height of 0.05m were arranged in different manner. Figure 3 represents the different baffle arrangements used in the experimental work. At first, the experiment was conducted for no baffle condition. Thereafter the experiment was conducted for the first arrangement of three baffles, in which two baffles were placed at a distance of 0.10m from the toe of the spillway and a distance of 0.10m was maintained between the first two baffles and the third baffle was placed between the first two baffles at a distance of 0.20m from the toe of the spillway (figure 4a). After that, the experiment was conducted for the third arrangement of baffles which consists of five baffles, two more baffles were introduced at a distance of 0.30m from the toe of the spillway and a distance of 0.10m was maintained between them (figure 4b). The baffles used in the experiment were rectangular shaped which had a height of 0.05m and length of 0.10m. The experiments were conducted for five different discharges 2 l/s, 4 l/s, 6 l/s, 8 l/s and 10 l/s. For the purpose of determining the head values both upstream and downstream of the spillway model, a point gauge with a precision of 0.1mm was used. In order to determine the average velocities of the upstream and downstream portions, respectively, a pitot static tube was used in conjunction with a digital manometer.

Figure 1. Rectangular tilting flume
Figure 2. Dimensions of classical stepped spillway
Figure 3. Arrangements of baffles in classical stepped spillway
Figure 4. Rectangular stepped spillway with (a) three baffle arrangement (b) five baffle arrangement
Intrusion of fine sediments into river bed and its effect on river environment โ€“ a research review

๋ฏธ์„ธํ•œ ํ‡ด์ ๋ฌผ์ด ๊ฐ•๋ฐ”๋‹ฅ์— ์นจํˆฌํ•˜๊ณ  ํ•˜์ฒœ ํ™˜๊ฒฝ์— ๋ฏธ์น˜๋Š” ์˜ํ–ฅ โ€“ ์—ฐ๊ตฌ ๊ฒ€ํ† 

Intrusion of fine sediments into river bed and its effect on river environment โ€“ a research review

Nilav Karna,K.S. Hari Prasad, Sanjay Giriย & A.S. Lodhi

Abstract

Fine sediments enter into the river through various sources such as channel bed, bank, and catchment. It has been regarded as a type of pollution in river. Fine sediments present in a river have a significant effect on river health. Benthic micro-organism, plants, and large fishes, all are part of food chain of river biota. Any detrimental effect on any of these components of food chain misbalances the entire riverine ecosystem. Numerous studies have been carried out on the various environmental aspects of rivers considering the presence of fine sediment in river flow. The present paper critically reviews many of these aspects to understand the various environmental impacts of suspended sediment on river health, flora and fauna.

Keywords: 

  1. Introduction
    The existence of fine sediment in a river system is a natural phenomenon. But in many cases it is exacerbated by the manmade activities. The natural cause of fines being in flow generally keeps the whole system in equilibrium except during some calamites whereas anthropogenic activities leading to fines entering into the flow puts several adverse impacts on the entire river system and its ecology. Presence of fines in flow is considered as a type of pollution in water. In United States,
    the fine sediment in water along with other non point source pollution is considered as a major obstacle in providing quality water for fishes and recreation activities (Diplas and Parker 1985).
    Sediments in a river are broadly of two types, organic and inorganic, and they both move in two ways either along the bed of the channel called bed load or in suspension called suspended load and their movements depend upon fluid flow and sediment characteristics. Further many investigators have divided the materials in suspension into two different types.
    One which originates from channel bed and bank is called bed material suspended load and another that migrates from feeding catchment area is called wash load. A general perception is that wash loads are very fine materials like clay, silt but it may not always be true (Woo et al. 1986). In general, suspended materials are of size less than 2 mm. The impact of sand on the various aspects of river is comparatively less than that of silt and clay. The latter are chemically active and good carrier of many contaminants and nutrients such as dioxins, phosphorous, heavy and trace metals, polychlorinated biphenyl (PCBs), radionuclide, etc. (Foster and Charlesworth 1996; Horowitz et al. 1995; Owens et al. 2001; Salomons and Fรถrstner 1984; Stone and Droppo 1994; Thoms 1987). Foy and Bailey-Watt (1998) reported that out of 129 lakes in England and Wales, 69% have phosphorous contamination. Ten percent lakes, rivers, and bays of United States have sediment contaminants with chemicals as reported by USEPA. Several field and experimental studies have been conducted
    considering, sand, silt, and clay as suspended material. Hence, the subject reported herein is based on considering the fine sediment size smaller than 2 mm.
    Fine sediments have the ability to alter the hydraulics of the flow. Presence of fines in flow can change the magnitude of turbulence, it can change the friction resistance to flow. Fines can change the mobility and permeability of the bed material. In some extreme cases, fines in flow may even change the morphology of the river (Doeg and Koehn 1994; Nuttall 1972; Wright and Berrie 1987). Fines in the flow adversely affect the producer by increasing the turbidity, hindering the
    photosynthesis process by limiting the light penetration. This is ultimately reflected in the entire food ecosystem of river (Davis-Colley et al. 1992; Van Niewenhuyre and Laparrieve 1986). In addition, abrasion due to flowing sediment kills the aquatic flora (Edwards 1969; Brookes 1986). Intrusion of fines into the pores of river bed reduces space for several invertebrates, affects the spawning process (Petts 1984; Richards and Bacon 1994; Schalchli 1992). There are several other direct
    or indirect, short-term or long-term impacts of fines in river.
    The present paper reports the physical/environmental significance of fines in river. The hydraulic significance of presence of fines in the river has been reviewed in another paper (Effect of fine sediments on river hydraulics โ€“ a research review – http://dx.doi.org/10.1080/09715010.2014.982001).

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The distribution of the computed maximum current speed during the entire duration of the NAMI DANCE and FLOW-3D simulations. The resolution of computational domain is 10 m

Performance Comparison of NAMI DANCE and FLOW-3Dยฎย Models in Tsunami Propagation, Inundation and Currents using NTHMP Benchmark Problems

NTHMP ๋ฒค์น˜๋งˆํฌ ๋ฌธ์ œ๋ฅผ ์‚ฌ์šฉํ•˜์—ฌ ์“ฐ๋‚˜๋ฏธ ์ „ํŒŒ, ์นจ์ˆ˜ ๋ฐ ํ•ด๋ฅ˜์—์„œ NAMI DANCE ๋ฐ FLOW-3Dยฎ ๋ชจ๋ธ์˜ ์„ฑ๋Šฅ ๋น„๊ต

Pure and Applied Geophysicsย volumeย 176,ย pages3115โ€“3153 (2019)Cite this article

Abstract

Field observations provide valuable data regarding nearshore tsunami impact, yet only in inundation areas where tsunami waves have already flooded. Therefore, tsunami modeling is essential to understand tsunami behavior and prepare for tsunami inundation. It is necessary that all numerical models used in tsunami emergency planning be subject to benchmark tests for validation and verification. This study focuses on two numerical codes, NAMI DANCE and FLOW-3Dยฎ, for validation and performance comparison. NAMI DANCE is an in-house tsunami numerical model developed by the Ocean Engineering Research Center of Middle East Technical University, Turkey and Laboratory of Special Research Bureau for Automation of Marine Research, Russia. FLOW-3Dยฎ is a general purpose computational fluid dynamics software, which was developed by scientists who pioneered in the design of the Volume-of-Fluid technique. The codes are validated and their performances are compared via analytical, experimental and field benchmark problems, which are documented in the โ€˜โ€˜Proceedings and Results of the 2011 National Tsunami Hazard Mitigation Program (NTHMP) Model Benchmarking Workshopโ€™โ€™ and the โ€˜โ€˜Proceedings and Results of the NTHMP 2015 Tsunami Current Modeling Workshopโ€. The variations between the numerical solutions of these two models are evaluated through statistical error analysis.

ํ˜„์žฅ ๊ด€์ฐฐ์€ ์—ฐ์•ˆ ์“ฐ๋‚˜๋ฏธ ์˜ํ–ฅ์— ๊ด€ํ•œ ๊ท€์ค‘ํ•œ ๋ฐ์ดํ„ฐ๋ฅผ ์ œ๊ณตํ•˜์ง€๋งŒ ์“ฐ๋‚˜๋ฏธ ํŒŒ๋„๊ฐ€ ์ด๋ฏธ ๋ฒ”๋žŒํ•œ ์นจ์ˆ˜ ์ง€์—ญ์—์„œ๋งŒ ๊ฐ€๋Šฅํ•ฉ๋‹ˆ๋‹ค. ๋”ฐ๋ผ์„œ ์“ฐ๋‚˜๋ฏธ ๋ชจ๋ธ๋ง์€ ์“ฐ๋‚˜๋ฏธ ํ–‰๋™์„ ์ดํ•ดํ•˜๊ณ  ์“ฐ๋‚˜๋ฏธ ๋ฒ”๋žŒ์— ๋Œ€๋น„ํ•˜๋Š” ๋ฐ ํ•„์ˆ˜์ ์ž…๋‹ˆ๋‹ค.

์“ฐ๋‚˜๋ฏธ ๋น„์ƒ ๊ณ„ํš์— ์‚ฌ์šฉ๋˜๋Š” ๋ชจ๋“  ์ˆ˜์น˜ ๋ชจ๋ธ์€ ๊ฒ€์ฆ ๋ฐ ๊ฒ€์ฆ์„ ์œ„ํ•œ ๋ฒค์น˜๋งˆํฌ ํ…Œ์ŠคํŠธ๋ฅผ ๋ฐ›์•„์•ผ ํ•ฉ๋‹ˆ๋‹ค. ์ด ์—ฐ๊ตฌ๋Š” ๊ฒ€์ฆ ๋ฐ ์„ฑ๋Šฅ ๋น„๊ต๋ฅผ ์œ„ํ•ด NAMI DANCE ๋ฐ FLOW-3Dยฎ์˜ ๋‘ ๊ฐ€์ง€ ์ˆซ์ž ์ฝ”๋“œ์— ์ค‘์ ์„ ๋‘ก๋‹ˆ๋‹ค.

NAMI DANCE๋Š” ํ„ฐํ‚ค ์ค‘๋™ ๊ธฐ์ˆ  ๋Œ€ํ•™์˜ ํ•ด์–‘ ๊ณตํ•™ ์—ฐ๊ตฌ ์„ผํ„ฐ์™€ ๋Ÿฌ์‹œ์•„ ํ•ด์–‘ ์—ฐ๊ตฌ ์ž๋™ํ™”๋ฅผ ์œ„ํ•œ ํŠน๋ณ„ ์กฐ์‚ฌ๊ตญ ์—ฐ๊ตฌ์†Œ์—์„œ ๊ฐœ๋ฐœํ•œ ์‚ฌ๋‚ด ์“ฐ๋‚˜๋ฏธ ์ˆ˜์น˜ ๋ชจ๋ธ์ž…๋‹ˆ๋‹ค. FLOW-3Dยฎ๋Š” Volume-of-Fluid ๊ธฐ์ˆ ์˜ ์„ค๊ณ„๋ฅผ ๊ฐœ์ฒ™ํ•œ ๊ณผํ•™์ž๋“ค์ด ๊ฐœ๋ฐœํ•œ ๋ฒ”์šฉ ์ „์‚ฐ ์œ ์ฒด ์—ญํ•™ ์†Œํ”„ํŠธ์›จ์–ด์ž…๋‹ˆ๋‹ค.

์ฝ”๋“œ์˜ ์œ ํšจ์„ฑ์ด ๊ฒ€์ฆ๋˜๊ณ  ๋ถ„์„, ์‹คํ—˜ ๋ฐ ํ˜„์žฅ ๋ฒค์น˜๋งˆํฌ ๋ฌธ์ œ๋ฅผ ํ†ตํ•ด ์ฝ”๋“œ์˜ ์„ฑ๋Šฅ์ด ๋น„๊ต๋˜๋ฉฐ, ์ด๋Š” ‘2011๋…„ NTHMP(National Tsunami Hazard Mitigation Program) ๋ชจ๋ธ ๋ฒค์น˜๋งˆํ‚น ์›Œํฌ์ˆ์˜ ์ ˆ์ฐจ ๋ฐ ๊ฒฐ๊ณผ’์™€ ”์ ˆ์ฐจ ๋ฐ NTHMP 2015 ์“ฐ๋‚˜๋ฏธ ํ˜„์žฌ ๋ชจ๋ธ๋ง ์›Œํฌ์ˆ ๊ฒฐ๊ณผโ€. ์ด ๋‘ ๋ชจ๋ธ์˜ ์ˆ˜์น˜ ํ•ด ์‚ฌ์ด์˜ ๋ณ€๋™์€ ํ†ต๊ณ„์  ์˜ค๋ฅ˜ ๋ถ„์„์„ ํ†ตํ•ด ํ‰๊ฐ€๋ฉ๋‹ˆ๋‹ค.

The distribution of the computed maximum current speed during the entire duration of the NAMI DANCE and FLOW-3D simulations. The resolution of computational domain is 10 m
The distribution of the computed maximum current speed during the entire duration of the NAMI DANCE and FLOW-3D simulations. The resolution of computational domain is 10 m

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Acknowledgements

The authors wish to thank Dr. Andrey Zaytsev due to his undeniable contributions to the development of in-house numerical model, NAMI DANCE. The Turkish branch of Flow Science, Inc. is also acknowledged. Finally, the National Tsunami Hazard Mitigation Program (NTHMP), who provided most of the benchmark data, is appreciated. This research did not receive any specific grant from funding agencies in the public, commercial, or not-for-profit sectors.

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  1. Deniz Velioglu SogutPresent address: 1212 Computer Science, Department of Civil Engineering, Stony Brook University, Stony Brook, NY, 11794, USA

Authors and Affiliations

  1. Middle East Technical University, 06800, Ankara, TurkeyDeniz Velioglu Sogut & Ahmet Cevdet Yalciner

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Correspondence to Deniz Velioglu Sogut.

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Velioglu Sogut, D., Yalciner, A.C. Performance Comparison of NAMI DANCE and FLOW-3Dยฎ Models in Tsunami Propagation, Inundation and Currents using NTHMP Benchmark Problems. Pure Appl. Geophys. 176, 3115โ€“3153 (2019). https://doi.org/10.1007/s00024-018-1907-9

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  • Received22 December 2017
  • Revised16 May 2018
  • Accepted24 May 2018
  • Published07 June 2018
  • Issue Date01 July 2019
  • DOIhttps://doi.org/10.1007/s00024-018-1907-9

Keywords

  • Tsunami
  • depth-averaged shallow water
  • Reynolds-averaged Navierโ€“Stokes
  • benchmarking
  • NAMI DANCE
  • FLOW-3Dยฎ
Fig. 1. Protection matt over the scour pit.

๊ทธ๋ฌผํ˜• ์„ธ๊ตด๋ฐฉ์ง€๋งคํŠธ๋ฅผ ์‚ฌ์šฉํ•œ ์ˆ˜์ง๋ง๋š์˜ ํ๋ฆ„์— ๋Œ€ํ•œ ์ˆ˜์น˜์  ์—ฐ๊ตฌ

Numerical study of the flow at a vertical pile with net-like scour protection matt
Minxi Zhanga,b
, Hanyan Zhaoc
, Dongliang Zhao d, Shaolin Yuee
, Huan Zhoue
,
Xudong Zhaoa
, Carlo Gualtierif
, Guoliang Yua,b,โˆ—
a SKLOE, School of Naval Architecture, Ocean & Civil Engineering, Shanghai Jiao Tong University, Shanghai 200240, China b KLMIES, MOE, School of Naval Architecture, Ocean & Civil Engineering, Shanghai Jiao Tong University, Shanghai 200240, China c Guangdong Research Institute of Water Resources and Hydropower, Guangzhou 510610, China d CCCC Second Harbor Engineering Co., Ltd., Wuhan 430040, China e CCCC Road & Bridge Special Engineering Co., Ltd, Wuhan 430071, China f Department of Structures for Engineering and Architecture, University of Naples Federico II, Italy

Abstract

ํ˜„์žฌ ๋˜๋Š” ํŒŒ๋„ ํ™˜๊ฒฝ์—์„œ ๋ง๋š ๋˜๋Š” ๋ถ€๋‘์˜ ๊ตญ๋ถ€ ์„ธ๊ตด์€ ์ „ ์„ธ๊ณ„์ ์œผ๋กœ ์ƒ๋ถ€ ๊ตฌ์กฐ๋ฌผ์˜ ์•ˆ์ „์„ ์œ„ํ˜‘ํ•ฉ๋‹ˆ๋‹ค. ๋ง๋š์ด๋‚˜ ๋ถ€๋‘์—์„œ ์„ธ๊ตด ๋ฐฉ์ง€ ๋ฎ๊ฐœ๋กœ ๊ทธ๋ฌผ ๋ชจ์–‘์˜ ๋งคํŠธ๋ฅผ ์ ์šฉํ•˜๋Š” ๊ฒƒ์ด ์ œ์•ˆ๋˜์—ˆ์Šต๋‹ˆ๋‹ค. ๋งคํŠธ๋Š” ๊ตญ๋ถ€ ์„ธ๊ตด ๊ตฌ๋ฉ์ด์˜ ํ๋ฆ„์„ ์•ฝํ™” ๋ฐ ํ™•์‚ฐ์‹œ์ผœ ๊ตญ๋ถ€ ์„ธ๊ตด์„ ์ค„์ด๊ณ  ํ‡ด์ ๋ฌผ ํ‡ด์ ์„ ๊ฐ•ํ™”ํ•ฉ๋‹ˆ๋‹ค. ๋งคํŠธ๋กœ ๋ฎํžŒ ๋ง๋š์˜ ํ๋ฆ„์„ ์กฐ์‚ฌํ•˜๊ธฐ ์œ„ํ•ด ์ˆ˜์น˜ ์‹œ๋ฎฌ๋ ˆ์ด์…˜์„ ์ˆ˜ํ–‰ํ–ˆ์Šต๋‹ˆ๋‹ค. ์‹œ๋ฎฌ๋ ˆ์ด์…˜ ๊ฒฐ๊ณผ๋Š” ๋งคํŠธ์˜ ๋‘๊ป˜ dt(2.6d95 ~ 17.9d95)์™€ ๊ฐœ๊ตฌ๋ถ€ ํฌ๊ธฐ dn(7.7d95 ~ 28.2d95)์„ ์ตœ์ ํ™”ํ•˜๋Š” ๋ฐ ์‚ฌ์šฉ๋˜์—ˆ์Šต๋‹ˆ๋‹ค. ๋งคํŠธ๊ฐ€ ๊ตญ๋ถ€ ์†๋„๋ฅผ ์ƒ๋‹นํžˆ ๊ฐ์†Œ์‹œํ‚ค๊ณ  ๋ง๋š์—์„œ ์™€๋ฅ˜๋ฅผ ์†Œ๋ฉธ์‹œ์ผœ ๊ตญ๋ถ€ ์„ธ๊ตด ๋ฒ”์œ„๋ฅผ ์‹ค์งˆ์ ์œผ๋กœ ๊ฐ์†Œ์‹œํ‚ค๋Š” ๊ฒƒ์œผ๋กœ ๋ฐํ˜€์กŒ์Šต๋‹ˆ๋‹ค. ๋งคํŠธ์˜ ๊ฐœ๊ตฌ๋ถ€ ํฌ๊ธฐ๊ฐ€ ์ž‘์„์ˆ˜๋ก ๋ฒ ๋“œ์—์„œ์˜ ์œ ๋™ํ™•์‚ฐ์ด ๋” ํšจ๊ณผ์ ์ด์—ˆ์œผ๋ฉฐ ๋ง๋š์—์„œ ๋” ์ž‘์€ ๋ฒ ๋“œ์ „๋‹จ์‘๋ ฅ์ด ๊ด€์ฐฐ๋˜์—ˆ๋‹ค. ๋ณธ ์—ฐ๊ตฌ์—์„œ ๊ณ ๋ คํ•œ ์œ ๋™ ์กฐ๊ฑด์˜ ๊ฒฝ์šฐ ์ƒ๋Œ€ ๋‘๊ป˜ T = 7.7 ๋ฐ ์ƒ๋Œ€ ๊ฐœ๊ตฌ ํฌ๊ธฐ S = 7.7์ธ ๋งคํŠธ๊ฐ€ ์„ธ๊ตด ๋ฐฉ์ง€์— ํšจ๊ณผ์ ์ผ ์ˆ˜ ์žˆ์Šต๋‹ˆ๋‹ค.

Fig. 1. Protection matt over the scour pit.
Fig. 26. Distribution of the turbulent kinetic energy on the y-z plane (X = 0.5) for various S
Fig. 26. Distribution of the turbulent kinetic energy on the y-z plane (X = 0.5) for various S

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Effects of pile-cap elevation on scour and turbulence around a complex bridge pier

๋ณต์žกํ•œ ๊ต๊ฐ ์ฃผ๋ณ€์˜ ์„ธ๊ตด ๋ฐ ๋‚œ๊ธฐ๋ฅ˜์— ๋Œ€ํ•œ ๋ง๋š ๋šœ๊ป‘ ๋†’์ด์˜ ์˜ํ–ฅ

ABSTRACT

์ด ์—ฐ๊ตฌ์—์„œ๋Š” ์„ธ ๊ฐ€์ง€ ๋‹ค๋ฅธ ๋ง๋š ๋šœ๊ป‘ ๋†’์ด์—์„œ ์ง์‚ฌ๊ฐํ˜• ๋ง๋š ์บก์ด ์žˆ๋Š” ๋ณต์žกํ•œ ๋ถ€๋‘ ์ฃผ๋ณ€์˜ ์ง€์—ญ ์„ธ๊ตด ๋ฐ ๊ด€๋ จ ํ๋ฆ„ ์œ ์ฒด ์—ญํ•™์„ ์กฐ์‚ฌํ•ฉ๋‹ˆ๋‹ค. ๋ง๋š ์บก ๋†’์ด๊ฐ€ ์ดˆ๊ธฐ ๋ชจ๋ž˜์ธต์— ๋Œ€ํ•ด ์„ ํƒ๋˜์—ˆ์œผ๋ฉฐ, ๋ง๋š ์บก์ด ํ๋ฆ„์— ๋…ธ์ถœ๋˜์ง€ ์•Š๊ณ (์‚ฌ๋ก€ I), ๋ถ€๋ถ„์ ์œผ๋กœ ๋…ธ์ถœ๋˜๊ณ (์‚ฌ๋ก€ II) ์™„์ „ํžˆ ๋…ธ์ถœ(์‚ฌ๋ก€ III)๋˜๋„๋ก ํ–ˆ์Šต๋‹ˆ๋‹ค. ์‹คํ—˜์€ ๋ง‘์€ ๋ฌผ ์„ธ๊ตด ์กฐ๊ฑด ํ•˜์—์„œ ์žฌ์ˆœํ™˜ ์ˆ˜๋กœ์—์„œ ์ˆ˜ํ–‰๋˜์—ˆ์œผ๋ฉฐ, ์ž…์ž ์ด๋ฏธ์ง€ ์œ ์†๊ณ„ (PIV) ๊ธฐ์ˆ ์„ ์‚ฌ์šฉํ•˜์—ฌ ๋‹ค๋ฅธ ์ˆ˜์ง๋ฉด์—์„œ ์ˆœ๊ฐ„ ์œ ์†์„ ์–ป์—ˆ์Šต๋‹ˆ๋‹ค. ๋ถ€๋ถ„์ ์œผ๋กœ ๋…ธ์ถœ๋œ ํŒŒ์ผ ์บก ์ผ€์ด์Šค๋Š” ์ตœ๋Œ€ ์ˆ˜์„ธ๋ฏธ ๊นŠ์ด(MSD)๋ฅผ ๋ณด์—ฌ์ฃผ์—ˆ์Šต๋‹ˆ๋‹ค. ์‚ฌ๋ก€ II์—์„œ MSD๊ฐ€ ๋ฐœ์ƒํ•œ ์ด์œ ๋Š” ๋‚œ๋ฅ˜ ์œ ๋™์žฅ ๋ถ„์„์„ ํ†ตํ•ด ๋ฐํ˜€์กŒ๋Š”๋ฐ, ์ด๋Š” ๋ง๋š ์บก์ด ํ๋ฆ„์— ๋…ธ์ถœ๋จ์— ๋”ฐ๋ผ ๋” ๋†’์€ ์„ธ๊ตด ๊นŠ์ด๋ฅผ ๋‹ด๋‹นํ•˜๋Š” ๋ง๋š ๊ฐ€์žฅ์ž๋ฆฌ์—์„œ ์™€๋ฅ˜ ์ƒ์„ฑ์— ์ง€๋ฐฐ์ ์œผ๋กœ ์˜ํ–ฅ์„ ๋ฏธ์นœ๋‹ค๋Š” ๊ฒƒ์„ ๋ณด์—ฌ์ฃผ์—ˆ์Šต๋‹ˆ๋‹ค. ์œ ๋™์žฅ์— ๋Œ€ํ•œ ํŒŒ์ผ ์บก์˜ ์˜ํ–ฅ์€ ํ‰๊ท  ์†๋„, ์†Œ์šฉ๋Œ์ด, ๋ ˆ์ด๋†€์ฆˆ ์ „๋‹จ ์‘๋ ฅ ๋ฐ ๋‚œ๋ฅ˜ ์šด๋™ ์—๋„ˆ์ง€ ์œค๊ณฝ์„ ํ†ตํ•ด ์‚ฌ๋ก€ III์—์„œ ๋‘๋“œ๋Ÿฌ์ง€๊ฒŒ ๋‚˜ํƒ€๋‚ฌ์ง€๋งŒ ํŒŒ์ผ ์บก์ด ๋ฒ ๋“œ์—์„œ ๋–จ์–ด์ ธ ์žˆ์—ˆ๊ธฐ ๋•Œ๋ฌธ์— ํŒŒ์ผ ์บก ๋ชจ์„œ๋ฆฌ๋Š” ์ˆ˜์„ธ๋ฏธ์— ์ง์ ‘์ ์ธ ์˜ํ–ฅ์„ ๋ฏธ์น˜์ง€ ์•Š์•˜์Šต๋‹ˆ๋‹ค.

In this study, the local scour and the associated flow hydrodynamics around a complex pier with rectangular pile-cap at three different pile-cap elevations are investigated. The pile-cap elevations were selected with respect to the initial sand bed, such that the pile-cap was unexposed (case I), partially exposed (case II), and fully exposed (case III) to the flow. The experiments were performed in a recirculating flume under clear-water scour conditions, and the instantaneous flow velocity was obtained at different vertical planes using the particle image velocimetry (PIV) technique. The partially exposed pile-cap case showed the maximum obtained scour-depth (MSD). The reason behind the MSD occurrence in case II was enunciated through the analysis of turbulent flow field which showed that as the pile-cap got exposed to the flow, it dominantly affected the generation of vortices from the pile-cap corners responsible for the higher scour depth. The effect of the pile-cap on the flow field was prominently seen in case III through the mean velocities, vorticity, Reynolds shear stresses and turbulent kinetic energy contours, but since the pile-cap was away from the bed, the pile-cap corners did not show any direct effect on the scour.

KEYWORDS: 

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Effects of surface roughness on overflow discharge of embankment weirs

ํ‘œ๋ฉด ๊ฑฐ์น ๊ธฐ๊ฐ€ ์ œ๋ฐฉ ๋‘‘์˜ ์˜ค๋ฒ„ํ”Œ๋กœ ๋ฐฐ์ถœ์— ๋ฏธ์น˜๋Š” ์˜ํ–ฅ

Effects of surface roughness on overflow discharge of embankment weirs

Abstract

A numerical study was performed on the embankment weir overflows with various surface roughness and tailwater submergence, to better understand the effects of weir roughness on discharge performances under the free and submerged conditions. The variation of flow regime is captured, from the free overflow, submerged hydraulic jump, to surface flow with increasing tailwater depth. A roughness factor is introduced to reflect the reduction in discharge caused by weir roughness. The roughness factor decreases with the roughness height, and it also depends on the tailwater depth, highlighting various relations of the roughness factor with the roughness height between different flow regimes, which is linear for the free overflow and submerged hydraulic jump while exponential for the surface flow. Accordingly, the effects of weir roughness on overflow discharge appear nonnegligible for the significant roughness height and the surface flow regime occurring under considerable tailwater submergence. The established empirical expressions of discharge coefficient and submergence and roughness factors make it possible to predict the discharge over embankment weirs considering both tailwater submergence and surface roughness.

์ž์œ  ๋ฐ ์นจ์ˆ˜ ์กฐ๊ฑด์—์„œ ๋ฐฉ๋ฅ˜ ์„ฑ๋Šฅ์— ๋Œ€ํ•œ ๋‘‘ ๊ฑฐ์น ๊ธฐ์˜ ์˜ํ–ฅ์„ ๋” ์ž˜ ์ดํ•ดํ•˜๊ธฐ ์œ„ํ•ด ๋‹ค์–‘ํ•œ ํ‘œ๋ฉด ๊ฑฐ์น ๊ธฐ์™€ ํ…Œ์ผ์›Œํ„ฐ ์นจ์ˆ˜๋ฅผ ๊ฐ–๋Š” ์ œ๋ฐฉ ๋‘‘ ๋ฒ”๋žŒ์— ๋Œ€ํ•œ ์ˆ˜์น˜ ์—ฐ๊ตฌ๊ฐ€ ์ˆ˜ํ–‰๋˜์—ˆ์Šต๋‹ˆ๋‹ค.

์ž์œ  ๋ฒ”๋žŒ, ์ˆ˜์ค‘ ์ˆ˜์•• ์ ํ”„, ํ…Œ์ผ์›Œํ„ฐ ๊นŠ์ด๊ฐ€ ์ฆ๊ฐ€ํ•˜๋Š” ํ‘œ๋ฉด ์œ ๋™์— ์ด๋ฅด๊ธฐ๊นŒ์ง€ ์œ ๋™ ์ฒด์ œ์˜ ๋ณ€ํ™”๊ฐ€ ์บก์ฒ˜๋ฉ๋‹ˆ๋‹ค. ์œ„์–ด ๊ฑฐ์น ๊ธฐ๋กœ ์ธํ•œ ๋ฐฐ์ถœ ๊ฐ์†Œ๋ฅผ ๋ฐ˜์˜ํ•˜๊ธฐ ์œ„ํ•ด ๊ฑฐ์น ๊ธฐ ๊ณ„์ˆ˜๊ฐ€ ๋„์ž…๋˜์—ˆ์Šต๋‹ˆ๋‹ค.

์กฐ๋„ ๊ณ„์ˆ˜๋Š” ์กฐ๋„ ๋†’์ด์™€ ํ•จ๊ป˜ ๊ฐ์†Œํ•˜๊ณ , ๋˜ํ•œ ํ…Œ์ผ์›Œํ„ฐ ๊นŠ์ด์— ๋”ฐ๋ผ ๋‹ฌ๋ผ์ง€๋ฉฐ, ์„œ๋กœ ๋‹ค๋ฅธ ํ๋ฆ„ ์˜์—ญ ์‚ฌ์ด์˜ ์กฐ๋„ ๋†’์ด์™€ ์กฐ๋„ ๊ณ„์ˆ˜์˜ ๋‹ค์–‘ํ•œ ๊ด€๊ณ„๋ฅผ ๊ฐ•์กฐํ•ฉ๋‹ˆ๋‹ค.

์ด๋Š” ์ž์œ  ๋ฒ”๋žŒ ๋ฐ ์ˆ˜์ค‘ ์ˆ˜์•• ์ ํ”„์— ๋Œ€ํ•ด ์„ ํ˜•์ธ ๋ฐ˜๋ฉด ํ‘œ๋ฉด์— ๋Œ€ํ•ด ์ง€์ˆ˜์ ์ž…๋‹ˆ๋‹ค. ํ๋ฆ„. ๋”ฐ๋ผ์„œ ์›”๋ฅ˜ ๋ฐฉ๋ฅ˜์— ๋Œ€ํ•œ ์›จ์–ด ์กฐ๋„์˜ ์˜ํ–ฅ์€ ์ƒ๋‹นํ•œ ์กฐ๋„ ๋†’์ด์™€ ์ƒ๋‹นํ•œ ๋ฐฉ์ˆ˜ ์นจ์ˆ˜ ํ•˜์—์„œ ๋ฐœ์ƒํ•˜๋Š” ํ‘œ๋ฉด ํ๋ฆ„ ์ฒด์ œ์— ๋Œ€ํ•ด ๋ฌด์‹œํ•  ์ˆ˜ ์—†๋Š” ๊ฒƒ์œผ๋กœ ๋ณด์ž…๋‹ˆ๋‹ค.

๋ฐฉ๋ฅ˜๊ณ„์ˆ˜์™€ ์นจ์ˆ˜ ๋ฐ ์กฐ๋„๊ณ„์ˆ˜์˜ ํ™•๋ฆฝ๋œ ์‹ค์ฆ์‹์€ ๋ฐฉ๋ฅ˜์ˆ˜ ์นจ์ˆ˜์™€ ์ง€ํ‘œ์กฐ๋„๋ฅผ ๋ชจ๋‘ ๊ณ ๋ คํ•œ ์ œ๋ฐฉ๋ณด ์œ„์˜ ๋ฐฉ๋ฅ˜๋Ÿ‰์„ ์˜ˆ์ธกํ•  ์ˆ˜ ์žˆ๊ฒŒ ํ•ฉ๋‹ˆ๋‹ค.

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Figure 4.2 Protrusion length investigation under R1 regime Q=1 mยณ/s with non-constrained BC elevation, 3 cm, 4 cm, 5 cm, 6cm & 7 cm from up to down respectively (grid M3 is employed).

Mathematical Modelling of Air-water flow Structure in Circular Dropshafts

Alternate title: Dairesel DรผลŸรผlรผ Bacalarda Hava-Su KarฤฑลŸฤฑmฤฑnฤฑn Matematiksel Modellemesi
Uรงar, Muhammed.โ€‰ โ€‰Necmettin Erbakan University (Turkey)โ€‰ProQuest Dissertations Publishing, โ€‰2021.โ€‰28840631.

Abstract

Citizensโ€™ daily needs such as; transportation, communication, clean water and sewage are supplied with infrastructure systems. Horizontal and vertical expansion in the cities due to the increase in population leads to serious demand for infrastructural improvements. The infrastructure systems in developing cities are required to be designed in a satisfactory capacity to supply the increasing demand for residential and industrial constructions. The districts having insufficient infrastructure systems inevitably confront heavy traffic, flood, air pollution problems, and also having difficulties with the inadequacy of parking area, clear and potable water, communication. The problems may cause social and health problems over time. At this point, it is wished to emphasize that the primary factor of citycivilization development depends on infrastructural systems and it is meaningful to name the engineering field like civil engineering, literally leads civilization. Dropshafts, commonly used in the urban storm and sewage water systems produced generally circular are used for energy dissipation and flow direction control. Aeration is significant for the working principle of the flow in dropshaft and this study is made mainly for this two-phase (air-water) physics of dropshafts. Chanson showed that aeration and energy dissipation is directly linked to each other (2002), but the influencing factors and the action mechanisms of the factors on the phenomena are not discovered entirely. By the comprehension of the factors, more effective dropshafts will be able to design. This study aims to guide the more comprehensive investigation of design factors using Computational Fluid Dynamics-CFD programs. The reasons for the preference of the programs are the cost-effectiveness of material, workmanship and duration relative to hydraulic modelling. The competence of the inputs, outputs and solution system of the CFD code is validated by the comparison of previous hydraulic modelling results.

Keywords

CFD, Dropshaft, Sewer system, Storm Water System, Two-Phase Flow

Figure 11. Sketch of scour mechanism around USAF under random waves.

Scour Characteristics and Equilibrium Scour Depth Prediction around Umbrella Suction Anchor Foundation under Random Waves

byย Ruigeng Huย 1,Hongjun Liuย 2,Hao Lengย 1,Peng Yuย 3ย andXiuhai Wangย 1,2,*

1College of Environmental Science and Engineering, Ocean University of China, Qingdao 266000, China

2Key Lab of Marine Environment and Ecology (Ocean University of China), Ministry of Education, Qingdao 266000, China

3Qingdao Geo-Engineering Survering Institute, Qingdao 266100, China

*Author to whom correspondence should be addressed.

J. Mar. Sci. Eng. 20219(8), 886; https://doi.org/10.3390/jmse9080886

Received: 6 July 2021 / Revised: 8 August 2021 / Accepted: 13 August 2021 / Published: 17 August 2021

(This article belongs to the Section Ocean Engineering)

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Abstract

A series of numerical simulation were conducted to study the local scour around umbrella suction anchor foundation (USAF) under random waves. In this study, the validation was carried out firstly to verify the accuracy of the present model. Furthermore, the scour evolution and scour mechanism were analyzed respectively. In addition, two revised models were proposed to predict the equilibrium scour depth Seq around USAF. At last, a parametric study was carried out to study the effects of the Froude number Fr and Euler number Eu for the Seq. The results indicate that the present numerical model is accurate and reasonable for depicting the scour morphology under random waves. The revised Raaijmakersโ€™s model shows good agreement with the simulating results of the present study when KCs,p < 8. The predicting results of the revised stochastic model are the most favorable for n = 10 when KCrms,a < 4. The higher Fr and Eu both lead to the more intensive horseshoe vortex and larger Seq.

Keywords: 

scournumerical investigationrandom wavesequilibrium scour depthKC number

1. Introduction

The rapid expansion of cities tends to cause social and economic problems, such as environmental pollution and traffic jam. As a kind of clean energy, offshore wind power has developed rapidly in recent years. The foundation of offshore wind turbine (OWT) supports the upper tower, and suffers the cyclic loading induced by waves, tides and winds, which exerts a vital influence on the OWT system. The types of OWT foundation include the fixed and floating foundation, and the fixed foundation was used usually for nearshore wind turbine. After the construction of fixed foundation, the hydrodynamic field changes in the vicinity of the foundation, leading to the horseshoe vortex formation and streamline compression at the upside and sides of foundation respectively [1,2,3,4]. As a result, the neighboring soil would be carried away by the shear stress induced by vortex, and the scour hole would emerge in the vicinity of foundation. The scour holes increase the cantilever length, and weaken the lateral bearing capacity of foundation [5,6,7,8,9]. Moreover, the natural frequency of OWT system increases with the increase of cantilever length, causing the resonance occurs when the system natural frequency equals the wave or wind frequency [10,11,12]. Given that, an innovative foundation called umbrella suction anchor foundation (USAF) has been designed for nearshore wind power. The previous studies indicated the USAF was characterized by the favorable lateral bearing capacity with the low cost [6,13,14]. The close-up of USAF is shown in Figure 1, and it includes six parts: 1-interal buckets, 2-external skirt, 3-anchor ring, 4-anchor branch, 5-supporting rod, 6-telescopic hook. The detailed description and application method of USAF can be found in reference [13].

Jmse 09 00886 g001 550

Figure 1. The close-up of umbrella suction anchor foundation (USAF).

Numerical and experimental investigations of scour around OWT foundation under steady currents and waves have been extensively studied by many researchers [1,2,15,16,17,18,19,20,21,22,23,24]. The seabed scour can be classified as two types according to Shields parameter ฮธ, i.e., clear bed scour (ฮธ < ฮธcr) or live bed scour (ฮธ > ฮธcr). Due to the set of foundation, the adverse hydraulic pressure gradient exists at upstream foundation edges, resulting in the streamline separation between boundary layer flow and seabed. The separating boundary layer ascended at upstream anchor edges and developed into the horseshoe vortex. Then, the horseshoe vortex moved downstream gradually along the periphery of the anchor, and the vortex shed off continually at the lee-side of the anchor, i.e., wake vortex. The core of wake vortex is a negative pressure center, liking a vacuum cleaner. Hence, the soil particles were swirled into the negative pressure core and carried away by wake vortexes. At the same time, the onset of scour at rear side occurred. Finally, the wake vortex became downflow when the turbulence energy could not support the survival of wake vortex. According to Tavouktsoglou et al. [25], the scale of pile wall boundary layer is proportional to 1/ln(Rd) (Rd is pile Reynolds), which means the turbulence intensity induced by the flow-structure interaction would decrease with Rd increases, but the effects of Rd can be neglected only if the flow around the foundation is fully turbulent [26]. According to previous studies [1,15,27,28,29,30,31,32], the scour development around pile foundation under waves was significantly influenced by Shields parameter ฮธ and KC number simultaneously (calculated by Equation (1)). Sand ripples widely existed around pile under waves in the case of live bed scour, and the scour morphology is related with ฮธ and KC. Compared with ฮธKC has a greater influence on the scour morphology [21,27,28]. The influence mechanism of KC on the scour around the pile is reflected in two aspects: the horseshoe vortex at upstream and wake vortex shedding at downstream.

KC=UwmTD๏ฟฝ๏ฟฝ=๏ฟฝwm๏ฟฝ๏ฟฝ(1)

where, Uwm is the maximum velocity of the undisturbed wave-induced oscillatory flow at the sea bottom above the wave boundary layer, T is wave period, and D is pile diameter.

There are two prerequisites to satisfy the formation of horseshoe vortex at upstream pile edges: (1) the incoming flow boundary layer with sufficient thickness and (2) the magnitude of upstream adverse pressure gradient making the boundary layer separating [1,15,16,18,20]. The smaller KC results the lower adverse pressure gradient, and the boundary layer cannot separate, herein, there is almost no horseshoe vortex emerging at upside of pile. Sumer et al. [1,15] carried out several sets of wave flume experiments under regular and irregular waves respectively, and the experiment results show that there is no horseshoe vortex when KC is less than 6. While the scale and lifespan of horseshoe vortex increase evidently with the increase of KC when KC is larger than 6. Moreover, the wake vortex contributes to the scour at lee-side of pile. Similar with the case of horseshoe vortex, there is no wake vortex when KC is less than 6. The wake vortex is mainly responsible for scour around pile when KC is greater than 6 and less than O(100), while horseshoe vortex controls scour nearly when KC is greater than O(100).

Sumer et al. [1] found that the equilibrium scour depth was nil around pile when KC was less than 6 under regular waves for live bed scour, while the equilibrium scour depth increased with the increase of KC. Based on that, Sumer proposed an equilibrium scour depth predicting equation (Equation (2)). Carreiras et al. [33] revised Sumerโ€™s equation with m = 0.06 for nonlinear waves. Different with the findings of Sumer et al. [1] and Carreiras et al. [33], Corvaro et al. [21] found the scour still occurred for KC โ‰ˆ 4, and proposed the revised equilibrium scour depth predicting equation (Equation (3)) for KC > 4.

Rudolph and Bos [2] conducted a series of wave flume experiments to investigate the scour depth around monopile under waves only, waves and currents combined respectively, indicting KC was one of key parameters in influencing equilibrium scour depth, and proposed the equilibrium scour depth predicting equation (Equation (4)) for low KC (1 < KC < 10). Through analyzing the extensive data from published literatures, Raaijmakers and Rudolph [34] developed the equilibrium scour depth predicting equation (Equation (5)) for low KC, which was suitable for waves only, waves and currents combined. Khalfin [35] carried out several sets of wave flume experiments to study scour development around monopile, and proposed the equilibrium scour depth predicting equation (Equation (6)) for low KC (0.1 < KC < 3.5). Different with above equations, the Khalfinโ€™s equation considers the Shields parameter ฮธ and KC number simultaneously in predicting equilibrium scour depth. The flow reversal occurred under through in one wave period, so sand particles would be carried away from lee-side of pile to upside, resulting in sand particles backfilled into the upstream scour hole [20,29]. Considering the backfilling effects, Zanke et al. [36] proposed the equilibrium scour depth predicting equation (Equation (7)) around pile by theoretical analysis, and the equation is suitable for the whole range of KC number under regular waves and currents combined.

S/D=1.3(1โˆ’exp([โˆ’m(KCโˆ’6)])๏ฟฝ/๏ฟฝ=1.3(1โˆ’exp(โˆ’๏ฟฝ(๏ฟฝ๏ฟฝโˆ’6))(2)

where, m = 0.03 for linear waves.

S/D=1.3(1โˆ’exp([โˆ’0.02(KCโˆ’4)])๏ฟฝ/๏ฟฝ=1.3(1โˆ’exp(โˆ’0.02(๏ฟฝ๏ฟฝโˆ’4))(3)

S/D=1.3ฮณKwaveKhw๏ฟฝ/๏ฟฝ=1.3๏ฟฝ๏ฟฝwave๏ฟฝโ„Žw(4)

where, ฮณ is safety factor, depending on design process, typically ฮณ = 1.5, Kwave is correction factor considering wave action, Khw is correction factor considering water depth.

S/D=1.5[tanh(hwD)]KwaveKhw๏ฟฝ/๏ฟฝ=1.5tanh(โ„Žw๏ฟฝ)๏ฟฝwave๏ฟฝโ„Žw(5)

where, hw is water depth.

S/D=0.0753(ฮธฮธcrโˆ’โˆ’โˆ’โˆšโˆ’0.5)0.69KC0.68๏ฟฝ/๏ฟฝ=0.0753(๏ฟฝ๏ฟฝcrโˆ’0.5)0.69๏ฟฝ๏ฟฝ0.68(6)

where, ฮธ is shields parameter, ฮธcr is critical shields parameter.

S/D=2.5(1โˆ’0.5u/uc)xrelxrel=xeff/(1+xeff)xeff=0.03(1โˆ’0.35ucr/u)(KCโˆ’6)โŽซโŽญโŽฌโŽชโŽช๏ฟฝ/๏ฟฝ=2.5(1โˆ’0.5๏ฟฝ/๏ฟฝ๏ฟฝ)๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ=๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ/(1+๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ)๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ=0.03(1โˆ’0.35๏ฟฝcr/๏ฟฝ)(๏ฟฝ๏ฟฝโˆ’6)(7)

where, u is near-bed orbital velocity amplitude, uc is critical velocity corresponding the onset of sediment motion.

S/D=1.3{1โˆ’exp[โˆ’0.03(KC2lnn+36)1/2โˆ’6]}๏ฟฝ/๏ฟฝ=1.31โˆ’expโˆ’0.03(๏ฟฝ๏ฟฝ2ln๏ฟฝ+36)1/2โˆ’6(8)

where, n is the 1/nโ€™th highest wave for random waves

For predicting equilibrium scour depth under irregular waves, i.e., random waves, Sumer and Fredsรธe [16] found itโ€™s suitable to take Equation (2) to predict equilibrium scour depth around pile under random waves with the root-mean-square (RMS) value of near-bed orbital velocity amplitude Um and peak wave period TP to calculate KC. Khalfin [35] recommended the RMS wave height Hrms and peak wave period TP were used to calculate KC for Equation (6). References [37,38,39,40] developed a series of stochastic theoretical models to predict equilibrium scour depth around pile under random waves, nonlinear random waves plus currents respectively. The stochastic approach thought the 1/nโ€™th highest wave were responsible for scour in vicinity of pile under random waves, and the KC was calculated in Equation (8) with Um and mean zero-crossing wave period Tz. The results calculated by Equation (8) agree well with experimental values of Sumer and Fredsรธe [16] if the 1/10โ€ฒth highest wave was used. To authorโ€™s knowledge, the stochastic approach proposed by Myrhaug and Rue [37] is the only theoretical model to predict equilibrium scour depth around pile under random waves for the whole range of KC number in published documents. Other methods of predicting scour depth under random waves are mainly originated from the equation for regular waves-only, waves and currents combined, which are limited to the large KC number, such as KC > 6 for Equation (2) and KC > 4 for Equation (3) respectively. However, situations with relatively low KC number (KC < 4) often occur in reality, for example, monopile or suction anchor for OWT foundations in ocean environment. Moreover, local scour around OWT foundations under random waves has not yet been investigated fully. Therefore, further study are still needed in the aspect of scour around OWT foundations with low KC number under random waves. Given that, this study presents the scour sediment model around umbrella suction anchor foundation (USAF) under random waves. In this study, a comparison of equilibrium scour depth around USAF between this present numerical models and the previous theoretical models and experimental results was presented firstly. Then, this study gave a comprehensive analysis for the scour mechanisms around USAF. After that, two revised models were proposed according to the model of Raaijmakers and Rudolph [34] and the stochastic model developed by Myrhaug and Rue [37] respectively to predict the equilibrium scour depth. Finally, a parametric study was conducted to study the effects of the Froude number (Fr) and Euler number (Eu) to equilibrium scour depth respectively.

2. Numerical Method

2.1. Governing Equations of Flow

The following equations adopted in present model are already available in Flow 3D software. The authors used these theoretical equations to simulate scour in random waves without modification. The incompressible viscous fluid motion satisfies the Reynolds-averaged Navier-Stokes (RANS) equation, so the present numerical model solves RANS equations:

โˆ‚uโˆ‚t+1VF(uAxโˆ‚uโˆ‚x+vAyโˆ‚uโˆ‚y+wAzโˆ‚uโˆ‚z)=โˆ’1ฯfโˆ‚pโˆ‚x+Gx+fxโˆ‚๏ฟฝโˆ‚๏ฟฝ+1๏ฟฝ๏ฟฝ(๏ฟฝ๏ฟฝ๏ฟฝโˆ‚๏ฟฝโˆ‚๏ฟฝ+๏ฟฝ๏ฟฝ๏ฟฝโˆ‚๏ฟฝโˆ‚๏ฟฝ+๏ฟฝ๏ฟฝ๏ฟฝโˆ‚๏ฟฝโˆ‚๏ฟฝ)=โˆ’1๏ฟฝfโˆ‚๏ฟฝโˆ‚๏ฟฝ+๏ฟฝ๏ฟฝ+๏ฟฝ๏ฟฝ(9)

โˆ‚vโˆ‚t+1VF(uAxโˆ‚vโˆ‚x+vAyโˆ‚vโˆ‚y+wAzโˆ‚vโˆ‚z)=โˆ’1ฯfโˆ‚pโˆ‚y+Gy+fyโˆ‚๏ฟฝโˆ‚๏ฟฝ+1๏ฟฝ๏ฟฝ(๏ฟฝ๏ฟฝ๏ฟฝโˆ‚๏ฟฝโˆ‚๏ฟฝ+๏ฟฝ๏ฟฝ๏ฟฝโˆ‚๏ฟฝโˆ‚๏ฟฝ+๏ฟฝ๏ฟฝ๏ฟฝโˆ‚๏ฟฝโˆ‚๏ฟฝ)=โˆ’1๏ฟฝfโˆ‚๏ฟฝโˆ‚๏ฟฝ+๏ฟฝ๏ฟฝ+๏ฟฝ๏ฟฝ(10)

โˆ‚wโˆ‚t+1VF(uAxโˆ‚wโˆ‚x+vAyโˆ‚wโˆ‚y+wAzโˆ‚wโˆ‚z)=โˆ’1ฯfโˆ‚pโˆ‚z+Gz+fzโˆ‚๏ฟฝโˆ‚๏ฟฝ+1๏ฟฝ๏ฟฝ(๏ฟฝ๏ฟฝ๏ฟฝโˆ‚๏ฟฝโˆ‚๏ฟฝ+๏ฟฝ๏ฟฝ๏ฟฝโˆ‚๏ฟฝโˆ‚๏ฟฝ+๏ฟฝ๏ฟฝ๏ฟฝโˆ‚๏ฟฝโˆ‚๏ฟฝ)=โˆ’1๏ฟฝfโˆ‚๏ฟฝโˆ‚๏ฟฝ+๏ฟฝ๏ฟฝ+๏ฟฝ๏ฟฝ(11)

where, VF is the volume fraction; uv, and w are the velocity components in xyz direction respectively with Cartesian coordinates; Ai is the area fraction; ฯf is the fluid density, fi is the viscous fluid acceleration, Gi is the fluid body acceleration (i = xyz).

2.2. Turbulent Model

The turbulence closure is available by the turbulent model, such as one-equation, the one-equation k-ฮต model, the standard k-ฮต model, RNG k-ฮต turbulent model and large eddy simulation (LES) model. The LES model requires very fine mesh grid, so the computational time is large, which hinders the LES model application in engineering. The RNG k-ฮต model can reduce computational time greatly with high accuracy in the near-wall region. Furthermore, the RNG k-ฮต model computes the maximum turbulent mixing length dynamically in simulating sediment scour model. Therefore, the RNG k-ฮต model was adopted to study the scour around anchor under random waves [41,42].

โˆ‚kTโˆ‚T+1VF(uAxโˆ‚kTโˆ‚x+vAyโˆ‚kTโˆ‚y+wAzโˆ‚kTโˆ‚z)=PT+GT+DiffkTโˆ’ฮตkTโˆ‚๏ฟฝ๏ฟฝโˆ‚๏ฟฝ+1๏ฟฝ๏ฟฝ(๏ฟฝ๏ฟฝ๏ฟฝโˆ‚๏ฟฝ๏ฟฝโˆ‚๏ฟฝ+๏ฟฝ๏ฟฝ๏ฟฝโˆ‚๏ฟฝ๏ฟฝโˆ‚๏ฟฝ+๏ฟฝ๏ฟฝ๏ฟฝโˆ‚๏ฟฝ๏ฟฝโˆ‚๏ฟฝ)=๏ฟฝ๏ฟฝ+๏ฟฝ๏ฟฝ+๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝโˆ’๏ฟฝ๏ฟฝ๏ฟฝ(12)

โˆ‚ฮตTโˆ‚T+1VF(uAxโˆ‚ฮตTโˆ‚x+vAyโˆ‚ฮตTโˆ‚y+wAzโˆ‚ฮตTโˆ‚z)=CDIS1ฮตTkT(PT+CDIS3GT)+Diffฮตโˆ’CDIS2ฮต2TkTโˆ‚๏ฟฝ๏ฟฝโˆ‚๏ฟฝ+1๏ฟฝ๏ฟฝ(๏ฟฝ๏ฟฝ๏ฟฝโˆ‚๏ฟฝ๏ฟฝโˆ‚๏ฟฝ+๏ฟฝ๏ฟฝ๏ฟฝโˆ‚๏ฟฝ๏ฟฝโˆ‚๏ฟฝ+๏ฟฝ๏ฟฝ๏ฟฝโˆ‚๏ฟฝ๏ฟฝโˆ‚๏ฟฝ)=๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ1๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ(๏ฟฝ๏ฟฝ+๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ3๏ฟฝ๏ฟฝ)+๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝโˆ’๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ2๏ฟฝ๏ฟฝ2๏ฟฝ๏ฟฝ(13)

where, kT is specific kinetic energy involved with turbulent velocity, GT is the turbulent energy generated by buoyancy; ฮตT is the turbulent energy dissipating rate, PT is the turbulent energy, Diffฮต and DiffkT are diffusion terms associated with VFAiCDIS1CDIS2 and CDIS3 are dimensionless parameters, and CDIS1CDIS3 have default values of 1.42, 0.2 respectively. CDIS2 can be obtained from PT and kT.

2.3. Sediment Scour Model

The sand particles may suffer four processes under waves, i.e., entrainment, bed load transport, suspended load transport, and deposition, so the sediment scour model should depict the above processes efficiently. In present numerical simulation, the sediment scour model includes the following aspects:

2.3.1. Entrainment and Deposition

The combination of entrainment and deposition determines the net scour rate of seabed in present sediment scour model. The entrainment lift velocity of sand particles was calculated as [43]:

ulift,i=ฮฑinsd0.3โˆ—(ฮธโˆ’ฮธcr)1.5โˆฅgโˆฅdi(ฯiโˆ’ฯf)ฯfโˆ’โˆ’โˆ’โˆ’โˆ’โˆ’โˆ’โˆ’โˆ’โˆ’โˆ’โˆ’โˆš๏ฟฝlift,i=๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ*0.3(๏ฟฝโˆ’๏ฟฝcr)1.5๏ฟฝ๏ฟฝ๏ฟฝ(๏ฟฝ๏ฟฝโˆ’๏ฟฝf)๏ฟฝf(14)

where, ฮฑi is the entrainment parameter, ns is the outward point perpendicular to the seabed, d* is the dimensionless diameter of sand particles, which was calculated by Equation (15), ฮธcr is the critical Shields parameter, g is the gravity acceleration, di is the diameter of sand particles, ฯi is the density of seabed species.

dโˆ—=di(โˆฅgโˆฅฯf(ฯiโˆ’ฯf)ฮผ2f)1/3๏ฟฝ*=๏ฟฝ๏ฟฝ(๏ฟฝ๏ฟฝf(๏ฟฝ๏ฟฝโˆ’๏ฟฝf)๏ฟฝf2)1/3(15)

where ฮผf is the fluid dynamic viscosity.

In Equation (14), the entrainment parameter ฮฑi confirms the rate at which sediment erodes when the given shear stress is larger than the critical shear stress, and the recommended value 0.018 was adopted according to the experimental data of Mastbergen and Von den Berg [43]. ns is the outward pointing normal to the seabed interface, and ns = (0,0,1) according to the Cartesian coordinates used in present numerical model.

The shields parameter was obtained from the following equation:

ฮธ=U2f,m(ฯi/ฯfโˆ’1)gd50๏ฟฝ=๏ฟฝf,m2(๏ฟฝ๏ฟฝ/๏ฟฝfโˆ’1)๏ฟฝ๏ฟฝ50(16)

where, Uf,m is the maximum value of the near-bed friction velocity; d50 is the median diameter of sand particles. The detailed calculation procedure of ฮธ was available in Soulsby [44].

The critical shields parameter ฮธcr was obtained from the Equation (17) [44]

ฮธcr=0.31+1.2dโˆ—+0.055[1โˆ’exp(โˆ’0.02dโˆ—)]๏ฟฝcr=0.31+1.2๏ฟฝ*+0.0551โˆ’exp(โˆ’0.02๏ฟฝ*)(17)

The sand particles begin to deposit on seabed when the turbulence energy weaken and cannโ€™t support the particles suspending. The setting velocity of the particles was calculated from the following equation [44]:

usettling,i=ฮฝfdi[(10.362+1.049d3โˆ—)0.5โˆ’10.36]๏ฟฝsettling,๏ฟฝ=๏ฟฝf๏ฟฝ๏ฟฝ(10.362+1.049๏ฟฝ*3)0.5โˆ’10.36(18)

where ฮฝf is the fluid kinematic viscosity.

2.3.2. Bed Load Transport

This is called bed load transport when the sand particles roll or bounce over the seabed and always have contact with seabed. The bed load transport velocity was computed by [45]:

ubedload,i=qb,iฮดicb,ifb๏ฟฝbedload,๏ฟฝ=๏ฟฝb,๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝb,๏ฟฝ๏ฟฝb(19)

where, qb,i is the bed load transport rate, which was obtained from Equation (20), ฮดi is the bed load thickness, which was calculated by Equation (21), cb,i is the volume fraction of sand i in the multiple species, fb is the critical packing fraction of the seabed.

qb,i=8[โˆฅgโˆฅ(ฯiโˆ’ฯfฯf)d3i]1/2๏ฟฝb,๏ฟฝ=8๏ฟฝ(๏ฟฝ๏ฟฝโˆ’๏ฟฝf๏ฟฝf)๏ฟฝ๏ฟฝ31/2(20)

ฮดi=0.3d0.7โˆ—(ฮธฮธcrโˆ’1)0.5di๏ฟฝ๏ฟฝ=0.3๏ฟฝ*0.7(๏ฟฝ๏ฟฝcrโˆ’1)0.5๏ฟฝ๏ฟฝ(21)

2.3.3. Suspended Load Transport

Through the following transport equation, the suspended sediment concentration could be acquired.

โˆ‚Cs,iโˆ‚t+โˆ‡(us,iCs,i)=โˆ‡โˆ‡(DfCs,i)โˆ‚๏ฟฝs,๏ฟฝโˆ‚๏ฟฝ+โˆ‡(๏ฟฝs,๏ฟฝ๏ฟฝs,๏ฟฝ)=โˆ‡โˆ‡(๏ฟฝf๏ฟฝs,๏ฟฝ)(22)

where, Cs,i is the suspended sand particles mass concentration of sand i in the multiple species, us,i is the sand particles velocity of sand iDf is the diffusivity.

The velocity of sand i in the multiple species could be obtained from the following equation:

us,i=uยฏยฏ+usettling,ics,i๏ฟฝs,๏ฟฝ=๏ฟฝยฏ+๏ฟฝsettling,๏ฟฝ๏ฟฝs,๏ฟฝ(23)

where, uยฏ๏ฟฝยฏ is the velocity of mixed fluid-particles, which can be calculated by the RANS equation with turbulence model, cs,i is the suspended sand particles volume concentration, which was computed from Equation (24).

cs,i=Cs,iฯi๏ฟฝs,๏ฟฝ=๏ฟฝs,๏ฟฝ๏ฟฝ๏ฟฝ(24)

3. Model Setup

The seabed-USAF-wave three-dimensional scour numerical model was built using Flow-3D software. As shown in Figure 2, the model includes sandy seabed, USAF model, sea water, two baffles and porous media. The dimensions of USAF are shown in Table 1. The sandy bed (210 m in length, 30 m in width and 11 m in height) is made up of uniform fine sand with median diameter d50 = 0.041 cm. The USAF model includes upper steel tube with the length of 20 m, which was installed in the middle of seabed. The location of USAF is positioned at 140 m from the upstream inflow boundary and 70 m from the downstream outflow boundary. Two baffles were installed at two ends of seabed. In order to eliminate the wave reflection basically, the porous media was set at the outflow side on the seabed.

Jmse 09 00886 g002 550

Figure 2. (a) The sketch of seabed-USAF-wave three-dimensional model; (b) boundary condation:Wv-wave boundary, S-symmetric boundary, O-outflow boundary; (c) USAF model.

Table 1. Numerical simulating cases.

Table

3.1. Mesh Geometric Dimensions

In the simulation of the scour under the random waves, the model includes the umbrella suction anchor foundation, seabed and fluid. As shown in Figure 3, the model mesh includes global mesh grid and nested mesh grid, and the total number of grids is 1,812,000. The basic procedure for building mesh grid consists of two steps. Step 1: Divide the global mesh using regular hexahedron with size of 0.6 ร— 0.6. The global mesh area is cubic box, embracing the seabed and whole fluid volume, and the dimensions are 210 m in length, 30 m in width and 32 m in height. The details of determining the grid size can see the following mesh sensitivity section. Step 2: Set nested fine mesh grid in vicinity of the USAF with size of 0.3 ร— 0.3 so as to shorten the computation cost and improve the calculation accuracy. The encryption range is โˆ’15 m to 15 m in x direction, โˆ’15 m to 15 m in y direction and 0 m to 32 m in z direction, respectively. In order to accurately capture the free-surface dynamics, such as the fluid-air interface, the volume of fluid (VOF) method was adopted for tracking the free water surface. One specific algorithm called FAVORTM (Fractional Area/Volume Obstacle Representation) was used to define the fractional face areas and fractional volumes of the cells which are open to fluid flow.

Jmse 09 00886 g003 550

Figure 3. The sketch of mesh grid.

3.2. Boundary Conditions

As shown in Figure 2, the initial fluid length is 210 m as long as seabed. A wave boundary was specified at the upstream offshore end. The details of determining the random wave spectrum can see the following wave parameters section. The outflow boundary was set at the downstream onshore end. The symmetry boundary was used at the top and two sides of the model. The symmetric boundaries were the better strategy to improve the computation efficiency and save the calculation cost [46]. At the seabed bottom, the wall boundary was adopted, which means the u = v = w= 0. Besides, the upper steel tube of USAF was set as no-slip condition.

3.3. Wave Parameters

The random waves with JONSWAP wave spectrum were used for all simulations as realistic representation of offshore conditions. The unidirectional JONSWAP frequency spectrum was described as [47]:

S(ฯ‰)=ฮฑg2ฯ‰5exp[โˆ’54(ฯ‰pฯ‰)4]ฮณexp[โˆ’(ฯ‰โˆ’ฯ‰p)22ฯƒ2ฯ‰2p]๏ฟฝ(๏ฟฝ)=๏ฟฝ๏ฟฝ2๏ฟฝ5expโˆ’54(๏ฟฝp๏ฟฝ)4๏ฟฝexpโˆ’(๏ฟฝโˆ’๏ฟฝp)22๏ฟฝ2๏ฟฝp2(25)

where, ฮฑ is wave energy scale parameter, which is calculated by Equation (26), ฯ‰ is frequency, ฯ‰p is wave spectrum peak frequency, which can be obtained from Equation (27). ฮณ is wave spectrum peak enhancement factor, in this study ฮณ = 3.3. ฯƒ is spectral width factor, ฯƒ equals 0.07 for ฯ‰ โ‰ค ฯ‰p and 0.09 for ฯ‰ > ฯ‰p respectively.

ฮฑ=0.0076(gXU2)โˆ’0.22๏ฟฝ=0.0076(๏ฟฝ๏ฟฝ๏ฟฝ2)โˆ’0.22(26)

ฯ‰p=22(gU)(gXU2)โˆ’0.33๏ฟฝp=22(๏ฟฝ๏ฟฝ)(๏ฟฝ๏ฟฝ๏ฟฝ2)โˆ’0.33(27)

where, X is fetch length, U is average wind velocity at 10 m height from mean sea level.

In present numerical model, the input key parameters include X and U for wave boundary with JONSWAP wave spectrum. The objective wave height and period are available by different combinations of X and U. In this study, we designed 9 cases with different wave heights, periods and water depths for simulating scour around USAF under random waves (see Table 2). For random waves, the wave steepness ฮต and Ursell number Ur were acquired form Equations (28) and (29) respectively

ฮต=2ฯ€gHsT2a๏ฟฝ=2๏ฟฝ๏ฟฝ๏ฟฝs๏ฟฝa2(28)

Ur=Hsk2h3w๏ฟฝr=๏ฟฝs๏ฟฝ2โ„Žw3(29)

where, Hs is significant wave height, Ta is average wave period, k is wave number, hw is water depth. The Shield parameter ฮธ satisfies ฮธ > ฮธcr for all simulations in current study, indicating the live bed scour prevails.

Table 2. Numerical simulating cases.

Table

3.4. Mesh Sensitivity

In this section, a mesh sensitivity analysis was conducted to investigate the influence of mesh grid size to results and make sure the calculation is mesh size independent and converged. Three mesh grid size were chosen: Mesh 1โ€”global mesh grid size of 0.75 ร— 0.75, nested fine mesh grid size of 0.4 ร— 0.4, and total number of grids 1,724,000, Mesh 2โ€”global mesh grid size of 0.6 ร— 0.6, nested fine mesh grid size of 0.3 ร— 0.3, and total number of grids 1,812,000, Mesh 3โ€”global mesh grid size of 0.4 ร— 0.4, nested fine mesh grid size of 0.2 ร— 0.2, and total number of grids 1,932,000. The near-bed shear velocity U* is an important factor for influencing scour process [1,15], so U* at the position of (4,0,11.12) was evaluated under three mesh sizes. As the Figure 4 shown, the maximum error of shear velocity โˆ†U*1,2 is about 39.8% between the mesh 1 and mesh 2, and 4.8% between the mesh 2 and mesh 3. According to the mesh sensitivity criterion adopted by Pang et al. [48], itโ€™s reasonable to think the results are mesh size independent and converged with mesh 2. Additionally, the present model was built according to prototype size, and the mesh size used in present model is larger than the mesh size adopted by Higueira et al. [49] and Corvaro et al. [50]. If we choose the smallest cell size, it will take too much time. For example, the simulation with Mesh3 required about 260 h by using a computer with Intel Xeon Scalable Gold 4214 CPU @24 Cores, 2.2 GHz and 64.00 GB RAM. Therefore, in this case, considering calculation accuracy and computation efficiency, the mesh 2 was chosen for all the simulation in this study.

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Figure 4. Comparison of near-bed shear velocity U* with different mesh grid size.

The nested mesh block was adopted for seabed in vicinity of the USAF, which was overlapped with the global mesh block. When two mesh blocks overlap each other, the governing equations are by default solved on the mesh block with smaller average cell size (i.e., higher grid resolution). It is should be noted that the Flow 3D software used the moving mesh captures the scour evolution and automatically adjusts the time step size to be as large as possible without exceeding any of the stability limits, affecting accuracy, or unduly increasing the effort required to enforce the continuity condition [51].

3.5. Model Validation

In order to verify the reliability of the present model, the results of present study were compared with the experimental data of Khosronejad et al. [52]. The experiment was conducted in an open channel with a slender vertical pile under unidirectional currents. The comparison of scour development between the present results and the experimental results is shown in Figure 5. The Figure 5 reveals that the present results agree well with the experimental data of Khosronejad et al. [52]. In the first stage, the scour depth increases rapidly. After that, the scour depth achieves a maximum value gradually. The equilibrium scour depth calculated by the present model is basically corresponding with the experimental results of Khosronejad et al. [52], although scour depth in the present model is slightly larger than the experimental results at initial stage.

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Figure 5. Comparison of time evolution of scour between the present study and Khosronejad et al. [52], Petersen et al. [17].

Secondly, another comparison was further conducted between the results of present study and the experimental data of Petersen et al. [17]. The experiment was carried out in a flume with a circular vertical pile in combined waves and current. Figure 4 shows a comparison of time evolution of scour depth between the simulating and the experimental results. As Figure 5 indicates, the scour depth in this study has good overall agreement with the experimental results proposed in Petersen et al. [17]. The equilibrium scour depth calculated by the present model is 0.399 m, which equals to the experimental value basically. Overall, the above verifications prove the present model is accurate and capable in dealing with sediment scour under waves.

In addition, in order to calibrate and validate the present model for hydrodynamic parameters, the comparison of water surface elevation was carried out with laboratory experiments conducted by Stahlmann [53] for wave gauge No. 3. The Figure 6 depicts the surface wave profiles between experiments and numerical model results. The comparison indicates that there is a good agreement between the model results and experimental values, especially the locations of wave crest and trough. Comparison of the surface elevation instructs the present model has an acceptable relative error, and the model is a calibrated in terms of the hydrodynamic parameters.

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Figure 6. Comparison of surface elevation between the present study and Stahlmann [53].

Finally, another comparison was conducted for equilibrium scour depth or maximum scour depth under random waves with the experimental data of Sumer and Fredsรธe [16] and Schendel et al. [22]. The Figure 7 shows the comparison between the numerical results and experimental data of Run01, Run05, Run21 and Run22 in Sumer and Fredsรธe [16] and test A05 and A09 in Schendel et al. [22]. As shown in Figure 7, the equilibrium scour depth or maximum scour depth distributed within the ยฑ30 error lines basically, meaning the reliability and accuracy of present model for predicting equilibrium scour depth around foundation in random waves. However, compared with the experimental values, the present model overestimated the equilibrium scour depth generally. Given that, a calibration for scour depth was carried out by multiplying the mean reduced coefficient 0.85 in following section.

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Figure 7. Comparison of equilibrium (or maximum) scour depth between the present study and Sumer and Fredsรธe [16], Schendel et al. [22].

Through the various examination for hydrodynamic and morphology parameters, it can be concluded that the present model is a validated and calibrated model for scour under random waves. Thus, the present numerical model would be utilized for scour simulation around foundation under random waves.

4. Numerical Results and Discussions

4.1. Scour Evolution

Figure 8 displays the scour evolution for case 1โ€“9. As shown in Figure 8a, the scour depth increased rapidly at the initial stage, and then slowed down at the transition stage, which attributes to the backfilling occurred in scour holes under live bed scour condition, resulting in the net scour decreasing. Finally, the scour reached the equilibrium state when the amount of sediment backfilling equaled to that of scouring in the scour holes, i.e., the net scour transport rate was nil. Sumer and Fredsรธe [16] proposed the following formula for the scour development under waves

St=Seq(1โˆ’exp(โˆ’t/Tc))๏ฟฝt=๏ฟฝeq(1โˆ’exp(โˆ’๏ฟฝ/๏ฟฝc))(30)

where Tc is time scale of scour process.

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Figure 8. Time evolution of scour for case 1โ€“9: (a) Case 1โ€“5; (b) Case 6โ€“9.

The computing time is 3600 s and the scour development curves in Figure 8 kept fluctuating, meaning itโ€™s still not in equilibrium scour stage in these cases. According to Sumer and Fredsรธe [16], the equilibrium scour depth can be acquired by fitting the data with Equation (30). From Figure 8, it can be seen that the scour evolution obtained from Equation (30) is consistent with the present study basically at initial stage, but the scour depth predicted by Equation (30) developed slightly faster than the simulating results and the Equation (30) overestimated the scour depth to some extent. Overall, the whole tendency of the results calculated by Equation (30) agrees well with the simulating results of the present study, which means the Equation (30) is applicable to depict the scour evolution around USAF under random waves.

4.2. Scour Mechanism under Random Waves

The scour morphology and scour evolution around USAF are similar under random waves in case 1~9. Taking case 7 as an example, the scour morphology is shown in Figure 9.

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Figure 9. Scour morphology under different times for case 7.

From Figure 9, at the initial stage (t < 1200 s), the scour occurred at upstream foundation edges between neighboring anchor branches. The maximum scour depth appeared at the lee-side of the USAF. Correspondingly, the sediments deposited at the periphery of the USAF, and the location of the maximum accretion depth was positioned at an angle of about 45ยฐ symmetrically with respect to the wave propagating direction in the lee-side of the USAF. After that, when t > 2400 s, the location of the maximum scour depth shifted to the upside of the USAF at an angle of about 45ยฐ with respect to the wave propagating direction.

According to previous studies [1,15,16,19,30,31], the horseshoe vortex, streamline compression and wake vortex shedding were responsible for scour around foundation. The Figure 10 displays the distribution of flow velocity in vicinity of foundation, which reflects the evolving processes of horseshoe vertex.

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Figure 10. Velocity profile around USAF: (a) Flow runup and down stream at upstream anchor edges; (b) Horseshoe vortex at upstream anchor edges; (c) Flow reversal during wave through stage at lee side.

As shown in Figure 10, the inflow tripped to the upstream edges of the USAF and it was blocked by the upper tube of USAF. Then, the downflow formed the horizontal axis clockwise vortex and rolled on the seabed bypassing the tube, that is, the horseshoe vortex (Figure 11). The Figure 12 displays the turbulence intensity around the tube on the seabed. From Figure 12, it can be seen that the turbulence intensity was high-intensity with respect to the region of horseshoe vortex. This phenomenon occurred because of drastic water flow momentum exchanging in the horseshoe vortex. As a result, it created the prominent shear stress on the seabed, causing the local scour at the upstream edges of USAF. Besides, the horseshoe vortex moved downstream gradually along the periphery of the tube and the wake vortex shed off continually at the lee-side of the USAF, i.e., wake vortex.

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Figure 11. Sketch of scour mechanism around USAF under random waves.

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Figure 12. Turbulence intensity: (a) Turbulence intensity of horseshoe vortex; (b) Turbulence intensity of wake vortex; (c) Turbulence intensity of accretion area.

The core of wake vortex is a negative pressure center, liking a vacuum cleaner [11,42]. Hence, the soil particles were swirled into the negative pressure core and carried away by wake vortex. At the same time, the onset of scour at rear side occurred. Finally, the wake vortex became downflow at the downside of USAF. As is shown in Figure 12, the turbulence intensity was low where the downflow occurred at lee-side, which means the turbulence energy may not be able to support the survival of wake vortex, leading to accretion happening. As mentioned in previous section, the formation of horseshoe vortex was dependent with adverse pressure gradient at upside of foundation. As shown in Figure 13, the evaluated range of pressure distribution is โˆ’15 m to 15 m in x direction. The t = 450 s and t = 1800 s indicate that the wave crest and trough arrived at the upside and lee-side of the foundation respectively, and the t = 350 s was neither the wave crest nor trough. The adverse gradient pressure reached the maximum value at t = 450 s corresponding to the wave crest phase. In this case, itโ€™s helpful for the wave boundary separating fully from seabed, which leads to the formation of horseshoe vortex with high turbulence intensity. Therefore, the horseshoe vortex is responsible for the local scour between neighboring anchor branches at upside of USAF. Whatโ€™s more, due to the combination of the horseshoe vortex and streamline compression, the maximum scour depth occurred at the upside of the USAF with an angle of about 45ยฐ corresponding to the wave propagating direction. This is consistent with the findings of Pang et al. [48] and Sumer et al. [1,15] in case of regular waves. At the wave trough phase (t = 1800 s), the pressure gradient became positive at upstream USAF edges, which hindered the separating of wave boundary from seabed. In the meantime, the flow reversal occurred (Figure 10) and the adverse gradient pressure appeared at downstream USAF edges, but the magnitude of adverse gradient pressure at lee-side was lower than the upstream gradient pressure under wave crest. In this way, the intensity of horseshoe vortex behind the USAF under wave trough was low, which explains the difference of scour depth at upstream and downstream, i.e., the scour asymmetry. In other words, the scour asymmetry at upside and downside of USAF was attributed to wave asymmetry for random waves, and the phenomenon became more evident for nonlinear waves [21]. Briefly speaking, the vortex system at wave crest phase was mainly related to the scour process around USAF under random waves.

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Figure 13. Pressure distribution around USAF.

4.3. Equilibrium Scour Depth

The KC number is a key parameter for horseshoe vortex emerging and evolving under waves. According to Equation (1), when pile diameter D is fixed, the KC depends on the maximum near-bed velocity Uwm and wave period T. For random waves, the Uwm can be denoted by the root-mean-square (RMS) value of near-bed velocity amplitude Uwm,rms or the significant value of near-bed velocity amplitude Uwm,s. The Uwm,rms and Uwm,s for all simulating cases of the present study are listed in Table 3 and Table 4. The T can be denoted by the mean up zero-crossing wave period Ta, peak wave period Tp, significant wave period Ts, the maximum wave period Tm, 1/10โ€ฒth highest wave period Tn = 1/10 and 1/5โ€ฒth highest wave period Tn = 1/5 for random waves, so the different combinations of Uwm and T will acquire different KC. The Table 3 and Table 4 list 12 types of KC, for example, the KCrms,s was calculated by Uwm,rms and Ts. Sumer and Fredsรธe [16] conducted a series of wave flume experiments to investigate the scour depth around monopile under random waves, and found the equilibrium scour depth predicting equation (Equation (2)) for regular waves was applicable for random waves with KCrms,p. It should be noted that the Equation (2) is only suitable for KC > 6 under regular waves or KCrms,p > 6 under random waves.

Table 3. Uwm,rms and KC for case 1~9.

Table

Table 4. Uwm,s and KC for case 1~9.

Table

Raaijmakers and Rudolph [34] proposed the equilibrium scour depth predicting model (Equation (5)) around pile under waves, which is suitable for low KC. The format of Equation (5) is similar with the formula proposed by Breusers [54], which can predict the equilibrium scour depth around pile at different scour stages. In order to verify the applicability of Raaijmakersโ€™s model for predicting the equilibrium scour depth around USAF under random waves, a validation of the equilibrium scour depth Seq between the present study and Raaijmakersโ€™s equation was conducted. The position where the scour depth Seq was evaluated is the location of the maximum scour depth, and it was depicted in Figure 14. The Figure 15 displays the comparison of Seq with different KC between the present study and Raaijmakersโ€™s model.

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Figure 14. Sketch of the position where the Seq was evaluated.

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Figure 15. Comparison of the equilibrium scour depth between the present model and the model of Raaijmakers and Rudolph [34]: (aKCrms,sKCrms,a; (bKCrms,pKCrms,m; (cKCrms,n = 1/10KCrms,n = 1/5; (dKCs,sKCs,a; (eKCs,pKCs,m; (fKCs,n = 1/10KCs,n = 1/5.

As shown in Figure 15, there is an error in predicting Seq between the present study and Raaijmakersโ€™s model, and Raaijmakersโ€™s model underestimates the results generally. Although the error exists, the varying trend of Seq with KC obtained from Raaijmakersโ€™s model is consistent with the present study basically. Whatโ€™s more, the error is minimum and the Raaijmakersโ€™s model is of relatively high accuracy for predicting scour around USAF under random waves by using KCs,p. Based on this, a further revision was made to eliminate the error as much as possible, i.e., add the deviation value โˆ†S/D in the Raaijmakersโ€™s model. The revised equilibrium scour depth predicting equation based on Raaijmakersโ€™s model can be written as

Sโ€ฒeq/D=1.95[tanh(hD)](1โˆ’exp(โˆ’0.012KCs,p))+ฮ”S/D๏ฟฝeqโ€ฒ/๏ฟฝ=1.95tanh(โ„Ž๏ฟฝ)(1โˆ’exp(โˆ’0.012๏ฟฝ๏ฟฝs,p))+โˆ†๏ฟฝ/๏ฟฝ(31)

As the Figure 16 shown, through trial-calculation, when โˆ†S/D = 0.05, the results calculated by Equation (31) show good agreement with the simulating results of the present study. The maximum error is about 18.2% and the engineering requirements have been met basically. In order to further verify the accuracy of the revised model for large KC (KCs,p > 4) under random waves, a validation between the revised model and the previous experimental results [21]. The experiment was conducted in a flume (50 m in length, 1.0 m in width and 1.3 m in height) with a slender vertical pile (D = 0.1 m) under random waves. The seabed is composed of 0.13 m deep layer of sand with d50 = 0.6 mm and the water depth is 0.5 m for all tests. The significant wave height is 0.12~0.21 m and the KCs,p is 5.52~11.38. The comparison between the predicting results by Equation (31) and the experimental results of Corvaro et al. [21] is shown in Figure 17. From Figure 17, the experimental data evenly distributes around the predicted results and the prediction accuracy is favorable when KCs,p < 8. However, the gap between the predicting results and experimental data becomes large and the Equation (31) overestimates the equilibrium scour depth to some extent when KCs,p > 8.

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Figure 16. Comparison of Seq between the simulating results and the predicting values by Equation (31).

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Figure 17. Comparison of Seq/D between the Experimental results of Corvaro et al. [21] and the predicting values by Equation (31).

In ocean environment, the waves are composed of a train of sinusoidal waves with different frequencies and amplitudes. The energy of constituent waves with very large and very small frequencies is relatively low, and the energy of waves is mainly concentrated in a certain range of moderate frequencies. Myrhaug and Rue [37] thought the 1/nโ€™th highest wave was responsible for scour and proposed the stochastic model to predict the equilibrium scour depth around pile under random waves for full range of KC. Noteworthy is that the KC was denoted by KCrms,a in the stochastic model. To verify the application of the stochastic model for predicting scour depth around USAF, a validation between the simulating results of present study and predicting results by the stochastic model with n = 2,3,5,10,20,500 was carried out respectively.

As shown in Figure 18, compared with the simulating results, the stochastic model underestimates the equilibrium scour depth around USAF generally. Although the error exists, the varying trend of Seq with KCrms,a obtained from the stochastic model is consistent with the present study basically. Whatโ€™s more, the gap between the predicting values by stochastic model and the simulating results decreases with the increase of n, but for large n, for example n = 500, the varying trend diverges between the predicting values and simulating results, meaning itโ€™s not feasible only by increasing n in stochastic model to predict the equilibrium scour depth around USAF.

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Figure 18. Comparison of Seq between the simulating results and the predicting values by Equation (8).

The Figure 19 lists the deviation value โˆ†Seq/Dโ€ฒ between the predicting values and simulating results with different KCrms,a and n. Then, fitted the relationship between the โˆ†Sโ€ฒand n under different KCrms,a, and the fitting curve can be written by Equation (32). The revised stochastic model (Equation (33)) can be acquired by adding โˆ†Seq/Dโ€ฒ to Equation (8).

ฮ”Seq/D=0.052*exp(โˆ’n/6.566)+0.068โˆ†๏ฟฝeq/๏ฟฝ=0.052*exp(โˆ’๏ฟฝ/6.566)+0.068(32)

Sโ€ฒeqยฏ/D=Sโ€ฒeq/D+0.052*exp(โˆ’n/6.566)+0.068๏ฟฝeqโ€ฒยฏ/๏ฟฝ=๏ฟฝeqโ€ฒ/๏ฟฝ+0.052*exp(โˆ’๏ฟฝ/6.566)+0.068(33)

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Figure 19. The fitting line between โˆ†Sโ€ฒand n.

The comparison between the predicting results by Equation (33) and the simulating results of present study is shown in Figure 20. According to the Figure 20, the varying trend of Seq with KCrms,a obtained from the stochastic model is consistent with the present study basically. Compared with predicting results by the stochastic model, the results calculated by Equation (33) is favorable. Moreover, comparison with simulating results indicates that the predicting results are the most favorable for n = 10, which is consistent with the findings of Myrhaug and Rue [37] for equilibrium scour depth predicting around slender pile in case of random waves.

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Figure 20. Comparison of Seq between the simulating results and the predicting values by Equation (33).

In order to further verify the accuracy of the Equation (33) for large KC (KCrms,a > 4) under random waves, a validation was conducted between the Equation (33) and the previous experimental results of Sumer and Fredsรธe [16] and Corvaro et al. [21]. The details of experiments conducted by Corvaro et al. [21] were described in above section. Sumer and Fredsรธe [16] investigated the local scour around pile under random waves. The experiments were conducted in a wave basin with a slender vertical pile (D = 0.032, 0.055 m). The seabed is composed of 0.14 m deep layer of sand with d50 = 0.2 mm and the water depth was maintained at 0.5 m. The JONSWAP wave spectrum was used and the KCrms,a was 5.29~16.95. The comparison between the predicting results by Equation (33) and the experimental results of Sumer and Fredsรธe [16] and Corvaro et al. [21] are shown in Figure 21. From Figure 21, contrary to the case of low KCrms,a (KCrms,a < 4), the error between the predicting values and experimental results increases with decreasing of n for KCrms,a > 4. Therefore, the predicting results are the most favorable for n = 2 when KCrms,a > 4.

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Figure 21. Comparison of Seq between the experimental results of Sumer and Fredsรธe [16] and Corvaro et al. [21] and the predicting values by Equation (33).

Noteworthy is that the present model was built according to prototype size, so the errors between the numerical results and experimental data of References [16,21] may be attribute to the scale effects. In laboratory experiments on scouring process, it is typically impossible to ensure a rigorous similarity of all physical parameters between the model and prototype structure, leading to the scale effects in the laboratory experiments. To avoid a cohesive behaviour, the bed material was not scaled geometrically according to model scale. As a consequence, the relatively large-scaled sediments sizes may result in the overestimation of bed load transport and underestimation of suspended load transport compared with field conditions. Whatโ€™s more, the disproportional scaled sediment presumably lead to the difference of bed roughness between the model and prototype, and thus large influences for wave boundary layer on the seabed and scour process. Besides, according to Corvaro et al. [21] and Schendel et al. [55], the pile Reynolds numbers and Froude numbers both affect the scour depth for the condition of non fully developed turbulent flow in laboratory experiments.

4.4. Parametric Study

4.4.1. Influence of Froude Number

As described above, the set of foundation leads to the adverse pressure gradient appearing at upstream, leading to the wave boundary layer separating from seabed, then horseshoe vortex formatting and the horseshoe vortex are mainly responsible for scour around foundation (see Figure 22). The Froude number Fr is the key parameter to influence the scale and intensity of horseshoe vortex. The Fr under waves can be calculated by the following formula [42]

Fr=UwgDโˆ’โˆ’โˆ’โˆš๏ฟฝr=๏ฟฝw๏ฟฝ๏ฟฝ(34)

where Uw is the mean water particle velocity during 1/4 cycle of wave oscillation, obtained from the following formula. Noteworthy is that the root-mean-square (RMS) value of near-bed velocity amplitude Uwm,rms is used for calculating Uwm.

Uw=1T/4โˆซ0T/4Uwmsin(t/T)dt=2ฯ€Uwm๏ฟฝw=1๏ฟฝ/4โˆซ0๏ฟฝ/4๏ฟฝwmsin(๏ฟฝ/๏ฟฝ)๏ฟฝ๏ฟฝ=2๏ฟฝ๏ฟฝwm(35)

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Figure 22. Sketch of flow field at upstream USAF edges.

Tavouktsoglou et al. [25] proposed the following formula between Fr and the vertical location of the stagnation y

yhโˆFer๏ฟฝโ„Žโˆ๏ฟฝr๏ฟฝ(36)

where e is constant.

The Figure 23 displays the relationship between Seq/D and Fr of the present study. In order to compare with the simulating results, the experimental data of Corvaro et al. [21] was also depicted in Figure 23. As shown in Figure 23, the equilibrium scour depth appears a logarithmic increase as Fr increases and approaches the mathematical asymptotic value, which is also consistent with the experimental results of Corvaro et al. [21]. According to Figure 24, the adverse pressure gradient pressure at upstream USAF edges increases with the increase of Fr, which is benefit for the wave boundary layer separating from seabed, resulting in the high-intensity horseshoe vortex, hence, causing intensive scour around USAF. Based on the previous study of Tavouktsoglou et al. [25] for scour around pile under currents, the high Fr leads to the stagnation point is closer to the mean sea level for shallow water, causing the stronger downflow kinetic energy. As mentioned in previous section, the energy of downflow at upstream makes up the energy of the subsequent horseshoe vortex, so the stronger downflow kinetic energy results in the more intensive horseshoe vortex. Therefore, the higher Fr leads to the more intensive horseshoe vortex by influencing the position of stagnation point y presumably. Qi and Gao [19] carried out a series of flume tests to investigate the scour around pile under regular waves, and proposed the fitting formula between Seq/D and Fr as following

lg(Seq/D)=Aexp(B/Fr)+Clg(๏ฟฝeq/๏ฟฝ)=๏ฟฝexp(๏ฟฝ/๏ฟฝr)+๏ฟฝ(37)

where AB and C are constant.

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Figure 23. The fitting curve between Seq/D and Fr.

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Figure 24. Sketch of adverse pressure gradient at upstream USAF edges.

Took the Equation (37) to fit the simulating results with A = โˆ’0.002, B = 0.686 and C = โˆ’0.808, and the results are shown in Figure 23. From Figure 23, the simulating results evenly distribute around the Equation (37) and the varying trend of Seq/D and Fr in present study is consistent with Equation (37) basically, meaning the Equation (37) is applicable to express the relationship of Seq/D with Fr around USAF under random waves.

4.4.2. Influence of Euler Number

The Euler number Eu is the influencing factor for the hydrodynamic field around foundation. The Eu under waves can be calculated by the following formula. The Eu can be represented by the Equation (38) for uniform cylinders [25]. The root-mean-square (RMS) value of near-bed velocity amplitude Um,rms is used for calculating Um.

Eu=U2mgD๏ฟฝu=๏ฟฝm2๏ฟฝ๏ฟฝ(38)

where Um is depth-averaged flow velocity.

The Figure 25 displays the relationship between Seq/D and Eu of the present study. In order to compare with the simulating results, the experimental data of Sumer and Fredsรธe [16] and Corvaro et al. [21] were also plotted in Figure 25. As shown in Figure 25, similar with the varying trend of Seq/D and Fr, the equilibrium scour depth appears a logarithmic increase as Eu increases and approaches the mathematical asymptotic value, which is also consistent with the experimental results of Sumer and Fredsรธe [16] and Corvaro et al. [21]. According to Figure 24, the adverse pressure gradient pressure at upstream USAF edges increases with the increasing of Eu, which is benefit for the wave boundary layer separating from seabed, inducing the high-intensity horseshoe vortex, hence, causing intensive scour around USAF.

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Figure 25. The fitting curve between Seq/D and Eu.

Therefore, the variation of Fr and Eu reflect the magnitude of adverse pressure gradient pressure at upstream. Given that, the Equation (37) also was used to fit the simulating results with A = 8.875, B = 0.078 and C = โˆ’9.601, and the results are shown in Figure 25. From Figure 25, the simulating results evenly distribute around the Equation (37) and the varying trend of Seq/D and Eu in present study is consistent with Equation (37) basically, meaning the Equation (37) is also applicable to express the relationship of Seq/D with Eu around USAF under random waves. Additionally, according to the above description of Fr, it can be inferred that the higher Fr and Eu both lead to the more intensive horseshoe vortex by influencing the position of stagnation point y presumably.

5. Conclusions

A series of numerical models were established to investigate the local scour around umbrella suction anchor foundation (USAF) under random waves. The numerical model was validated for hydrodynamic and morphology parameters by comparing with the experimental data of Khosronejad et al. [52], Petersen et al. [17], Sumer and Fredsรธe [16] and Schendel et al. [22]. Based on the simulating results, the scour evolution and scour mechanisms around USAF under random waves were analyzed respectively. Two revised models were proposed according to the model of Raaijmakers and Rudolph [34] and the stochastic model developed by Myrhaug and Rue [37] to predict the equilibrium scour depth around USAF under random waves. Finally, a parametric study was carried out with the present model to study the effects of the Froude number Fr and Euler number Eu to the equilibrium scour depth around USAF under random waves. The main conclusions can be described as follows.(1)

The packed sediment scour model and the RNG kโˆ’ฮต turbulence model were used to simulate the sand particles transport processes and the flow field around UASF respectively. The scour evolution obtained by the present model agrees well with the experimental results of Khosronejad et al. [52], Petersen et al. [17], Sumer and Fredsรธe [16] and Schendel et al. [22], which indicates that the present model is accurate and reasonable for depicting the scour morphology around UASF under random waves.(2)

The vortex system at wave crest phase is mainly related to the scour process around USAF under random waves. The maximum scour depth appeared at the lee-side of the USAF at the initial stage (t < 1200 s). Subsequently, when t > 2400 s, the location of the maximum scour depth shifted to the upside of the USAF at an angle of about 45ยฐ with respect to the wave propagating direction.(3)

The error is negligible and the Raaijmakersโ€™s model is of relatively high accuracy for predicting scour around USAF under random waves when KC is calculated by KCs,p. Given that, a further revision model (Equation (31)) was proposed according to Raaijmakersโ€™s model to predict the equilibrium scour depth around USAF under random waves and it shows good agreement with the simulating results of the present study when KCs,p < 8.(4)

Another further revision model (Equation (33)) was proposed according to the stochastic model established by Myrhaug and Rue [37] to predict the equilibrium scour depth around USAF under random waves, and the predicting results are the most favorable for n = 10 when KCrms,a < 4. However, contrary to the case of low KCrms,a, the predicting results are the most favorable for n = 2 when KCrms,a > 4 by the comparison with experimental results of Sumer and Fredsรธe [16] and Corvaro et al. [21].(5)

The same formula (Equation (37)) is applicable to express the relationship of Seq/D with Eu or Fr, and it can be inferred that the higher Fr and Eu both lead to the more intensive horseshoe vortex and larger Seq.

Author Contributions

Conceptualization, H.L. (Hongjun Liu); Data curation, R.H. and P.Y.; Formal analysis, X.W. and H.L. (Hao Leng); Funding acquisition, X.W.; Writingโ€”original draft, R.H. and P.Y.; Writingโ€”review & editing, X.W. and H.L. (Hao Leng); The final manuscript has been approved by all the authors. All authors have read and agreed to the published version of the manuscript.

Funding

This research was funded by the Fundamental Research Funds for the Central Universities (grant number 202061027) and the National Natural Science Foundation of China (grant number 41572247).

Institutional Review Board Statement

Not applicable.

Informed Consent Statement

Not applicable.

Data Availability Statement

The data presented in this study are available on request from the corresponding author.

Conflicts of Interest

The authors declare no conflict of interest.

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Hu, R.; Liu, H.; Leng, H.; Yu, P.; Wang, X. Scour Characteristics and Equilibrium Scour Depth Prediction around Umbrella Suction Anchor Foundation under Random Waves. J. Mar. Sci. Eng. 20219, 886. https://doi.org/10.3390/jmse9080886

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Hu R, Liu H, Leng H, Yu P, Wang X. Scour Characteristics and Equilibrium Scour Depth Prediction around Umbrella Suction Anchor Foundation under Random Waves. Journal of Marine Science and Engineering. 2021; 9(8):886. https://doi.org/10.3390/jmse9080886Chicago/Turabian Style

Hu, Ruigeng, Hongjun Liu, Hao Leng, Peng Yu, and Xiuhai Wang. 2021. “Scour Characteristics and Equilibrium Scour Depth Prediction around Umbrella Suction Anchor Foundation under Random Waves” Journal of Marine Science and Engineering 9, no. 8: 886. https://doi.org/10.3390/jmse9080886

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Influence of crest geometric on discharge coefficient efficiency of labyrinth weirs

Influence of crest geometric on discharge coefficient efficiency of labyrinth weirs

Erick Mattos-Villarroel a, Jorge Flores-Velรกzquez b, Waldo Ojeda-Bustamante c, Carlos Dรญaz-Delgado d, Humberto Salinas-Tapia dShow moreAdd to MendeleyShareCite

aMexican Institute of Water Technology, Mexico
bPostgraduate College, Hydrosciences, Carr. Mex-Tex Km 36.5, Texcoco, Mexico State, 56230, Mexico
cAgricultural Engineering Graduate Program, University of Chapingo, Mexicod
Inter-American Institute of Water Science and Technology, Mexico

https://doi.org/10.1016/j.flowmeasinst.2021.102031Get rights and content

Highlights

  • โ€ขOptimizing the geometric design of weirs can improve hydraulic performance.
  • โ€ขLabyrinth type weirs allow the discharge capacity to be increased compared to linear weirs.
  • โ€ขHydraulic heads with ratio HT/P > 0.5 generated sub-atmospheric pressures on the side walls of the weir.
  • โ€ขNumerical simulation it is a strong tool to analyze and get optimized the weir function.

Abstract

Labyrinth type weirs are structures that, due to their geometry, allow the discharge capacity to be increased compared to linear weirs. They are a favorable option for dam rehabilitation and upstream level control. There are various geometries of labyrinth type weirs such as trapezoidal, triangular or piano key as well as different types of crest profiles. Geometric changes are directly related to hydraulic efficiency. The objective of this work was to analyze the hydraulic performance of a labyrinth type weir, by simulating several geometries of the apex and of the crest using Computational Fluid Dynamics (CFD). For model validation, experimental studies reported in the literature were used. Tests were carried out with trapezoidal and circular apexes and four types of crest profiles: sharp-crest, half-round, quarter-round and Waterways Experiment Station (WES). The results revealed a determination coefficient of R2 = 0.984 between experimental and simulated data with CFD, which provides statistical agreement. Simulations showed that circular-apex weirs are more efficient than those with trapezoidal apex, because they have a higher discharge coefficient (4.7% higher). Of the four types of crest profiles analyzed, the half-round and the WES crest profiles had similar discharge coefficients and were generally greater than those of the sharp-crest and the quarter-round (5.26% y 8.5% higher) profiles. Nevertheless, to facilitate a practical construction process, it is recommended to use a half-round profile. For hydraulic heads with HT/P > 0.5 ratio, all profiles generated sub-atmospheric pressures on the side walls of the weir. However, when HT/P โ‰ˆ 0.8 ratio the half-round crest generated a higher negative pressure (โˆ’1500 Pa), while the sharp-crest profile managed to increase the pressure by 76% (โˆ’350 Pa), but with a greater area of negative pressure. On the other hand, the WES profile reduced the negative-pressure area by 50%.

Keywords

Labyrinth weir

Computational fluids dynamics (CFD)

Discharge coefficient

Apex shape

Crest profile

Figures (12)

  1. Fig. 1. Geometric parameters of a labyrinth weir
  2. Fig. 2. Crest profiles: (A) sharp-crest, (B) half-round, (C) quarter-round, (D) WES
  3. Fig. 3. Apex shapes
  4. Fig. 4. Weir and boundary conditions
  5. Fig. 5. Hydraulic head approach an asymptotic zero-grid spacing value
  6. Fig. 6. Percentage relative error of the discharge coefficient as a function of HT/P
  7. Fig. 7. Comparison of the discharge coefficients obtained numerically against theโ€ฆ
  8. Fig. 8. Pressure distribution in the downstream side walls of the labyrinth weir
  9. Fig. 9. Comparison of the discharge coefficient in trapezoidal apex labyrinth weirs
  10. Fig. 10. Comparison of the discharge coefficient in circular apex labyrinth weirs
  11. Fig. 11. Local drowning at the upstream apex
  12. Fig. 12. Ratio of the discharge coefficient of the circular apex weir with theโ€ฆ
Figure 1. Photorealistic view of an inclined axis TAST (photo A. Stergiopoulou).

CFD Simulations of Tubular Archimedean Screw Turbines Harnessing the Small Hydropotential of Greek Watercourses

Alkistis Stergiopoulou1, Vassilios Stergiopoulos2
1Institut fรผr Wasserwirtschaft, Hydrologie und Konstruktiven Wasserbau, B.O.K.U. University,
Muthgasse 18, 1190 Vienna, (actually Senior Process Engineer at the VTU Engineering in Vienna,
Zieglergasse 53/1/24, 1070 Vienna, Austria).
2 School of Pedagogical and Technological Education, Department of Civil Engineering Educators,
ASPETE Campus, Eirini Station, 15122 Amarousio, Athens, Greece.
Received 4 Jan. 2021; Received in revised form 8 Aug. 2021; Accepted 8 Aug. 2021; Available online 14 Aug. 2021

Abstract

This paper presents a short view of the first Archimedean Screw Turbines CFD modelling results, which
were carried out within the recent research entitled โ€œRebirth of Archimedes in Greece: contribution to the
study of hydraulic mechanics and hydrodynamic behavior of Archimedean cochlear waterwheels, for
recovering the hydraulic potential of Greek natural and technical watercoursesโ€. This CFD analysis, based
to the Flow-3D code, concerns typical Tubular Archimedean Screw Turbines (TASTs) and shows some
promising performances for such small hydropower systems harnessing the important unexploited
hydraulic potential of natural and technical watercourses of Greece, of the order of several TWh / year and of a total installed capacity in the range of thousands MWs.

์ด ๋…ผ๋ฌธ์€ ์ตœ์ดˆ์˜ ์•„๋ฅดํ‚ค๋ฉ”๋ฐ์Šค ๋‚˜์‚ฌ ํ„ฐ๋นˆ CFD ๋ชจ๋ธ๋ง ๊ฒฐ๊ณผ์— ๋Œ€ํ•œ ๊ฐ„๋žตํ•œ ๊ฒฌํ•ด๋ฅผ ์ œ์‹œํ•˜๋ฉฐ, ์ด๋Š” “๊ทธ๋ฆฌ์Šค์—์„œ ์•„๋ฅดํ‚ค๋ฉ”๋ฐ์Šค์˜ ๋ถ€ํ™œ: ์ˆ˜๋ฆฌ ์—ญํ•™ ๋ฐ ์•„๋ฅดํ‚ค๋ฉ”๋ฐ์Šค ๋‹ฌํŒฝ์ด๊ด€ ๋ฌผ๋ ˆ๋ฐฉ์•„์˜ ์œ ์ฒด์—ญํ•™์  ๊ฑฐ๋™ ์—ฐ๊ตฌ์— ๋Œ€ํ•œ ๊ธฐ์—ฌ”๋ผ๋Š” ์ œ๋ชฉ์˜ ์ตœ๊ทผ ์—ฐ๊ตฌ์—์„œ ์ˆ˜ํ–‰๋˜์—ˆ์Šต๋‹ˆ๋‹ค. ๊ทธ๋ฆฌ์Šค ์ž์—ฐ ๋ฐ ๊ธฐ์ˆ  ์ˆ˜๋กœ์˜ ์ˆ˜๋ ฅ ์ž ์žฌ๋ ฅโ€. Flow-3D ์ฝ”๋“œ๋ฅผ ๊ธฐ๋ฐ˜์œผ๋กœ ํ•˜๋Š” ์ด CFD ๋ถ„์„์€ ์ผ๋ฐ˜์ ์ธ TAST(Tubular Archimedean Screw Turbines)์— ๊ด€ํ•œ ๊ฒƒ์ด๋ฉฐ ๊ทธ๋ฆฌ์Šค์˜ ์ž์—ฐ ๋ฐ ๊ธฐ์ˆ  ์ˆ˜๋กœ์˜ ์ค‘์š”ํ•œ ๋ฏธ๊ฐœ๋ฐœ ์ˆ˜๋ ฅ ์ž ์žฌ๋ ฅ์„ ํ™œ์šฉํ•˜๋Š” ์ด๋Ÿฌํ•œ TWh/๋…„ ๋ฐ ์ˆ˜์ฒœ MW ๋ฒ”์œ„์˜ ์ด ์„ค์น˜ ์šฉ๋Ÿ‰์ธ ์†Œ๊ทœ๋ชจ ์ˆ˜๋ ฅ ๋ฐœ์ „ ์‹œ์Šคํ…œ์— ๋Œ€ํ•œ ๋ช‡ ๊ฐ€์ง€ ์œ ๋งํ•œ ์„ฑ๋Šฅ์„ ๋ณด์—ฌ์ค๋‹ˆ๋‹ค.
Copyright ยฉ 2021 International Energy and Environment Foundation – All rights reserved.

Keywords

CFD; Flow-3D; TAST; Small Hydro; Renewable Energy; Greek Watercourses.

Figure 1. Photorealistic view of an inclined axis TAST (photo A. Stergiopoulou).
Figure 1. Photorealistic view of an inclined axis TAST (photo A. Stergiopoulou).

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Study on Hydrodynamic Performance of Unsymmetrical Double Vertical Slotted Barriers

์นจ์ˆ˜๋œ ๊ฐ•์„ฑ ์‹์ƒ์„ ๊ฐ–๋Š” ๊ฐœ๋ฐฉ ์ˆ˜๋กœ ํ๋ฆ„์˜ ํŠน์„ฑ์— ๋Œ€ํ•œ 3์ฐจ์› ์ˆ˜์น˜ ์‹œ๋ฎฌ๋ ˆ์ด์…˜

A 3-D numerical simulation of the characteristics of open channel flows with submerged rigid vegetation

Journal of Hydrodynamicsย volumeย 33,ย pages833โ€“843 (2021)

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Abstract

์ด ๋ฐฑ์„œ๋Š” Flow-3D๋ฅผ ์ ์šฉํ•˜์—ฌ ๋‹ค์–‘ํ•œ ํ๋ฆ„ ๋ฐฐ์ถœ ๋ฐ ์‹์ƒ ์‹œ๋‚˜๋ฆฌ์˜ค๊ฐ€ ํ๋ฆ„ ์†๋„(์„ธ๋กœ, ๊ฐ€๋กœ ๋ฐ ์ˆ˜์ง ์†๋„ ํฌํ•จ)์— ๋ฏธ์น˜๋Š” ์˜ํ–ฅ์„ ์กฐ์‚ฌํ•ฉ๋‹ˆ๋‹ค.

์‹คํ—˜์  ์ธก์ •์„ ํ†ตํ•œ ๊ฒ€์ฆ ํ›„ ์‹์ƒ์ง๊ฒฝ, ์‹์ƒ๋†’์ด, ์œ ๋Ÿ‰๋ฐฉ๋ฅ˜๋Ÿ‰์— ๋Œ€ํ•œ ๋ฏผ๊ฐ๋„ ๋ถ„์„์„ ์ˆ˜ํ–‰ํ•˜์˜€๋‹ค. ์ข…๋ฐฉํ–ฅ ์†๋„์˜ ๊ฒฝ์šฐ ํ๋ฆ„ ๊ตฌ์กฐ์— ๊ฐ€์žฅ ํฐ ์˜ํ–ฅ์„ ๋ฏธ์น˜๋Š” ๊ฒƒ์€ ๋ฐฐ์ถœ๋ณด๋‹ค๋Š” ์‹์ƒ ์ง๊ฒฝ์—์„œ ๋น„๋กฏ๋ฉ๋‹ˆ๋‹ค.

๊ทธ๋Ÿฌ๋‚˜ ์‹์ƒ ๋†’์ด๋Š” ์ˆ˜์ง ๋ถ„ํฌ์˜ ๋ณ€๊ณก์ ์„ ๊ฒฐ์ •ํ•ฉ๋‹ˆ๋‹ค. ์‹์ƒ์ง€ ๋‚ด ๋‘ ์ง€์ , ์ฆ‰ ์ƒ๋ฅ˜์™€ ํ•˜๋ฅ˜์˜ ํšก์†๋„๋ฅผ ๋น„๊ตํ•˜๋ฉด ์ˆ˜์‹ฌ์— ๋”ฐ๋ฅธ ๋Œ€์นญ์ ์ธ ํŒจํ„ด์„ ํ™•์ธํ•  ์ˆ˜ ์žˆ๋‹ค. ์‹์ƒ ์ง€์—ญ์˜ ๊ฐ€๋กœ ๋ฐ ์„ธ๋กœ ์œ ์ฒด ์ˆœํ™˜ ํŒจํ„ด์„ ํฌํ•จํ•˜์—ฌ ํ๋ฆ„ ๋˜๋Š” ์‹์ƒ ์‹œ๋‚˜๋ฆฌ์˜ค์™€ ๊ด€๊ณ„์—†์ด ์ˆ˜์ง ์†๋„์— ๋Œ€ํ•ด์„œ๋„ ๋™์ผํ•œ ํŒจํ„ด์ด ๊ด€์ฐฐ๋ฉ๋‹ˆ๋‹ค.

๋˜ํ•œ ์‹์ƒ์˜ ์ง๊ฒฝ์ด ํด์ˆ˜๋ก ์ด๋Ÿฌํ•œ ํŒจํ„ด์ด ๋” ๋ถ„๋ช…ํ•ด์ง‘๋‹ˆ๋‹ค. ์ƒ๋ถ€ ์ˆœํ™˜์€ ์ดˆ๋ชฉ ์บ๋…ธํ”ผ ๊ทผ์ฒ˜์—์„œ ๋ฐœ์ƒํ•ฉ๋‹ˆ๋‹ค. ์‹์ƒ์ง€์—ญ์˜ ๊ฐ€๋กœ๋ฐฉํ–ฅ๊ณผ ์„ธ๋กœ๋ฐฉํ–ฅ์˜ ์ˆœํ™˜์— ๊ด€ํ•œ ์ด๋Ÿฌํ•œ ๋ฐœ๊ฒฌ์€ ์นจ์ˆ˜์‹์ƒ์„ ํ†ตํ•œ 3์ฐจ์› ์œ ๋™๊ตฌ์กฐ๋ฅผ ๋ฐํ˜€์ค€๋‹ค.

This paper applies the Flow-3D to investigate the impacts of different flow discharge and vegetation scenarios on the flow velocity (including the longitudinal, transverse and vertical velocities). After the verification by using experimental measurements, a sensitivity analysis is conducted for the vegetation diameter, the vegetation height and the flow discharge. For the longitudinal velocity, the greatest impact on the flow structure originates from the vegetation diameter, rather than the discharge. The vegetation height, however, determines the inflection point of the vertical distribution. Comparing the transverse velocities at two positions in the vegetated area, i.e., the upstream and the downstream, a symmetric pattern is identified along the water depth. The same pattern is also observed for the vertical velocity regardless of the flow or vegetation scenario, including both transverse and vertical fluid circulation patterns in the vegetated area. Moreover, the larger the vegetation diameter is, the more evident these patterns become. The upper circulation occurs near the vegetation canopy. These findings regarding the circulations along the transverse and vertical directions in the vegetated region shed light on the 3-D flow structure through the submerged vegetation.

Key words

  • Submerged rigid vegetation
  • longitudinal velocity
  • transverse velocity
  • vertical velocity
  • open channel

References

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Figure 2 Modeling the plant with cylindrical tubes at the bottom of the canal.

Optimized Vegetation Density to Dissipate Energy of Flood Flow in Open Canals

์—ด๋ฆฐ ์šดํ•˜์—์„œ ํ™์ˆ˜ ํ๋ฆ„์˜ ์—๋„ˆ์ง€๋ฅผ ๋ถ„์‚ฐ์‹œํ‚ค๊ธฐ ์œ„ํ•ด ์ตœ์ ํ™”๋œ ์‹์ƒ ๋ฐ€๋„

Mahdi Feizbahr,1Navid Tonekaboni,2Guang-Jun Jiang,3,4andย Hong-Xia Chen3,4
Academic Editor:ย Mohammad Yazdi

Abstract

๊ฐ•์„ ๋”ฐ๋ผ ์‹์ƒ์€ ์กฐ๋„๋ฅผ ์ฆ๊ฐ€์‹œํ‚ค๊ณ  ํ‰๊ท  ์œ ์†์„ ๊ฐ์†Œ์‹œํ‚ค๋ฉฐ, ์œ ๋™ ์—๋„ˆ์ง€๋ฅผ ๊ฐ์†Œ์‹œํ‚ค๊ณ  ๊ฐ• ํšก๋‹จ๋ฉด์˜ ์œ ์† ํ”„๋กœํŒŒ์ผ์„ ๋ณ€๊ฒฝํ•ฉ๋‹ˆ๋‹ค.ย ์ž์—ฐ์˜ ๋งŽ์€ ์šดํ•˜์™€ ๊ฐ•์€ ํ™์ˆ˜ ๋™์•ˆ ์ดˆ๋ชฉ์œผ๋กœ ๋ฎ์—ฌ ์žˆ์Šต๋‹ˆ๋‹ค.ย ์šดํ•˜์˜ ์กฐ๋„๋Š” ์‹๋ฌผ์˜ ์˜ํ–ฅ์„ ๋งŽ์ด ๋ฐ›๊ธฐ ๋•Œ๋ฌธ์— ํ™์ˆ˜์‹œ ์œ ๋™์ €ํ•ญ์— ํฐ ์˜ํ–ฅ์„ ๋ฏธ์นœ๋‹ค.ย ์‹๋ฌผ๋กœ ์ธํ•œ ํ๋ฆ„์— ๋Œ€ํ•œ ๊ฑฐ์น ๊ธฐ ์ €ํ•ญ์€ ํ๋ฆ„ ์กฐ๊ฑด๊ณผ ์‹๋ฌผ์— ๋”ฐ๋ผ ๋‹ฌ๋ผ์ง€๋ฏ€๋กœ ๋ชจ๋ธ์€ ์œ ์†, ์œ ์† ๊นŠ์ด ๋ฐ ์ˆ˜๋กœ๋ฅผ ๋”ฐ๋ผ ์‹์ƒ ์œ ํ˜•์˜ ์˜ํ–ฅ์„ ๊ณ ๋ คํ•˜์—ฌ ์œ ์†์„ ์‹œ๋ฎฌ๋ ˆ์ด์…˜ํ•ด์•ผ ํ•ฉ๋‹ˆ๋‹ค.ย ์ด 48๊ฐœ์˜ ๋ชจ๋ธ์„ ์‹œ๋ฎฌ๋ ˆ์ด์…˜ํ•˜์—ฌ ๊ทผ๊ด€์˜ ๊ฑฐ์น ๊ธฐ ํšจ๊ณผ๋ฅผ ์กฐ์‚ฌํ–ˆ์Šต๋‹ˆ๋‹ค.ย ๊ฒฐ๊ณผ๋Š” ์†๋„๋ฅผ ๋†’์ž„์œผ๋กœ์จ ๋ฒ ๋“œ ์†๋„๋ฅผ ๊ฐ์†Œ์‹œํ‚ค๋Š” ์‹์ƒ์˜ ์˜ํ–ฅ์ด ๋ฌด์‹œํ• ๋งŒํ•˜๋‹ค๋Š” ๊ฒƒ์„ ๋‚˜ํƒ€๋ƒ…๋‹ˆ๋‹ค.

Abstract

Vegetation along the river increases the roughness and reduces the average flow velocity, reduces flow energy, and changes the flow velocity profile in the cross section of the river. Many canals and rivers in nature are covered with vegetation during the floods. Canalโ€™s roughness is strongly affected by plants and therefore it has a great effect on flow resistance during flood. Roughness resistance against the flow due to the plants depends on the flow conditions and plant, so the model should simulate the current velocity by considering the effects of velocity, depth of flow, and type of vegetation along the canal. Total of 48 models have been simulated to investigate the effect of roughness in the canal. The results indicated that, by enhancing the velocity, the effect of vegetation in decreasing the bed velocity is negligible, while when the current has lower speed, the effect of vegetation on decreasing the bed velocity is obviously considerable.

1. Introduction

Considering the impact of each variable is a very popular field within the analytical and statistical methods and intelligent systems [1โ€“14]. This can help research for better modeling considering the relation of variables or interaction of them toward reaching a better condition for the objective function in control and engineering [15โ€“27]. Consequently, it is necessary to study the effects of the passive factors on the active domain [28โ€“36]. Because of the effect of vegetation on reducing the discharge capacity of rivers [37], pruning plants was necessary to improve the condition of rivers. One of the important effects of vegetation in river protection is the action of roots, which cause soil consolidation and soil structure improvement and, by enhancing the shear strength of soil, increase the resistance of canal walls against the erosive force of water. The outer limbs of the plant increase the roughness of the canal walls and reduce the flow velocity and deplete the flow energy in vicinity of the walls. Vegetation by reducing the shear stress of the canal bed reduces flood discharge and sedimentation in the intervals between vegetation and increases the stability of the walls [38โ€“41].

One of the main factors influencing the speed, depth, and extent of flood in this method is Manningโ€™s roughness coefficient. On the other hand, soil cover [42], especially vegetation, is one of the most determining factors in Manningโ€™s roughness coefficient. Therefore, it is expected that those seasonal changes in the vegetation of the region will play an important role in the calculated value of Manningโ€™s roughness coefficient and ultimately in predicting the flood wave behavior [43โ€“45]. The roughness caused by plantsโ€™ resistance to flood current depends on the flow and plant conditions. Flow conditions include depth and velocity of the plant, and plant conditions include plant type, hardness or flexibility, dimensions, density, and shape of the plant [46]. In general, the issue discussed in this research is the optimization of flood-induced flow in canals by considering the effect of vegetation-induced roughness. Therefore, the effect of plants on the roughness coefficient and canal transmission coefficient and in consequence the flow depth should be evaluated [4748].

Current resistance is generally known by its roughness coefficient. The equation that is mainly used in this field is Manning equation. The ratio of shear velocity to average current velocity  is another form of current resistance. The reason for using the  ratio is that it is dimensionless and has a strong theoretical basis. The reason for using Manning roughness coefficient is its pervasiveness. According to Freeman et al. [49], the Manning roughness coefficient for plants was calculated according to the Kouwen and Unny [50] method for incremental resistance. This method involves increasing the roughness for various surface and plant irregularities. Manningโ€™s roughness coefficient has all the factors affecting the resistance of the canal. Therefore, the appropriate way to more accurately estimate this coefficient is to know the factors affecting this coefficient [51].

To calculate the flow rate, velocity, and depth of flow in canals as well as flood and sediment estimation, it is important to evaluate the flow resistance. To determine the flow resistance in open ducts, Manning, Chรฉzy, and Darcyโ€“Weisbach relations are used [52]. In these relations, there are parameters such as Manningโ€™s roughness coefficient (n), Chรฉzy roughness coefficient (C), and Darcyโ€“Weisbach coefficient (f). All three of these coefficients are a kind of flow resistance coefficient that is widely used in the equations governing flow in rivers [53].

The three relations that express the relationship between the average flow velocity (V) and the resistance and geometric and hydraulic coefficients of the canal are as follows:where nf, and c are Manning, Darcyโ€“Weisbach, and Chรฉzy coefficients, respectively. Vโ€‰=โ€‰average flow velocity, Rโ€‰=โ€‰hydraulic radius, Sfโ€‰=โ€‰slope of energy line, which in uniform flow is equal to the slope of the canal bed, โ€‰=โ€‰gravitational acceleration, and Kn is a coefficient whose value is equal to 1 in the SI system and 1.486 in the English system. The coefficients of resistance in equations (1) to (3) are related as follows:

Based on the boundary layer theory, the flow resistance for rough substrates is determined from the following general relation:where fโ€‰=โ€‰Darcyโ€“Weisbach coefficient of friction, yโ€‰=โ€‰flow depth, Ksโ€‰=โ€‰bed roughness size, and Aโ€‰=โ€‰constant coefficient.

On the other hand, the relationship between the Darcyโ€“Weisbach coefficient of friction and the shear velocity of the flow is as follows:

By using equation (6), equation (5) is converted as follows:

Investigation on the effect of vegetation arrangement on shear velocity of flow in laboratory conditions showed that, with increasing the shear Reynolds number (), the numerical value of the  ratio also increases; in other words the amount of roughness coefficient increases with a slight difference in the cases without vegetation, checkered arrangement, and cross arrangement, respectively [54].

Roughness in river vegetation is simulated in mathematical models with a variable floor slope flume by different densities and discharges. The vegetation considered submerged in the bed of the flume. Results showed that, with increasing vegetation density, canal roughness and flow shear speed increase and with increasing flow rate and depth, Manningโ€™s roughness coefficient decreases. Factors affecting the roughness caused by vegetation include the effect of plant density and arrangement on flow resistance, the effect of flow velocity on flow resistance, and the effect of depth [4555].

One of the works that has been done on the effect of vegetation on the roughness coefficient is Darby [56] study, which investigates a flood wave model that considers all the effects of vegetation on the roughness coefficient. There are currently two methods for estimating vegetation roughness. One method is to add the thrust force effect to Manningโ€™s equation [475758] and the other method is to increase the canal bed roughness (Manning-Strickler coefficient) [4559โ€“61]. These two methods provide acceptable results in models designed to simulate floodplain flow. Wang et al. [62] simulate the floodplain with submerged vegetation using these two methods and to increase the accuracy of the results, they suggested using the effective height of the plant under running water instead of using the actual height of the plant. Freeman et al. [49] provided equations for determining the coefficient of vegetation roughness under different conditions. Lee et al. [63] proposed a method for calculating the Manning coefficient using the flow velocity ratio at different depths. Much research has been done on the Manning roughness coefficient in rivers, and researchers [4963โ€“66] sought to obtain a specific number for n to use in river engineering. However, since the depth and geometric conditions of rivers are completely variable in different places, the values of Manning roughness coefficient have changed subsequently, and it has not been possible to choose a fixed number. In river engineering software, the Manning roughness coefficient is determined only for specific and constant conditions or normal flow. Lee et al. [63] stated that seasonal conditions, density, and type of vegetation should also be considered. Hydraulic roughness and Manning roughness coefficient n of the plant were obtained by estimating the total Manning roughness coefficient from the matching of the measured water surface curve and water surface height. The following equation is used for the flow surface curve:where  is the depth of water change, S0 is the slope of the canal floor, Sf is the slope of the energy line, and Fr is the Froude number which is obtained from the following equation:where D is the characteristic length of the canal. Flood flow velocity is one of the important parameters of flood waves, which is very important in calculating the water level profile and energy consumption. In the cases where there are many limitations for researchers due to the wide range of experimental dimensions and the variety of design parameters, the use of numerical methods that are able to estimate the rest of the unknown results with acceptable accuracy is economically justified.

FLOW-3D software uses Finite Difference Method (FDM) for numerical solution of two-dimensional and three-dimensional flow. This software is dedicated to computational fluid dynamics (CFD) and is provided by Flow Science [67]. The flow is divided into networks with tubular cells. For each cell there are values of dependent variables and all variables are calculated in the center of the cell, except for the velocity, which is calculated at the center of the cell. In this software, two numerical techniques have been used for geometric simulation, FAVORโ„ข (Fractional-Area-Volume-Obstacle-Representation) and the VOF (Volume-of-Fluid) method. The equations used at this model for this research include the principle of mass survival and the magnitude of motion as follows. The fluid motion equations in three dimensions, including the Navierโ€“Stokes equations with some additional terms, are as follows:where  are mass accelerations in the directions xyz and  are viscosity accelerations in the directions xyz and are obtained from the following equations:

Shear stresses  in equation (11) are obtained from the following equations:

The standard model is used for high Reynolds currents, but in this model, RNG theory allows the analytical differential formula to be used for the effective viscosity that occurs at low Reynolds numbers. Therefore, the RNG model can be used for low and high Reynolds currents.

Weather changes are high and this affects many factors continuously. The presence of vegetation in any area reduces the velocity of surface flows and prevents soil erosion, so vegetation will have a significant impact on reducing destructive floods. One of the methods of erosion protection in floodplain watersheds is the use of biological methods. The presence of vegetation in watersheds reduces the flow rate during floods and prevents soil erosion. The external organs of plants increase the roughness and decrease the velocity of water flow and thus reduce its shear stress energy. One of the important factors with which the hydraulic resistance of plants is expressed is the roughness coefficient. Measuring the roughness coefficient of plants and investigating their effect on reducing velocity and shear stress of flow is of special importance.

Roughness coefficients in canals are affected by two main factors, namely, flow conditions and vegetation characteristics [68]. So far, much research has been done on the effect of the roughness factor created by vegetation, but the issue of plant density has received less attention. For this purpose, this study was conducted to investigate the effect of vegetation density on flow velocity changes.

In a study conducted using a software model on three density modes in the submerged state effect on flow velocity changes in 48 different modes was investigated (Table 1).

Table 1 

The studied models.

The number of cells used in this simulation is equal to 1955888โ€‰cells. The boundary conditions were introduced to the model as a constant speed and depth (Figure 1). At the output boundary, due to the presence of supercritical current, no parameter for the current is considered. Absolute roughness for floors and walls was introduced to the model (Figure 1). In this case, the flow was assumed to be nonviscous and air entry into the flow was not considered. After  seconds, this model reached a convergence accuracy of .

Figure 1 

The simulated model and its boundary conditions.

Due to the fact that it is not possible to model the vegetation in FLOW-3D software, in this research, the vegetation of small soft plants was studied so that Manningโ€™s coefficients can be entered into the canal bed in the form of roughness coefficients obtained from the studies of Chow [69] in similar conditions. In practice, in such modeling, the effect of plant height is eliminated due to the small height of herbaceous plants, and modeling can provide relatively acceptable results in these conditions.

48 models with input velocities proportional to the height of the regular semihexagonal canal were considered to create supercritical conditions. Manning coefficients were applied based on Chow [69] studies in order to control the canal bed. Speed profiles were drawn and discussed.

Any control and simulation system has some inputs that we should determine to test any technology [70โ€“77]. Determination and true implementation of such parameters is one of the key steps of any simulation [2378โ€“81] and computing procedure [82โ€“86]. The input current is created by applying the flow rate through the VFR (Volume Flow Rate) option and the output flow is considered Output and for other borders the Symmetry option is considered.

Simulation of the models and checking their action and responses and observing how a process behaves is one of the accepted methods in engineering and science [8788]. For verification of FLOW-3D software, the results of computer simulations are compared with laboratory measurements and according to the values of computational error, convergence error, and the time required for convergence, the most appropriate option for real-time simulation is selected (Figures 2 and 3 ).

Figure 2 

Modeling the plant with cylindrical tubes at the bottom of the canal.

Figure 3 

Velocity profiles in positions 2 and 5.

The canal is 7 meters long, 0.5 meters wide, and 0.8 meters deep. This test was used to validate the application of the software to predict the flow rate parameters. In this experiment, instead of using the plant, cylindrical pipes were used in the bottom of the canal.

The conditions of this modeling are similar to the laboratory conditions and the boundary conditions used in the laboratory were used for numerical modeling. The critical flow enters the simulation model from the upstream boundary, so in the upstream boundary conditions, critical velocity and depth are considered. The flow at the downstream boundary is supercritical, so no parameters are applied to the downstream boundary.

The software well predicts the process of changing the speed profile in the open canal along with the considered obstacles. The error in the calculated speed values can be due to the complexity of the flow and the interaction of the turbulence caused by the roughness of the floor with the turbulence caused by the three-dimensional cycles in the hydraulic jump. As a result, the software is able to predict the speed distribution in open canals.

2. Modeling Results

After analyzing the models, the results were shown in graphs (Figures 4โ€“14 ). The total number of experiments in this study was 48 due to the limitations of modeling.


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Figure 4 

Flow velocity profiles for canals with a depth of 1โ€‰m and flow velocities of 3โ€“3.3โ€‰m/s. Canal with a depth of 1 meter and a flow velocity of (a) 3 meters per second, (b) 3.1 meters per second, (c) 3.2 meters per second, and (d) 3.3 meters per second.

Figure 5 

Canal diagram with a depth of 1 meter and a flow rate of 3 meters per second.

Figure 6 

Canal diagram with a depth of 1 meter and a flow rate of 3.1 meters per second.

Figure 7 

Canal diagram with a depth of 1 meter and a flow rate of 3.2 meters per second.

Figure 8 

Canal diagram with a depth of 1 meter and a flow rate of 3.3 meters per second.


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Figure 9 

Flow velocity profiles for canals with a depth of 2โ€‰m and flow velocities of 4โ€“4.3โ€‰m/s. Canal with a depth of 2 meters and a flow rate of (a) 4 meters per second, (b) 4.1 meters per second, (c) 4.2 meters per second, and (d) 4.3 meters per second.

Figure 10 

Canal diagram with a depth of 2 meters and a flow rate of 4 meters per second.

Figure 11 

Canal diagram with a depth of 2 meters and a flow rate of 4.1 meters per second.

Figure 12 

Canal diagram with a depth of 2 meters and a flow rate of 4.2 meters per second.

Figure 13 

Canal diagram with a depth of 2 meters and a flow rate of 4.3 meters per second.


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Figure 14 

Flow velocity profiles for canals with a depth of 3โ€‰m and flow velocities of 5โ€“5.3โ€‰m/s. Canal with a depth of 2 meters and a flow rate of (a) 4 meters per second, (b) 4.1 meters per second, (c) 4.2 meters per second, and (d) 4.3 meters per second.

To investigate the effects of roughness with flow velocity, the trend of flow velocity changes at different depths and with supercritical flow to a Froude number proportional to the depth of the section has been obtained.

According to the velocity profiles of Figure 5, it can be seen that, with the increasing of Manningโ€™s coefficient, the canal bed speed decreases.

According to Figures 5 to 8, it can be found that, with increasing the Manningโ€™s coefficient, the canal bed speed decreases. But this deceleration is more noticeable than the deceleration of the models 1 to 12, which can be justified by increasing the speed and of course increasing the Froude number.

According to Figure 10, we see that, with increasing Manningโ€™s coefficient, the canal bed speed decreases.

According to Figure 11, we see that, with increasing Manningโ€™s coefficient, the canal bed speed decreases. But this deceleration is more noticeable than the deceleration of Figures 5โ€“10, which can be justified by increasing the speed and, of course, increasing the Froude number.

With increasing Manningโ€™s coefficient, the canal bed speed decreases (Figure 12). But this deceleration is more noticeable than the deceleration of the higher models (Figures 5โ€“8 and 1011), which can be justified by increasing the speed and, of course, increasing the Froude number.

According to Figure 13, with increasing Manningโ€™s coefficient, the canal bed speed decreases. But this deceleration is more noticeable than the deceleration of Figures 5 to 12, which can be justified by increasing the speed and, of course, increasing the Froude number.

According to Figure 15, with increasing Manningโ€™s coefficient, the canal bed speed decreases.

Figure 15 

Canal diagram with a depth of 3 meters and a flow rate of 5 meters per second.

According to Figure 16, with increasing Manningโ€™s coefficient, the canal bed speed decreases. But this deceleration is more noticeable than the deceleration of the higher model, which can be justified by increasing the speed and, of course, increasing the Froude number.

Figure 16 

Canal diagram with a depth of 3 meters and a flow rate of 5.1 meters per second.

According to Figure 17, it is clear that, with increasing Manningโ€™s coefficient, the canal bed speed decreases. But this deceleration is more noticeable than the deceleration of the higher models, which can be justified by increasing the speed and, of course, increasing the Froude number.

Figure 17 

Canal diagram with a depth of 3 meters and a flow rate of 5.2 meters per second.

According to Figure 18, with increasing Manningโ€™s coefficient, the canal bed speed decreases. But this deceleration is more noticeable than the deceleration of the higher models, which can be justified by increasing the speed and, of course, increasing the Froude number.

Figure 18 

Canal diagram with a depth of 3 meters and a flow rate of 5.3 meters per second.

According to Figure 19, it can be seen that the vegetation placed in front of the flow input velocity has negligible effect on the reduction of velocity, which of course can be justified due to the flexibility of the vegetation. The only unusual thing is the unexpected decrease in floor speed of 3โ€‰m/s compared to higher speeds.


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Figure 19 

Comparison of velocity profiles with the same plant densities (depth 1โ€‰m). Comparison of velocity profiles with (a) plant densities of 25%, depth 1โ€‰m; (b) plant densities of 50%, depth 1โ€‰m; and (c) plant densities of 75%, depth 1โ€‰m.

According to Figure 20, by increasing the speed of vegetation, the effect of vegetation on reducing the flow rate becomes more noticeable. And the role of input current does not have much effect in reducing speed.


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Figure 20 

Comparison of velocity profiles with the same plant densities (depth 2โ€‰m). Comparison of velocity profiles with (a) plant densities of 25%, depth 2โ€‰m; (b) plant densities of 50%, depth 2โ€‰m; and (c) plant densities of 75%, depth 2โ€‰m.

According to Figure 21, it can be seen that, with increasing speed, the effect of vegetation on reducing the bed flow rate becomes more noticeable and the role of the input current does not have much effect. In general, it can be seen that, by increasing the speed of the input current, the slope of the profiles increases from the bed to the water surface and due to the fact that, in software, the roughness coefficient applies to the channel floor only in the boundary conditions, this can be perfectly justified. Of course, it can be noted that, due to the flexible conditions of the vegetation of the bed, this modeling can show acceptable results for such grasses in the canal floor. In the next directions, we may try application of swarm-based optimization methods for modeling and finding the most effective factors in this research [278151889โ€“94]. In future, we can also apply the simulation logic and software of this research for other domains such as power engineering [95โ€“99].


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Figure 21 

Comparison of velocity profiles with the same plant densities (depth 3โ€‰m). Comparison of velocity profiles with (a) plant densities of 25%, depth 3โ€‰m; (b) plant densities of 50%, depth 3โ€‰m; and (c) plant densities of 75%, depth 3โ€‰m.

3. Conclusion

The effects of vegetation on the flood canal were investigated by numerical modeling with FLOW-3D software. After analyzing the results, the following conclusions were reached:(i)Increasing the density of vegetation reduces the velocity of the canal floor but has no effect on the velocity of the canal surface.(ii)Increasing the Froude number is directly related to increasing the speed of the canal floor.(iii)In the canal with a depth of one meter, a sudden increase in speed can be observed from the lowest speed and higher speed, which is justified by the sudden increase in Froude number.(iv)As the inlet flow rate increases, the slope of the profiles from the bed to the water surface increases.(v)By reducing the Froude number, the effect of vegetation on reducing the flow bed rate becomes more noticeable. And the input velocity in reducing the velocity of the canal floor does not have much effect.(vi)At a flow rate between 3 and 3.3โ€‰meters per second due to the shallow depth of the canal and the higher landing number a more critical area is observed in which the flow bed velocity in this area is between 2.86 and 3.1โ€‰m/s.(vii)Due to the critical flow velocity and the slight effect of the roughness of the horseshoe vortex floor, it is not visible and is only partially observed in models 1-2-3 and 21.(viii)As the flow rate increases, the effect of vegetation on the rate of bed reduction decreases.(ix)In conditions where less current intensity is passing, vegetation has a greater effect on reducing current intensity and energy consumption increases.(x)In the case of using the flow rate of 0.8 cubic meters per second, the velocity distribution and flow regime show about 20% more energy consumption than in the case of using the flow rate of 1.3 cubic meters per second.

Nomenclature

n:Manningโ€™s roughness coefficient
C:Chรฉzy roughness coefficient
f:Darcyโ€“Weisbach coefficient
V:Flow velocity
R:Hydraulic radius
g:Gravitational acceleration
y:Flow depth
Ks:Bed roughness
A:Constant coefficient
:Reynolds number
โˆ‚y/โˆ‚x:Depth of water change
S0:Slope of the canal floor
Sf:Slope of energy line
Fr:Froude number
D:Characteristic length of the canal
G:Mass acceleration
:Shear stresses.

Data Availability

All data are included within the paper.

Conflicts of Interest

The authors declare that they have no conflicts of interest.

Acknowledgments

This work was partially supported by the National Natural Science Foundation of China under Contract no. 71761030 and Natural Science Foundation of Inner Mongolia under Contract no. 2019LH07003.

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Strain rate magnitude at the free surface, illustrating Kelvin-Helmoltz (KH) shear instabilities.

On the reef scale hydrodynamics at Sodwana Bay, South Africa

Environmental Fluid Mechanics (2022)Cite this article

Abstract

The hydrodynamics of coral reefs strongly influences their biological functioning, impacting processes such as nutrient availability and uptake, recruitment success and bleaching. For example, coral reefs located in oligotrophic regions depend on upwelling for nutrient supply. Coral reefs at Sodwana Bay, located on the east coast of South Africa, are an example of high latitude marginal reefs. These reefs are subjected to complex hydrodynamic forcings due to the interaction between the strong Agulhas current and the highly variable topography of the region. In this study, we explore the reef scale hydrodynamics resulting from the bathymetry for two steady current scenarios at Two-Mile Reef (TMR) using a combination of field data and numerical simulations. The influence of tides or waves was not considered for this study as well as reef-scale roughness. Tilt current meters with onboard temperature sensors were deployed at selected locations within TMR. We used field observations to identify the dominant flow conditions on the reef for numerical simulations that focused on the hydrodynamics driven by mean currents. During the field campaign, southerly currents were the predominant flow feature with occasional flow reversals to the north. Northerly currents were associated with greater variability towards the southern end of TMR. Numerical simulations showed that Jesser Point was central to the development of flow features for both the northerly and southerly current scenarios. High current variability in the south of TMR during reverse currents is related to the formation of Kelvin-Helmholtz type shear instabilities along the outer edge of an eddy formed north of Jesser Point. Furthermore, downward vertical velocities were computed along the offshore shelf at TMR during southerly currents. Current reversals caused a change in vertical velocities to an upward direction due to the orientation of the bathymetry relative to flow directions.

Highlights

  • A predominant southerly current was measured at Two-Mile Reef with occasional reversals towards the north.
  • Field observations indicated that northerly currents are spatially varied along Two-Mile Reef.
  • Simulation of reverse currents show the formation of a separated flow due to interaction with Jesser Point with Kelvinโ€“Helmholtz type shear instabilities along the seaward edge.

์ง€๊ธˆ๊นŒ์ง€ Sodwana Bay์—์„œ ์ž์„ธํ•œ ์•”์ดˆ ๊ทœ๋ชจ ์œ ์ฒด ์—ญํ•™์„ ๋ชจ๋ธ๋งํ•˜๋ ค๋Š” ์‹œ๋„๋Š” ์—†์—ˆ์Šต๋‹ˆ๋‹ค.ย ์ด๋Ÿฌํ•œ ๋ชจ๋ธ์˜ ๊ฒฐ๊ณผ๋Š” ๊ทœ๋ชจ๊ฐ€ ์žˆ๋Š” ์‚ฐํ˜ธ์ดˆ ์‚ฌ์ด์˜ ํ๋ฆ„์ด ์‚ฐํ˜ธ์ดˆ ๊ฑด๊ฐ•์— ์–ด๋–ค ์˜ํ–ฅ์„ ๋ฏธ์น˜๋Š”์ง€ ํƒ์ƒ‰ํ•˜๋Š” ๋ฐ ์‚ฌ์šฉํ•  ์ˆ˜ ์žˆ์Šต๋‹ˆ๋‹ค.ย ์ด ์—ฐ๊ตฌ์—์„œ๋Š” Sodwana Bay์˜ ์œ ์ฒด์—ญํ•™์„ ํƒ์ƒ‰ํ•˜๋Š” ๋ฐ ์‚ฌ์šฉํ•  ์ˆ˜ ์žˆ๋Š” LES ๋ชจ๋ธ์„ ๊ฐœ๋ฐœํ•˜๊ธฐ ์œ„ํ•œ ๋‹จ๊ณ„๋ณ„ ์ ‘๊ทผ ๋ฐฉ์‹์„ ๊ตฌํ˜„ํ•ฉ๋‹ˆ๋‹ค.ย ์—ฌ๊ธฐ์„œ ์šฐ๋ฆฌ๋Š” ์ด ์ดˆ๊ธฐ ๋‹จ๊ณ„์—์„œ ํŒŒ๋„์™€ ์กฐ์ˆ˜์˜ ์˜ํ–ฅ์„ ๋ฐฐ์ œํ•˜๋ฉด์„œ Agulhas ํ•ด๋ฅ˜์˜ ์œ ์ฒด์—ญํ•™์— ์ดˆ์ ์„ ๋งž์ถฅ๋‹ˆ๋‹ค.ย ์ด ์ ‘๊ทผ๋ฒ•์€ ํ๋ฆ„์˜ ์ฒซ ๋ฒˆ์งธ LES๋ฅผ ์ œ์‹œํ•˜๊ณ  Sodwana Bay์˜ ์‚ฐํ˜ธ์ดˆ์—์„œ ํ˜ผํ•ฉํ•จ์œผ๋กœ์จ ํ–ฅํ›„ ์—ฐ๊ตฌ์˜ ๊ธฐ์ดˆ๋ฅผ ์ œ๊ณตํ•ฉ๋‹ˆ๋‹ค.

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Text and image taken from Deoraj, et al. (2022), On the reef scale hydrodynamics at Sodwana Bay, South Africa. Preprint courtesy the authors.

Fig. 2. Design of the grate inlet types studied: (a) R1, (b) R2, (c) R3, (d) R4, (e) R5, (f) R6, (g) R7 (source: based on geometries of Chaparro Andrade and Abaunza Tabares, 2021)

Three-dimensional Numerical Evaluation of Hydraulic Efficiency and Discharge Coefficient in Grate Inlets

์‡ ์ฐฝ์‚ด ๊ฒฉ์ž ์œ ์ž…๊ตฌ์˜ ์ˆ˜๋ฆฌํšจ์œจ ๋ฐ ๋ฐฐ์ถœ๊ณ„์ˆ˜์— ๋Œ€ํ•œ 3์ฐจ์› ์ˆ˜์น˜์  ํ‰๊ฐ€

Melquisedec Cortรฉs Zambrano*, Helmer Edgardo Monroy Gonzรกlez,
Wilson Enrique Amaya Tequia
Faculty of Civil Engineering, Santo Tomas Tunja University. Address Av. Universitaria No. 45-202.
Tunja โ€“ Boyacรก – Colombia

Abstract

ํ™์ˆ˜๋Š” ์ง€๋ฐ˜์ด๋™ ๋ฐ ์ด๋™์˜ ์›์ธ ์ค‘ ํ•˜๋‚˜์ด๋ฉฐ, ๊ธ‰์†ํ•œ ๋„์‹œํ™” ๋ฐ ๋„์‹œํ™”๋กœ ์ธํ•ด ์ด์ „๋ณด๋‹ค ๋นˆ๋ฒˆํ•˜๊ฒŒ ๋ฐœ์ƒํ•  ์ˆ˜ ์žˆ๋‹ค. ๋„์‹œ ๋ฐฐ์ˆ˜ ์‹œ์Šคํ…œ์˜ ํŠน์„ฑ์€ ์ง‘์ˆ˜ ์š”์†Œ๊ฐ€ ๊ฒฐ์ •์ ์ธ ์—ญํ• ์„ ํ•˜๋Š” ๋ฒ”๋žŒ์˜ ๋ฐœ์ƒ ๋ฐ ๋ฒ”์œ„๋ฅผ ์ •์˜ํ•  ์ˆ˜ ์žˆ์Šต๋‹ˆ๋‹ค. ์ด ๋ฌธ์„œ๋Š” 7๊ฐ€์ง€ ์œ ํ˜•์˜ ํ™”๊ฒฉ์ž ์œ ์ž…๊ตฌ์˜ ์ˆ˜๋ ฅ ์œ ์ž… ํšจ์œจ ๋ฐ ๋ฐฐ์ถœ ๊ณ„์ˆ˜์— ๋Œ€ํ•œ ์ˆ˜์น˜ ์กฐ์‚ฌ๋ฅผ ์ œ์‹œํ•ฉ๋‹ˆ๋‹ค. FLOW-3Dยฎ ์‹œ๋ฎฌ๋ ˆ์ดํ„ฐ๋Š” Q = 24, 34.1, 44, 100, 200 ๋ฐ 300 L/s์˜ ์œ ์†์—์„œ ํ’€ ์Šค์ผ€์ผ๋กœ ๊ฒฉ์ž๋ฅผ ํ…Œ์ŠคํŠธํ•˜๋Š” ๋ฐ ์‚ฌ์šฉ๋˜๋ฉฐ ์ข…๋ฐฉํ–ฅ ๊ธฐ์šธ๊ธฐ๊ฐ€ 1.0์ธ ์‹คํ—˜ ํ”„๋กœํ† ํƒ€์ž…์˜ ๊ตฌ์„ฑ์„ ์œ ์ง€ํ•ฉ๋‹ˆ๋‹ค. %, 1.5% ๋ฐ 2.0% ๋ฐ ๊ณ ์ • ํšก๋‹จ ๊ฒฝ์‚ฌ, ์ด 126๊ฐœ ๋ชจ๋ธ. ๊ทธ ๊ฒฐ๊ณผ๋ฅผ ๋ฐ”ํƒ•์œผ๋กœ ์ข…๋ฅ˜๋ณ„ ๋ฐ ์ข…๋‹จ๊ฒฝ์‚ฌ ์กฐ๊ฑด์— ๋”ฐ๋ฅธ ์ˆ˜๋ ฅ์œ ์ž…๊ตฌ ํšจ์œจ๊ณก์„ ๊ณผ ํ† ์ถœ๊ณ„์ˆ˜๋ฅผ ๊ตฌ์„ฑํ•˜์˜€๋‹ค. ๊ฒฐ๊ณผ๋Š” ๋‹ค๋ฅธ ์กฐ์‚ฌ์—์„œ ์ œ์•ˆ๋œ ๊ฒฝํ—˜์  ๊ณต์‹์œผ๋กœ ์กฐ์ •๋˜์–ด ํ”„๋กœํ† ํƒ€์ž…์˜ ๋ฌผ๋ฆฌ์  ํ…Œ์ŠคํŠธ ๊ฒฐ๊ณผ๋ฅผ ๊ฒ€์ฆํ•˜๋Š” ์—ญํ• ์„ ํ•ฉ๋‹ˆ๋‹ค.

Floods are one of the causes of ground movement and displacement, and due to rapid urbanization and urban growth may occur more frequently than before. The characteristics of an urban drainage system can define the occurrence and extent of flooding, where catchment elements have a determining role. This document presents the numerical investigation of the hydraulic inlet efficiency and the discharge coefficient of seven types of grate inlets. The FLOW-3Dยฎ simulator is used to test the gratings at a full scale, under flow rates of Q = 24, 34.1, 44, 100, 200 and 300 L/s, preserving the configuration of the experimental prototype with longitudinal slopes of 1.0%, 1.5% and 2.0% and a fixed cross slope, for a total of 126 models. Based on the results, hydraulic inlet efficiency curves and discharge coefficients are constructed for each type and a longitudinal slope condition. The results are adjusted with empirical formulations proposed in other investigations, serving to verify the results of physical testing of prototypes.

Keywords

grate inlet, inlet efficiency, discharge coefficient, computational fluid dynamic, 3D modelling.

Fig. 1. Physical model of the experimental campaign (source: Chaparro Andrade and Abaunza Tabares, 2021)
Fig. 1. Physical model of the experimental campaign (source: Chaparro Andrade and Abaunza Tabares, 2021)
Fig. 2. Design of the grate inlet types studied: (a) R1, (b) R2, (c) R3, (d) R4, (e) R5, (f) R6, (g) R7 (source: based on geometries of Chaparro Andrade
and Abaunza Tabares, 2021)
Fig. 2. Design of the grate inlet types studied: (a) R1, (b) R2, (c) R3, (d) R4, (e) R5, (f) R6, (g) R7 (source: based on geometries of Chaparro Andrade and Abaunza Tabares, 2021)
Fig. 4. Comparison between the results obtained during physical experimentation in prototype 7 and simulation results with FLOW-3Dยฎ (source:
made with FlowSightยฎ and photographic record by Chaparro Andrade and Abaunza Tabares, 2021)
Fig. 4. Comparison between the results obtained during physical experimentation in prototype 7 and simulation results with FLOW-3Dยฎ (source: made with FlowSightยฎ and photographic record by Chaparro Andrade and Abaunza Tabares, 2021)
Fig. 6. Example of the results of flow depth and velocity vectors in the xy plane, for a stable flow condition in a grate inlet type and free surface
configuration and flow regime, of some grating types (source: produced with FlowSightยฎ)
Fig. 6. Example of the results of flow depth and velocity vectors in the xy plane, for a stable flow condition in a grate inlet type and free surface configuration and flow regime, of some grating types (source: produced with FlowSightยฎ)

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Numerical Modeling of Self-Aeration in High-Speed Flows over Smooth Chute Spillways

Smooth Chute ์—ฌ์ˆ˜๋กœ ์œ„์˜ ๊ณ ์† ํ๋ฆ„์—์„œ ์ž์ฒด ํญ๊ธฐ์˜ ์ˆ˜์น˜ ๋ชจ๋ธ๋ง

Numerical Modeling of Self-Aeration in High-Speed Flows over Smooth Chute Spillways

Authors:

Mohmmadreza Jalili Ghazizadeh

Associate Professor, Faculty of Civil, Water and Environmental Engineering, Shahid Beheshti Univ., Tehran 177651719, Iran (corresponding author). ORCID: https://orcid.org/0000-0002-8242-7619. Email: m_jalili@sbu.ac.ir

Amir R. Zarrati

Professor, Dept. of Civil and Environmental Engineering, Amirkabir Univ. of Technology (Tehran Polytechnic), Tehran 1591634311, Iran. ORCID: https://orcid.org/0000-0002-8483-3186. Email: zarrati@aut.ac.ir

Mohammad J. Ostad Mirza Tehrani

Assistant Professor, Faculty of Civil Engineering, K. N. Toosi Univ. of Technology, Tehran 1996715433, Iran; formerly, Postdoctoral Research Fellow, Dept. of Civil and Environmental Engineering, Amirkabir Univ. of Technology (Tehran Polytechnic), Tehran 1591634311, Iran. ORCID: https://orcid.org/0000-0002-5162-6332. Email: mohammad.tehrani@kntu.ac.ir

https://doi.org/10.1061/JHEND8.HYENG-12914

Received: May 15, 2021

Accepted: September 30, 2022

Published online: December 21, 2022Journal of Hydraulic Engineering

Vol. 149, Issue 3 (March 2023)

ยฉ 2022 American Society of Civil Engineers

Abstract

chute ์—ฌ์ˆ˜๋กœ์—์„œ๋Š” ๋‚œ๋ฅ˜ ๊ฒฝ๊ณ„์ธต ๊ฐ€์žฅ์ž๋ฆฌ๊ฐ€ ์ถฉ๋ถ„ํžˆ ๊ธธ๋ฉด ์ž์œ  ํ‘œ๋ฉด์— ์ ‘๊ทผํ•˜๋Š” ์‹œ์ž‘์ ์˜ ํ•˜๋ฅ˜์—์„œ ์ž์ฒด ํ†ต๊ธฐ๊ฐ€ ๋ฐœ์ƒํ•ฉ๋‹ˆ๋‹ค. ์‹œ์ž‘ ์ง€์ ์˜ ํ•˜๋ฅ˜์—์„œ ๊ณต๊ธฐ-๋ฌผ ํ˜ผํ•ฉ๋ฌผ์„ ํฌํ•จํ•˜๋Š” ์ธต์ด ํŒฝ์ฐฝ ํšจ๊ณผ์™€ ํ•จ๊ป˜ ํ๋ฆ„์„ ํ†ตํ•ด ์ ์ง„์ ์œผ๋กœ ํ™•์žฅ๋ฉ๋‹ˆ๋‹ค.

์œ ๋™ ๋ฒŒํ‚น์€ ์ธก๋ฒฝ ๊ฑดํ˜„ ์„ค๊ณ„ ์ธก๋ฉด์—์„œ ํ•„์ˆ˜์ ์ž…๋‹ˆ๋‹ค. ๋˜ํ•œ ๊ณ ์ฒด ๊ฒฝ๊ณ„ ๊ทผ์ฒ˜์— ์ถฉ๋ถ„ํ•œ ์–‘์˜ ๊ณต๊ธฐ๋ฅผ ๋„์ž…ํ•˜๋ฉด ์บ๋น„ํ…Œ์ด์…˜ ์†์ƒ์„ ๋ฐฉ์ง€ํ•  ์ˆ˜ ์žˆ์Šต๋‹ˆ๋‹ค. ํ˜„์žฌ ์—ฐ๊ตฌ์—์„œ, ๋งค๋„๋Ÿฌ์šด chute ์„ ๋”ฐ๋ผ ์œ ๋™ ๋ฒŒํ‚น๊ณผ ํ•จ๊ป˜ ๊นŠ์ด์™€ ์ž์œ  ํ‘œ๋ฉด ์œ„์น˜์— ๊ฑธ์ณ ์ž์ฒด ํญ๊ธฐ ๋ฐ ๊ณต๊ธฐ ๋†๋„ ํ”„๋กœํŒŒ์ผ์„ ์˜ˆ์ธกํ•˜๊ธฐ ์œ„ํ•ด 2D ์ˆ˜์น˜ ๋ชจ๋ธ์ด ๊ฐœ๋ฐœ๋˜์—ˆ์Šต๋‹ˆ๋‹ค.

๊ฐœ๋ฐœ๋œ ๋ชจ๋ธ์€ ํ˜ผํ•ฉ๋ฌผ ์—ฐ์†์„ฑ, ๊ธฐ๋‹จ ๋ฐ ๊ณต๊ธฐ-๋ฌผ ํ˜ผํ•ฉ๋ฌผ ์šด๋™๋Ÿ‰ ๋ณด์กด์˜ ์ผ๋ฐฉํ–ฅ ํฌ๋ฌผ์„  ๋ฐฉ์ •์‹์˜ ํ•ด๋ฅผ ๋‹ค๋ฃน๋‹ˆ๋‹ค. ์ด๋Ÿฌํ•œ ๋ฐฉ์ •์‹์€ ํ–‰์ง„ ๊ธฐ๋ฒ•๊ณผ Prandtl์˜ ํ˜ผํ•ฉ ๊ธธ์ด ๋‚œ๋ฅ˜ ๋ชจ๋ธ์„ ํ™œ์šฉํ•˜์—ฌ ์ž์œ  ํ‘œ๋ฉด์— ๋Œ€ํ•œ ๋™์  ๋ฐฉ์ •์‹๊ณผ ํ•จ๊ป˜ ํ•ด๊ฒฐ๋ฉ๋‹ˆ๋‹ค.

ํ”„๋กœํ† ํƒ€์ž… ์ธก์ • ๋ฐ ์‹คํ—˜์‹ค ํ…Œ์ŠคํŠธ๋ฅผ ํ†ตํ•ด ์–ป์€ ์‹คํ—˜ ๋ฐ์ดํ„ฐ๋ฅผ ์‚ฌ์šฉํ•˜์—ฌ ์ˆ˜์น˜ ๋ชจ๋ธ์˜ ์ •ํ™•๋„๋ฅผ ํ‰๊ฐ€ํ–ˆ์Šต๋‹ˆ๋‹ค. ๊ด€๋ จ ๊ฒฐ๊ณผ๋Š” ๊ฒฝ๊ณ„์ธต ๋ฐœ๋‹ฌ์˜ ์œ ๋„๋œ ์‹œ์ž‘์ , ์ž์ฒด ์œ ์ž… ํ๋ฆ„ ๋‚ด์˜ ๊ณต๊ธฐ ๋†๋„ ํ”„๋กœํŒŒ์ผ ๋ฐ ๊ทธ์— ๋”ฐ๋ฅธ ํ๋ฆ„์˜ ๋ฒŒํ‚น ์ธก๋ฉด์—์„œ ๋น„๊ต๋˜์—ˆ์Šต๋‹ˆ๋‹ค.

์‹ค์šฉ์ ์ธ ๋ชฉ์ ์„ ์œ„ํ•œ ์ˆ˜์น˜ ๋ชจ๋ธ์˜ ๊ธฐ๋Šฅ์€ ์ƒ๋‹นํžˆ ์ •ํ™•ํ•œ ๊ฒฐ๊ณผ์— ๋”ฐ๋ผ ์˜๋ฏธ๊ฐ€ ์žˆ์œผ๋ฉฐ ์ถ”๊ฐ€ ์—ฐ๊ตฌ๋ฅผ ์œ„ํ•œ ์ƒˆ๋กœ์šด ์ง€ํ‰์„ ๋ฐํž™๋‹ˆ๋‹ค.

In chute spillways, self-aeration occurs downstream of the inception point, where the turbulent boundary layer edge approaches the free surface, if they are long enough. Downstream of the inception point, a layer containing an airโ€“water mixture extends gradually through the flow with the bulking effect. Flow bulking is essential in terms of sidewall freeboard design. In addition, the introduction of enough air quantity near the solid boundaries prevents cavitation damage. In the present work, a 2D numerical model was developed for the prediction of self-aeration and air concentration profiles across the depth and the free-surface location, together with flow bulking along the smooth chutes. The developed model deals with the solution of the one-way direction parabolic equations of mixture continuity, air mass, and airโ€“water mixture momentum conservation. These equations are solved accompanied by the dynamic equation for the free surface, utilizing the marching technique and Prandtlโ€™s mixing length turbulent model. The experimental data obtained by prototype measurements and laboratory tests were used to assess the accuracy of the numerical model. The relevant results were compared in terms of the induced inception point of the boundary layer development, air concentration profiles within self-entrained flows, and the consequent bulking of the flow. The capability of the numerical model for practical purposes is signified in accordance with the fairly accurate obtained results, shedding light on new horizons for further research.

Figure 3. Different parts of a Searaser; 1) Buoy 2) Chamber 3) Valves 4) Generator 5) Anchor system

๋ฐ์ดํ„ฐ ๊ธฐ๋ฐ˜ ๋ฐฉ๋ฒ•์„ ํ™œ์šฉํ•œ ์žฌ์ƒ ๊ฐ€๋Šฅ ์—๋„ˆ์ง€ ๋ณ€ํ™˜๊ธฐ์˜ ์ „๋ ฅ ๋ฐ ์ˆ˜์†Œ ์ƒ์„ฑ ์˜ˆ์ธก ์ง€์† ๊ฐ€๋Šฅํ•œ ์Šค๋งˆํŠธ ๊ทธ๋ฆฌ๋“œ ์‚ฌ๋ก€ ์—ฐ๊ตฌ

Fatemehsadat Mirshafiee1, Emad Shahbazi 2, Mohadeseh Safi 3, Rituraj Rituraj 4,*
1Department of Electrical and Computer Engineering, K.N. Toosi University of Technology, Tehran 1999143344 , Iran
2Department of Mechatronic, Amirkabir University of Technology, Tehran 158754413, Iran
3Department of Mechatronic, Electrical and Computer Engineering, University of Tehran, Tehran 1416634793, Iran
4 Faculty of Informatics, Obuda University, 1023, Budapest, Hungary

  • Correspondence: rituraj88@stud.uni-obuda.hu

ABSTRACT

๋ณธ ์—ฐ๊ตฌ๋Š” ์ง€์†๊ฐ€๋Šฅํ•œ ์—๋„ˆ์ง€ ๋ณ€ํ™˜๊ธฐ์˜ ์ „๋ ฅ ๋ฐ ์ˆ˜์†Œ ๋ฐœ์ƒ ๋ชจ๋ธ๋ง์„ ์œ„ํ•œ ๋ฐ์ดํ„ฐ ๊ธฐ๋ฐ˜ ๋ฐฉ๋ฒ•๋ก ์„ ์ œ์•ˆํ•ฉ๋‹ˆ๋‹ค. ํŒŒ๊ณ ์™€ ํ’์†์„ ๋‹ฌ๋ฆฌํ•˜์—ฌ ํŒŒ๊ณ ์™€ ์ˆ˜์†Œ์ƒ์‚ฐ์„ ์˜ˆ์ธกํ•ฉ๋‹ˆ๋‹ค.

๋˜ํ•œ ์ด ์—ฐ๊ตฌ๋Š” ํŒŒ๋„์—์„œ ์ˆ˜์†Œ๋ฅผ ์ถ”์ถœํ•  ์ˆ˜ ์žˆ๋Š” ๊ฐ€๋Šฅ์„ฑ์„ ๊ฐ•์กฐํ•˜๊ณ  ์žฅ๋ คํ•ฉ๋‹ˆ๋‹ค. FLOW-3D ์†Œํ”„ํŠธ์›จ์–ด ์‹œ๋ฎฌ๋ ˆ์ด์…˜์—์„œ ์ถ”์ถœํ•œ ๋ฐ์ดํ„ฐ์™€ ํ•ด์–‘ ํŠน์ˆ˜ ํ…Œ์ŠคํŠธ์˜ ์‹คํ—˜ ๋ฐ์ดํ„ฐ๋ฅผ ์‚ฌ์šฉํ•˜์—ฌ ๋‘ ๊ฐ€์ง€ ๋ฐ์ดํ„ฐ ๊ธฐ๋ฐ˜ ํ•™์Šต ๋ฐฉ๋ฒ•์˜ ๋น„๊ต ๋ถ„์„์„ ์ˆ˜ํ–‰ํ•ฉ๋‹ˆ๋‹ค.

๊ฒฐ๊ณผ๋Š” ์ˆ˜์†Œ ์ƒ์‚ฐ์˜ ์–‘์€ ์ƒ์„ฑ๋œ ์ „๋ ฅ์˜ ์–‘์— ๋น„๋ก€ํ•œ๋‹ค๋Š” ๊ฒƒ์„ ๋ณด์—ฌ์ค๋‹ˆ๋‹ค. ์ œ์•ˆ๋œ ์žฌ์ƒ ์—๋„ˆ์ง€ ๋ณ€ํ™˜๊ธฐ์˜ ์‹ ๋ขฐ์„ฑ์€ ์ง€์† ๊ฐ€๋Šฅํ•œ ์Šค๋งˆํŠธ ๊ทธ๋ฆฌ๋“œ ์• ํ”Œ๋ฆฌ์ผ€์ด์…˜์œผ๋กœ ์ถ”๊ฐ€๋กœ ๋…ผ์˜๋ฉ๋‹ˆ๋‹ค.

This study proposes a data-driven methodology for modeling power and hydrogen generation of a sustainable energy converter. The wave and hydrogen production at different wave heights and wind speeds are predicted. Furthermore, this research emphasizes and encourages the possibility of extracting hydrogen from ocean waves. By using the extracted data from FLOW-3D software simulation and the experimental data from the special test in the ocean, the comparison analysis of two data-driven learning methods is conducted. The results show that the amount of hydrogen production is proportional to the amount of generated electrical power. The reliability of the proposed renewable energy converter is further discussed as a sustainable smart grid application.

Key words

Cavity, Combustion efficiency, hydrogen fuel, Computational Fluent and Gambit.

Figure 1. The process of power and hydrogen production with Searaser.
Figure 1. The process of power and hydrogen production with Searaser.
Figure 2. The cross-section A-A of the two essential parts of a Searaser
Figure 2. The cross-section A-A of the two essential parts of a Searaser
Figure 3. Different parts of a Searaser; 1) Buoy 2) Chamber 3) Valves 4) Generator 5) Anchor system
Figure 3. Different parts of a Searaser; 1) Buoy 2) Chamber 3) Valves 4) Generator 5) Anchor system
Figure 4. The boundary conditions of the control volume
Figure 4. The boundary conditions of the control volume
Figure 5. The wind velocity during the period of the experimental test
Figure 5. The wind velocity during the period of the experimental test

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Figure 1 | Laboratory channel dimensions.

๊ฐ•ํ™”๋œ ์กฐ๋„ ๊ณ„์ˆ˜ ๋ฐ ์ธ๋ฒ„ํŠธ ๋ ˆ๋ฒจ ๋ณ€ํ™”๊ฐ€ ์žˆ๋Š” 90๋„ ์ธก๋ฉด ํ„ด์•„์›ƒ์—์„œ์˜ ์œ ๋™์— ๋Œ€ํ•œ ์‹คํ—˜์  ๋ฐ ์ˆ˜์น˜์  ์—ฐ๊ตฌ

Experimental and numerical study of flow at a 90 degree lateral turnout with enhanced roughness coefficient and invert level changes

Maryam Bagheria, Seyed M. Ali Zomorodianb, Masih Zolghadrc, H. Md. Azamathulla d,*
and C. Venkata Siva Rama Prasade
a Hydraulic Structures, Department of Water Engineering, Shiraz University, Shiraz, Iran
b Department of Water Engineering, College of Agriculture, Shiraz University, Shiraz, Iran
c Department of Water Sciences Engineering, College of Agriculture, Jahrom University, Jahrom, Iran
d Civil & Environmental Engineering, The University of the West Indies, St. Augustine Campus, Port of Spain, Trinidad
e Department of Civil Engineering, St. Peters Engineering College, Hyderabad, India
*Corresponding author. E-mail: azmatheditor@gmail.com

ABSTRACT

์ธก๋ฉด ๋ถ„๊ธฐ๊ธฐ(ํก์ž…๊ตฌ)์˜ ์ƒ๋ฅ˜์ธก์—์„œ ์œ ๋™ ๋ถ„๋ฆฌ๋Š” ๋ถ„๊ธฐ๊ธฐ ์ž…๊ตฌ์—์„œ ๋งด๋Œ์ด ์ „๋ฅ˜๋ฅผ ์ผ์œผํ‚ค๋Š” ์ค‘์š”ํ•œ ๋ฌธ์ œ์ž…๋‹ˆ๋‹ค. ์ด๋Š” ํ๋ฆ„์˜ ์œ ํšจ ํญ, ๋ถ„๊ธฐ ์šฉ๋Ÿ‰ ๋ฐ ํšจ์œจ์„ฑ์„ ๊ฐ์†Œ์‹œํ‚ต๋‹ˆ๋‹ค. ๋”ฐ๋ผ์„œ ๋ถ„๋ฆฌ๊ตฌ์—ญ์˜ ํฌ๊ธฐ๋ฅผ ํŒŒ์•…ํ•˜๊ณ  ๊ทธ ํฌ๊ธฐ๋ฅผ ์ค„์ด๊ธฐ ์œ„ํ•œ ๋ฐฉ์•ˆ์„ ์ œ์‹œํ•˜๋Š” ๊ฒƒ์ด ํ•„์ˆ˜์ ์ด๋‹ค.

๋ณธ ์—ฐ๊ตฌ์—์„œ๋Š” ๋ถ„๋ฆฌ ๊ตฌ์—ญ์˜ ํฌ๊ธฐ๋ฅผ ์ค„์ด๊ธฐ ์œ„ํ•œ ๋ฐฉ๋ฒ•์œผ๋กœ ๋ถ„์ถœ๊ตฌ ์ž…๊ตฌ์— 7๊ฐ€์ง€ ์œ ํ˜•์˜ ์กฐ๋ฉดํ™” ์š”์†Œ์™€ 4๊ฐ€์ง€ ๋‹ค๋ฅธ ๋ฐฉ๋ฅ˜๊ฐ€ ์žˆ๋Š” 3๊ฐ€์ง€ ๋‹ค๋ฅธ ๋ฒ ๋“œ ์ธ๋ฒ„ํŠธ ๋ ˆ๋ฒจ์˜ ์„ค์น˜(์ด 84ํšŒ ์‹คํ—˜)๋ฅผ ์กฐ์‚ฌํ–ˆ์Šต๋‹ˆ๋‹ค. ๋˜ํ•œ 3D ์ „์‚ฐ ์œ ์ฒด ์—ญํ•™(CFD) ๋ชจ๋ธ์„ ์‚ฌ์šฉํ•˜์—ฌ ๋ถ„๋ฆฌ ๊ตฌ์—ญ์˜ ํ๋ฆ„ ํŒจํ„ด๊ณผ ์น˜์ˆ˜๋ฅผ ํ‰๊ฐ€ํ–ˆ์Šต๋‹ˆ๋‹ค.

๊ฒฐ๊ณผ๋Š” ์กฐ๋„ ๊ณ„์ˆ˜๋ฅผ ํ–ฅ์ƒ์‹œํ‚ค๋ฉด ๋ถ„๋ฆฌ ์˜์—ญ ์น˜์ˆ˜๋ฅผ ์ตœ๋Œ€ 38%๊นŒ์ง€ ์ค„์ผ ์ˆ˜ ์žˆ๋Š” ๋ฐ˜๋ฉด ๋“œ๋กญ ๊ตฌํ˜„ ํšจ๊ณผ๋Š” ์‚ฌ์šฉ๋œ ์กฐ๋„ ๊ณ„์ˆ˜์— ๋”ฐ๋ผ ์ด ์˜์—ญ์„ ๋‹ค๋ฅด๊ฒŒ ์ถ•์†Œํ•  ์ˆ˜ ์žˆ์Œ์„ ๋ณด์—ฌ์ฃผ์—ˆ์Šต๋‹ˆ๋‹ค. ๋‘ ๋ฐฉ๋ฒ•์„ ๊ฒฐํ•ฉํ•˜๋ฉด ๋ถ„๋ฆฌ ๊ตฌ์—ญ ์น˜์ˆ˜๋ฅผ ์ตœ๋Œ€ 63%๊นŒ์ง€ ์ค„์ผ ์ˆ˜ ์žˆ์Šต๋‹ˆ๋‹ค.

Flow separation at the upstream side of lateral turnouts (intakes) is a critical issue causing eddy currents at the turnout entrance. It reduces the effective width of flow, turnout capacity and efficiency. Therefore, it is essential to identify the dimensions of the separation zone and propose remedies to reduce its dimensions.

Installation of 7 types of roughening elements at the turnout entrance and 3 different bed invert levels, with 4 different discharges (making a total of 84 experiments) were examined in this study as a method to reduce the dimensions of the separation zone. Additionally, a 3-D Computational Fluid Dynamic (CFD) model was utilized to evaluate the flow pattern and dimensions of the separation zone.

Results showed that enhancing the roughness coefficient can reduce the separation zone dimensions up to 38% while the drop implementation effect can scale down this area differently based on the roughness coefficient used. Combining both methods can reduce the separation zone dimensions up to 63%.

Key words

discharge ratio, flow separation zone, intake, three dimensional simulation

Experimental and numerical study of flow at a 90 degree lateral turnout with enhanced
roughness coefficient and invert level changes
Experimental and numerical study of flow at a 90 degree lateral turnout with enhanced roughness coefficient and invert level changes
Figure 1 | Laboratory channel dimensions.
Figure 1 | Laboratory channel dimensions.
Figure 2 | Roughness plates.
Figure 2 | Roughness plates.
Figure 4 | Effect of roughness on separation zone dimensions.
Figure 4 | Effect of roughness on separation zone dimensions.
Figure 10 | Comparision of the vortex area (software output) for three roughnesses (0.009, 0.023 and 0.032).
Figure 10 | Comparision of the vortex area (software output) for three roughnesses (0.009, 0.023 and 0.032).
Figure 11 | Comparison of vortex area in 3D mode (tecplot output) with two roughnesses (a) 0.009 and (b) 0.032.
Figure 11 | Comparison of vortex area in 3D mode (tecplot output) with two roughnesses (a) 0.009 and (b) 0.032.
Figure 12 | Velocity vector for flow condition Qยผ22 l/s, near surface.
Figure 12 | Velocity vector for flow condition Qยผ22 l/s, near surface.

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Figure 7. Comparison of Archimedean screw power performances P(W) for Q = 0.15 m3 /s and 0.30m3 /s and angles of orientation 22ฮฟ & 32ฮฟ .

CFD Simulations of Tubular Archimedean Screw Turbines Harnessing the Small Hydropotential of Greek Watercourses

Alkistis Stergiopoulou 1, Vassilios Stergiopoulos 2
1 Institut fรผr Wasserwirtschaft, Hydrologie und Konstruktiven Wasserbau, B.O.K.U. University, Muthgasse 18, 1190 Vienna, (actually Senior Process Engineer at the VTU Engineering in Vienna, Zieglergasse 53/1/24, 1070 Vienna, Austria).2 School of Pedagogical and Technological Education, Department of Civil Engineering Educators, ASPETE Campus, Eirini Station, 15122 Amarousio, Athens, Greece.

Abstract

์ด ๋…ผ๋ฌธ์€ ์ตœ์ดˆ์˜ ์•„๋ฅดํ‚ค๋ฉ”๋ฐ์Šค ๋‚˜์‚ฌ ํ„ฐ๋นˆ CFD ๋ชจ๋ธ๋ง ๊ฒฐ๊ณผ์— ๋Œ€ํ•œ ๊ฐ„๋žตํ•œ ๊ฒฌํ•ด๋ฅผ ์ œ์‹œํ•˜๋ฉฐ, ์ด๋Š” “๊ทธ๋ฆฌ์Šค์—์„œ ์•„๋ฅดํ‚ค๋ฉ”๋ฐ์Šค์˜ ๋ถ€ํ™œ: ์ˆ˜๋ฆฌ ์—ญํ•™ ๋ฐ ์•„๋ฅดํ‚ค๋ฉ”๋ฐ์Šค ๋‹ฌํŒฝ์ด๊ด€ ๋ฌผ๋ ˆ๋ฐฉ์•„์˜ ์œ ์ฒด์—ญํ•™์  ๊ฑฐ๋™ ์—ฐ๊ตฌ์— ๋Œ€ํ•œ ๊ธฐ์—ฌ”๋ผ๋Š” ์ œ๋ชฉ์˜ ์ตœ๊ทผ ์—ฐ๊ตฌ์—์„œ ์ˆ˜ํ–‰๋˜์—ˆ์Šต๋‹ˆ๋‹ค.
๊ทธ๋ฆฌ์Šค ์ž์—ฐ ๋ฐ ๊ธฐ์ˆ  ์ˆ˜๋กœ์˜ ์ˆ˜๋ ฅ ์ž ์žฌ๋ ฅโ€. Flow-3D ์ฝ”๋“œ๋ฅผ ๊ธฐ๋ฐ˜์œผ๋กœ ํ•˜๋Š” ์ด CFD ๋ถ„์„์€ ์ผ๋ฐ˜์ ์ธ TAST(Tubular Archimedean Screw Turbines)์™€ ๊ด€๋ จ์ด ์žˆ์œผ๋ฉฐ ๋ช‡ TWh ์ •๋„์˜ ๊ทธ๋ฆฌ์Šค ์ž์—ฐ ๋ฐ ๊ธฐ์ˆ  ์ˆ˜๋กœ์˜ ์ค‘์š”ํ•œ ๋ฏธ๊ฐœ๋ฐœ ์ˆ˜๋ ฅ ์ž ์žฌ๋ ฅ์„ ํ™œ์šฉํ•˜๋Š” ์—ฐ๊ฐ„ ๋ฐ ์ˆ˜์ฒœ MW ๋ฒ”์œ„์˜ ์ด ์„ค์น˜ ์šฉ๋Ÿ‰์ธ ์†Œ๊ทœ๋ชจ ์ˆ˜๋ ฅ ๋ฐœ์ „ ์‹œ์Šคํ…œ์— ๋Œ€ํ•œ ๋ช‡ ๊ฐ€์ง€ ์œ ๋งํ•œ ์„ฑ๋Šฅ์„ ๋ณด์—ฌ์ค๋‹ˆ๋‹ค.

This paper presents a short view of the first Archimedean Screw Turbines CFD modelling results, which were carried out within the recent research entitled โ€œRebirth of Archimedes in Greece: contribution to the study of hydraulic mechanics and hydrodynamic behavior of Archimedean cochlear waterwheels, for recovering the hydraulic potential of Greek natural and technical watercoursesโ€. This CFD analysis, based to the Flow-3D code, concerns typical Tubular Archimedean Screw Turbines (TASTs) and shows some promising performances for such small hydropower systems harnessing the important unexploited hydraulic potential of natural and technical watercourses of Greece, of the order of several TWh / year and of a total installed capacity in the range of thousands MWs.

Keywords

CFD; Flow-3D; TAST; Small Hydro; Renewable Energy; Greek Watercourses.

Figure 1. Photorealistic view of an inclined axis TAST (photo A. Stergiopoulou).
Figure 1. Photorealistic view of an inclined axis TAST (photo A. Stergiopoulou).
Figure 3. The spectrum of all the screw axis orientation cases.
Figure 3. The spectrum of all the screw axis orientation cases.
Figure 4. Creation of the 3bladed Archimedean Screw with Solidworks
Figure 4. Creation of the 3bladed Archimedean Screw with Solidworks
Figure 6. โ€œMeshing & Geometryโ€ tab Operations (Flow 3-D).
Figure 6. โ€œMeshing & Geometryโ€ tab Operations (Flow 3-D).
Figure 7. Comparison of Archimedean screw power performances P(W) for Q = 0.15 m3
/s and 0.30m3
/s
and angles of orientation 22ฮฟ & 32ฮฟ
.
Figure 7. Comparison of Archimedean screw power performances P(W) for Q = 0.15 m3 /s and 0.30m3 /s and angles of orientation 22ฮฟ & 32ฮฟ .
Figure 12. Various performances of the Archimedean Screw (MKE/Mean Kinetic Energy, Torque,
Turbulent Kinetic Energy, Turbulent Dissipation) for flow discharge Q = 0.45 m3
/s and an angle of
orientation ฮธ = 32ฮฟ
Figure 12. Various performances of the Archimedean Screw (MKE/Mean Kinetic Energy, Torque, Turbulent Kinetic Energy, Turbulent Dissipation) for flow discharge Q = 0.45 m3 /s and an angle of orientation ฮธ = 32ฮฟ

References

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Figure 5. Schematic view of flap and support structure [32]

Design Optimization of Ocean Renewable Energy Converter Using a Combined Bi-level Metaheuristic Approach

๊ฒฐํ•ฉ๋œ Bi-level ๋ฉ”ํƒ€ํœด๋ฆฌ์Šคํ‹ฑ ์ ‘๊ทผ๋ฒ•์„ ์‚ฌ์šฉํ•œ ํ•ด์–‘ ์žฌ์ƒ ์—๋„ˆ์ง€ ๋ณ€ํ™˜๊ธฐ์˜ ์„ค๊ณ„ ์ตœ์ ํ™”

Erfan Amini a1, Mahdieh Nasiri b1, Navid Salami Pargoo a, Zahra Mozhgani c, Danial Golbaz d, Mehrdad Baniesmaeil e, Meysam Majidi Nezhad f, Mehdi Neshat gj, Davide Astiaso Garcia h, Georgios Sylaios i

Abstract

In recent years, there has been an increasing interest in renewable energies in view of the fact that fossil fuels are the leading cause of catastrophic environmental consequences. Ocean wave energy is a renewable energy source that is particularly prevalent in coastal areas. Since many countries have tremendous potential to extract this type of energy, a number of researchers have sought to determine certain effective factors on wave convertersโ€™ performance, with a primary emphasis on ambient factors. In this study, we used metaheuristic optimization methods to investigate the effects of geometric factors on the performance of an Oscillating Surge Wave Energy Converter (OSWEC), in addition to the effects of hydrodynamic parameters. To do so, we used CATIA software to model different geometries which were then inserted into a numerical model developed in Flow3D software. A Ribed-surface design of the converterโ€™s flap is also introduced in this study to maximize wave-converter interaction. Besides, a Bi-level Hill Climbing Multi-Verse Optimization (HCMVO) method was also developed for this application. The results showed that the converter performs better with greater wave heights, flap freeboard heights, and shorter wave periods. Additionally, the added ribs led to more wave-converter interaction and better performance, while the distance between the flap and flume bed negatively impacted the performance. Finally, tracking the changes in the five-dimensional objective function revealed the optimum value for each parameter in all scenarios. This is achieved by the newly developed optimization algorithm, which is much faster than other existing cutting-edge metaheuristic approaches.

Keywords

Wave Energy Converter

OSWEC

Hydrodynamic Effects

Geometric Design

Metaheuristic Optimization

Multi-Verse Optimizer

1Introduction

The increase in energy demand, the limitations of fossil fuels, as well as environmental crises, such as air pollution and global warming, are the leading causes of calling more attention to harvesting renewable energy recently [1][2][3]. While still in its infancy, ocean wave energy has neither reached commercial maturity nor technological convergence. In recent decades, remarkable progress has been made in the marine energy domain, which is still in the early stage of development, to improve the technology performance level (TPL) [4][5]and technology readiness level (TRL) of wave energy converters (WECs). This has been achieved using novel modeling techniques [6][7][8][9][10][11][12][13][14] to gain the following advantages [15]: (i) As a source of sustainable energy, it contributes to the mix of energy resources that leads to greater diversity and attractiveness for coastal cities and suppliers. [16] (ii) Since wave energy can be exploited offshore and does not require any land, in-land site selection would be less expensive and undesirable visual effects would be reduced. [17] (iii) When the best layout and location of offshore site are taken into account, permanent generation of energy will be feasible (as opposed to using solar energy, for example, which is time-dependent) [18].

In general, the energy conversion process can be divided into three stages in a WEC device, including primary, secondary, and tertiary stages [19][20]. In the first stage of energy conversion, which is the subject of this study, the wave power is converted to mechanical power by wave-structure interaction (WSI) between ocean waves and structures. Moreover, the mechanical power is transferred into electricity in the second stage, in which mechanical structures are coupled with power take-off systems (PTO). At this stage, optimal control strategies are useful to tune the system dynamics to maximize power output [10][13][12]. Furthermore, the tertiary energy conversion stage revolves around transferring the non-standard AC power into direct current (DC) power for energy storage or standard AC power for grid integration [21][22]. We discuss only the first stage regardless of the secondary and tertiary stages. While Page 1 of 16 WECs include several categories and technologies such as terminators, point absorbers, and attenuators [15][23], we focus on oscillating surge wave energy converters (OSWECs) in this paper due to its high capacity for industrialization [24].

Over the past two decades, a number of studies have been conducted to understand how OSWECsโ€™ structures and interactions between ocean waves and flaps affect converters performance. Henry et al.โ€™s experiment on oscillating surge wave energy converters is considered as one of the most influential pieces of research [25], which demonstrated how the performance of oscillating surge wave energy converters (OSWECs) is affected by seven different factors, including wave period, wave power, flapโ€™s relative density, water depth, free-board of the flap, the gap between the tubes, gap underneath the flap, and flap width. These parameters were assessed in their two models in order to estimate the absorbed energy from incoming waves [26][27]. In addition, Folly et al. investigated the impact of water depth on the OSWECs performance analytically, numerically, and experimentally. According to this and further similar studies, the average annual incident wave power is significantly reduced by water depth. Based on the experimental results, both the surge wave force and the power capture of OSWECs increase in shallow water [28][29]. Following this, Sarkar et al. found that under such circumstances, the device that is located near the coast performs much better than those in the open ocean [30]. On the other hand, other studies are showing that the size of the converter, including height and width, is relatively independent of the location (within similar depth) [31]. Subsequently, Schmitt et al. studied OSWECs numerically and experimentally. In fact, for the simulation of OSWEC, OpenFOAM was used to test the applicability of Reynolds-averaged Navier-Stokes (RANS) solvers. Then, the experimental model reproduced the numerical results with satisfying accuracy [32]. In another influential study, Wang et al. numerically assessed the effect of OSWECโ€™s width on their performance. According to their findings, as converter width increases, its efficiency decreases in short wave periods while increases in long wave periods [33]. One of the main challenges in the analysis of the OSWEC is the coupled effect of hydrodynamic and geometric variables. As a result, numerous cutting-edge geometry studies have been performed in recent years in order to find the optimal structure that maximizes power output and minimizes costs. Garcia et al. reviewed hull geometry optimization studies in the literature in [19]. In addition, Guo and Ringwood surveyed geometric optimization methods to improve the hydrodynamic performance of OSWECs at the primary stage [14]. Besides, they classified the hull geometry of OSWECs based on Figure 1. Subsequently, Whittaker et al. proposed a different design of OSWEC called Oyster2. There have been three examples of different geometries of oysters with different water depths. Based on its water depth, they determined the width and height of the converter. They also found that in the constant wave period the less the converterโ€™s width, the less power captures the converter has [34]. Afterward, Oโ€™Boyle et al. investigated a type of OSWEC called Oyster 800. They compared the experimental and numerical models with the prototype model. In order to precisely reproduce the shape, mass distribution, and buoyancy properties of the prototype, a 40th-scale experimental model has been designed. Overall, all the models were fairly accurate according to the results [35].

Inclusive analysis of recent research avenues in the area of flap geometry has revealed that the interaction-based designs of such converters are emerging as a novel approach. An initiative workflow is designed in the current study to maximizing the wave energy extrication by such systems. To begin with, a sensitivity analysis plays its role of determining the best hydrodynamic values for installing the converterโ€™s flap. Then, all flap dimensions and characteristics come into play to finalize the primary model. Following, interactive designs is proposed to increase the influence of incident waves on the body by adding ribs on both sides of the flap as a novel design. Finally, a new bi-level metaheuristic method is proposed to consider the effects of simultaneous changes in ribs properties and other design parameters. We hope this novel approach will be utilized to make big-scale projects less costly and justifiable. The efficiency of the method is also compared with four well known metaheuristic algorithms and out weight them for this application.

This paper is organized as follows. First, the research methodology is introduced by providing details about the numerical model implementation. To that end, we first introduced the primary modelโ€™s geometry and software details. That primary model is later verified with a benchmark study with regard to the flap angle of rotation and water surface elevation. Then, governing equations and performance criteria are presented. In the third part of the paper, we discuss the modelโ€™s sensitivity to lower and upper parts width (we proposed a two cross-sectional design for the flap), bottom elevation, and freeboard. Finally, the novel optimization approach is introduced in the final part and compared with four recent metaheuristic algorithms.

2. Numerical Methods

In this section, after a brief introduction of the numerical software, Flow3D, boundary conditions are defined. Afterwards, the numerical model implementation, along with primary model properties are described. Finally, governing equations, as part of numerical process, are discussed.

2.1Model Setup

FLOW-3D is a powerful and comprehensive CFD simulation platform for studying fluid dynamics. This software has several modules to solve many complex engineering problems. In addition, modeling complex flows is simple and effective using FLOW-3Dโ€™s robust meshing capabilities [36]. Interaction between fluid and moving objects might alter the computational range. Dynamic meshes are used in our modeling to take these changes into account. At each time step, the computational node positions change in order to adapt the meshing area to the moving object. In addition, to choose mesh dimensions, some factors are taken into account such as computational accuracy, computational time, and stability. The final grid size is selected based on the detailed procedure provided in [37]. To that end, we performed grid-independence testing on a CFD model using three different mesh grid sizes of 0.01, 0.015, and 0.02 meters. The problem geometry and boundary conditions were defined the same, and simulations were run on all three grids under the same conditions. The predicted values of the relevant variable, such as velocity, was compared between the grids. The convergence behavior of the numerical solution was analyzed by calculating the relative L2 norm error between two consecutive grids. Based on the results obtained, it was found that the grid size of 0.02 meters showed the least error, indicating that it provided the most accurate and reliable solution among the three grids. Therefore, the grid size of 0.02 meters was selected as the optimal spatial resolution for the mesh grid.

In this work, the flume dimensions are 10 meters long, 0.1 meters wide, and 2.2 meters high, which are shown in figure2. In addition, input waves with linear characteristics have a height of 0.1 meters and a period of 1.4 seconds. Among the linear wave methods included in this software, RNGk-ฮต and k- ฮต are appropriate for turbulence model. The research of Lopez et al. shows that RNGk- ฮต provides the most accurate simulation of turbulence in OSWECs [21]. We use CATIA software to create the flap primary model and other innovative designs for this project. The flap measures 0.1 m x 0.65 m x 0.360 m in x, y and z directions, respectively. In Figure 3, the primary model of flap and its dimensions are shown. In this simulation, five boundaries have been defined, including 1. Inlet, 2. Outlet, 3. Converter flap, 4. Bed flume, and 5. Water surface, which are shown in figure 2. Besides, to avoid wave reflection in inlet and outlet zones, Flow3D is capable of defining some areas as damping zones, the length of which has to be one to one and a half times the wavelength. Therefore, in the model, this length is considered equal to 2 meters. Furthermore, there is no slip in all the boundaries. In other words, at every single time step, the fluid velocity is zero on the bed flume, while it is equal to the flap velocity on the converter flap. According to the wave theory defined in the software, at the inlet boundary, the water velocity is called from the wave speed to be fed into the model.

2.2Verification

In the current study, we utilize the Schmitt experimental model as a benchmark for verification, which was developed at the Queenโ€™s University of Belfast. The experiments were conducted on the flap of the converter, its rotation, and its interaction with the water surface. Thus, the details of the experiments are presented below based up on the experimental setupโ€™s description [38]. In the experiment, the laboratory flume has a length of 20m and a width of 4.58m. Besides, in order to avoid incident wave reflection, a wave absorption source is devised at the end of the left flume. The flume bed, also, includes two parts with different slops. The flap position and dimensions of the flume can be seen in Figure4. In addition, a wave-maker with 6 paddles is installed at one end. At the opposite end, there is a beach with wire meshes. Additionally, there are 6 indicators to extract the water level elevation. In the flap model, there are three components: the fixed support structure, the hinge, and the flap. The flap measures 0.1m x 0.65m x 0.341m in x, y and z directions, respectively. In Figure5, the details are given [32]. The support structure consists of a 15 mm thick stainless steel base plate measuring 1m by 1.4m, which is screwed onto the bottom of the tank. The hinge is supported by three bearing blocks. There is a foam centerpiece on the front and back of the flap which is sandwiched between two PVC plates. Enabling changes of the flap, three metal fittings link the flap to the hinge. Moreover, in this experiment, the selected wave is generated based on sea wave data at scale 1:40. The wave height and the wave period are equal to 0.038 (m) and 2.0625 (s), respectively, which are tantamount to a wave with a period of 13 (s) and a height of 1.5 (m).

Two distinct graphs illustrate the numerical and experi-mental study results. Figure6 and Figure7 are denoting the angle of rotation of flap and surface elevation in computational and experimental models, respectively. The two figures roughly represent that the numerical and experimental models are a good match. However, for the purpose of verifying the match, we calculated the correlation coefficient (C) and root mean square error (RMSE). According to Figure6, correlation coefficient and RMSE are 0.998 and 0.003, respectively, and in Figure7 correlation coefficient and RMSE are respectively 0.999 and 0.001. Accordingly, there is a good match between the numerical and empirical models. It is worth mentioning that the small differences between the numerical and experimental outputs may be due to the error of the measuring devices and the calibration of the data collection devices.

Including continuity equation and momentum conserva- tion for incompressible fluid are given as [32][39]:(1)

where P represents the pressure, g denotes gravitational acceleration, u represents fluid velocity, and Di is damping coefficient. Likewise, the model uses the same equation. to calculate the fluid velocity in other directions as well. Considering the turbulence, we use the two-equation model of RNGK- ฮต. These equations are:

(3)๏ฟฝ๏ฟฝt(๏ฟฝ๏ฟฝ)+๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ(๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ)=๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ[๏ฟฝeff๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ]+๏ฟฝ๏ฟฝ-๏ฟฝ๏ฟฝand(4)๏ฟฝ๏ฟฝ๏ฟฝ(๏ฟฝ๏ฟฝ)+๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ(๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ)=๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ[๏ฟฝeff๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ]+๏ฟฝ1๏ฟฝโˆ—๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ-๏ฟฝ๏ฟฝ2๏ฟฝ๏ฟฝ2๏ฟฝWhere ๏ฟฝ2๏ฟฝ and ๏ฟฝ1๏ฟฝ are constants. In addition, ๏ฟฝ๏ฟฝ and ๏ฟฝ๏ฟฝ represent the turbulent Prandtl number of ๏ฟฝ and k, respectively.

๏ฟฝ๏ฟฝ also denote the production of turbulent kinetic energy of k under the effect of velocity gradient, which is calculated as follows:(5)๏ฟฝ๏ฟฝ=๏ฟฝeff[๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ+๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ]๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ(6)๏ฟฝeff=๏ฟฝ+๏ฟฝ๏ฟฝ(7)๏ฟฝeff=๏ฟฝ+๏ฟฝ๏ฟฝwhere ๏ฟฝ is molecular viscosity,๏ฟฝ๏ฟฝ represents turbulence viscosity, k denotes kinetic energy, and โˆŠโˆŠ is energy dissipation rate. The values of constant coefficients in the two-equation RNGK โˆŠ-โˆŠ model is as shown in the Table 1 [40].Table 2.

Table 1. Constant coefficients in RNGK-โˆŠ model

Factors๏ฟฝ๏ฟฝ0๏ฟฝ1๏ฟฝ2๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ
Quantity0.0124.381.421.681.391.390.084

Table 2. Flap properties

Joint height (m)0.476
Height of the center of mass (m)0.53
Weight (Kg)10.77

It is worth mentioning that the volume of fluid method is used to separate water and air phases in this software [41]. Below is the equation of this method [40].(8)๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ+๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ(๏ฟฝ๏ฟฝ๏ฟฝ)=0where ฮฑ and 1 โˆ’ ฮฑ are portion of water phase and air phase, respectively. As a weighting factor, each fluid phase portion is used to determine the mixture properties. Finally, using the following equations, we calculate the efficiency of converters [42][34][43]:(9)๏ฟฝ=14|๏ฟฝ|2๏ฟฝ+๏ฟฝ2+(๏ฟฝ+๏ฟฝa)2(๏ฟฝn2-๏ฟฝ2)2where ๏ฟฝ๏ฟฝ represents natural frequency, I denotes the inertia of OSWEC, Ia is the added inertia, F is the complex wave force, and B denotes the hydrodynamic damping coefficient. Afterward, the capture factor of the converter is calculated by [44]:(10)๏ฟฝ๏ฟฝ=๏ฟฝ1/2๏ฟฝ๏ฟฝ2๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝgw where ๏ฟฝ๏ฟฝ represents the capture factor, which is the total efficiency of device per unit length of the wave crest at each time step [15], ๏ฟฝ๏ฟฝ represent the dimensional amplitude of the incident wave, w is the flapโ€™s width, and Cg is the group velocity of the incident wave, as below:(11)๏ฟฝ๏ฟฝ=๏ฟฝ๏ฟฝ0ยท121+2๏ฟฝ0โ„Žsinh2๏ฟฝ0โ„Žwhere ๏ฟฝ0 denotes the wave number, h is water depth, and H is the height of incident waves.

According to previous sections โˆŠ,๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ-โˆŠ modeling is used for all models simulated in this section. For this purpose, the empty boundary condition is used for flume walls. In order to preventing wave reflection at the inlet and outlet of the flume, the length of wave absorption is set to be at least one incident wavelength. In addition, the structured mesh is chosen, and the mesh dimensions are selected in two distinct directions. In each model, all grids have a length of 2 (cm) and a height of 1 (cm). Afterwards, as an input of the software for all of the models, we define the time step as 0.001 (s). Moreover, the run time of every simulation is 30 (s). As mentioned before, our primary model is Schmitt model, and the flap properties is given in table2. For all simulations, the flume measures 15 meters in length and 0.65 meters in width, and water depth is equal to 0.335 (m). The flap is also located 7 meters from the flumeโ€™s inlet.

Finally, in order to compare the results, the capture factor is calculated for each simulation and compared to the primary model. It is worth mentioning that capture factor refers to the ratio of absorbed wave energy to the input wave energy.

According to primary model simulation and due to the decreasing horizontal velocity with depth, the wave crest has the highest velocity. Considering the fact that the waveโ€™s orbital velocity causes the flap to move, the contact between the upper edge of the flap and the incident wave can enhance its performance. Additionally, the numerical model shows that the dynamic pressure decreases as depth increases, and the hydrostatic pressure increases as depth increases.

To determine the OSWEC design, it is imperative to understand the correlation between the capture factor, wave period, and wave height. Therefore, as it is shown in Figure8, we plot the change in capture factor over the variations in wave period and wave height in 3D and 2D. In this diagram, the first axis features changes in wave period, the second axis displays changes in wave height, and the third axis depicts changes in capture factor. According to our wave properties in the numerical model, the wave period and wave height range from 2 to 14 seconds and 2 to 8 meters, respectively. This is due to the fact that the flap does not oscillate if the wave height is less than 2 (m), and it does not reverse if the wave height is more than 8 (m). In addition, with wave periods more than 14 (s), the wavelength would be so long that it would violate the deep-water conditions, and with wave periods less than 2 (s), the flap would not oscillate properly due to the shortness of wavelength. The results of simulation are shown in Figure 8. As it can be perceived from Figure 8, in a constant wave period, the capture factor is in direct proportion to the wave height. It is because of the fact that waves with more height have more energy to rotate the flap. Besides, in a constant wave height, the capture factor increases when the wave period increases, until a given wave period value. However, the capture factor falls after this point. These results are expected since the flapโ€™s angular displacement is not high in lower wave periods, while the oscillating motion of that is not fast enough to activate the power take-off system in very high wave periods.

As is shown in Figure 9, we plot the change in capture factor over the variations in wave period (s) and water depth (m) in 3D. As it can be seen in this diagram, the first axis features changes in water depth (m), the second axis depicts the wave period (s), and the third axis displays OSWECโ€™s capture factor. The wave period ranges from 0 to 10 seconds based on our wave properties, which have been adopted from Schmittโ€™s model, while water depth ranges from 0 to 0.5 meters according to the flume and flap dimensions and laboratory limitations. According to Figure9, for any specific water depth, the capture factor increases in a varying rate when the wave period increases, until a given wave period value. However, the capture factor falls steadily after this point. In fact, the maximum capture factor occurs when the wave period is around 6 seconds. This trend is expected since, in a specific water depth, the flap cannot oscillate properly when the wavelength is too short. As the wave period increases, the flap can oscillate more easily, and consequently its capture factor increases. However, the capture factor drops in higher wave periods because the wavelength is too large to move the flap. Furthermore, in a constant wave period, by changing the water depth, the capture factor does not alter. In other words, the capture factor does not depend on the water depth when it is around its maximum value.

3Sensitivity Analysis

Based on previous studies, in addition to the flap design, the location of the flap relative to the water surface (freeboard) and its elevation relative to the flume bed (flap bottom elevation) play a significant role in extracting energy from the wave energy converter. This study measures the sensitivity of the model to various parameters related to the flap design including upper part width of the flap, lower part width of the flap, the freeboard, and the flap bottom elevation. Moreover, as a novel idea, we propose that the flap widths differ in the lower and upper parts. In Figure10, as an example, a flap with an upper thickness of 100 (mm) and a lower thickness of 50 (mm) and a flap with an upper thickness of 50 (mm) and a lower thickness of 100 (mm) are shown. The influence of such discrepancy between the widths of the upper and lower parts on the interaction between the wave and the flap, or in other words on the capture factor, is evaluated. To do so, other parameters are remained constant, such as the freeboard, the distance between the flap and the flume bed, and the wave properties.

In Figure11, models are simulated with distinct upper and lower widths. As it is clear in this figure, the first axis depicts the lower part width of the flap, the second axis indicates the upper part width of the flap, and the colors represent the capture factor values. Additionally, in order to consider a sufficient range of change, the flap thickness varies from half to double the value of the primary model for each part.

According to this study, the greater the discrepancy in these two parts, the lower the capture factor. It is on account of the fact that when the lower part of the flap is thicker than the upper part, and this thickness difference in these two parts is extremely conspicuous, the inertia against the motion is significant at zero degrees of rotation. Consequently, it is difficult to move the flap, which results in a low capture factor. Similarly, when the upper part of the flap is thicker than the lower part, and this thickness difference in these two parts is exceedingly noticeable, the inertia is so great that the flap can not reverse at the maximum degree of rotation. As the results indicate, the discrepancy can enhance the performance of the converter if the difference between these two parts is around 20%. As it is depicted in the Figure11, the capture factor reaches its own maximum amount, when the lower part thickness is from 5 to 6 (cm), and the upper part thickness is between 6 and 7 (cm). Consequently, as a result of this discrepancy, less material will be used, and therefore there will be less cost.

As illustrated in Figure12, this study examines the effects of freeboard (level difference between the flap top and water surface) and the flap bottom elevation (the distance between the flume bed and flap bottom) on the converter performance. In this diagram, the first axis demonstrates the freeboard and the second axis on the left side displays the flap bottom elevation, while the colors indicate the capture factor. In addition, the feasible range of freeboard is between -15 to 15 (cm) due to the limitation of the numerical model, so that we can take the wave slamming and the overtopping into consideration. Additionally, based on the Schmitt model and its scaled model of 1:40 of the base height, the flap bottom should be at least 9 (cm) high. Since the effect of surface waves is distributed over the depth of the flume, it is imperative to maintain a reasonable flap height exposed to incoming waves. Thus, the maximum flap bottom elevation is limited to 19 (cm). As the Figure12 pictures, at constant negative values of the freeboard, the capture factor is in inverse proportion with the flap bottom elevation, although slightly.

Furthermore, at constant positive values of the freeboard, the capture factor fluctuates as the flap bottom elevation decreases while it maintains an overall increasing trend. This is on account of the fact that increasing the flap bottom elevation creates turbulence flow behind the flap, which encumbers its rotation, as well as the fact that the flap surface has less interaction with the incoming waves. Furthermore, while keeping the flap bottom elevation constant, the capture factor increases by raising the freeboard. This is due to the fact that there is overtopping with adverse impacts on the converter performance when the freeboard is negative and the flap is under the water surface. Besides, increasing the freeboard makes the wave slam more vigorously, which improves the converter performance.

Adding ribs to the flap surface, as shown in Figure13, is a novel idea that is investigated in the next section. To achieve an optimized design for the proposed geometry of the flap, we determine the optimal number and dimensions of ribs based on the flap properties as our decision variables in the optimization process. As an example, Figure13 illustrates a flap with 3 ribs on each side with specific dimensions.

Figure14 shows the flow velocity field around the flap jointed to the flume bed. During the oscillation of the flap, the pressure on the upper and lower surfaces of the flap changes dynamically due to the changing angle of attack and the resulting change in the direction of fluid flow. As the flap moves upwards, the pressure on the upper surface decreases, and the pressure on the lower surface increases. Conversely, as the flap moves downwards, the pressure on the upper surface increases, and the pressure on the lower surface decreases. This results in a cyclic pressure variation around the flap. Under certain conditions, the pressure field around the flap can exhibit significant variations in magnitude and direction, forming vortices and other flow structures. These flow structures can affect the performance of the OSWEC by altering the lift and drag forces acting on the flap.

4Design Optimization

We consider optimizing the design parameters of the flap of converter using a nature-based swarm optimization method, that fall in the category of metaheuristic algorithms [45]. Accordingly, we choose four state-of-the-art algorithms to perform an optimization study. Then, based on their performances to achieve the highest capture factor, one of them will be chosen to be combined with the Hill Climb algorithm to carry out a local search. Therefore, in the remainder of this section, we discuss the search process of each algorithm and visualize their performance and convergence curve as they try to find the best values for decision variables.

4.1. Metaheuristic Approaches

As the first considered algorithm, the Gray Wolf Optimizer (GWO) algorithm simulates the natural leadership and hunting performance of gray wolves which tend to live in colonies. Hunters must obey the alpha wolf, the leader, who is responsible for hunting. Then, the beta wolf is at the second level of the gray wolf hierarchy. A subordinate of alpha wolf, beta stands under the command of the alpha. At the next level in this hierarchy, there are the delta wolves. They are subordinate to the alpha and beta wolves. This category of wolves includes scouts, sentinels, elders, hunters, and caretakers. In this ranking, omega wolves are at the bottom, having the lowest level and obeying all other wolves. They are also allowed to eat the prey just after others have eaten. Despite the fact that they seem less important than others, they are really central to the pack survival. Since, it has been shown that without omega wolves, the entire pack would experience some problems like fighting, violence, and frustration. In this simulation, there are three primary steps of hunting including searching, surrounding, and finally attacking the prey. Mathematically model of gray wolvesโ€™ hunting technique and their social hierarchy are applied in determined by optimization. this study. As mentioned before, gray wolves can locate their prey and surround them. The alpha wolf also leads the hunt. Assuming that the alpha, beta, and delta have more knowledge about prey locations, we can mathematically simulate gray wolf hunting behavior. Hence, in addition to saving the top three best solutions obtained so far, we compel the rest of the search agents (also the omegas) to adjust their positions based on the best search agent. Encircling behavior can be mathematically modeled by the following equations: [46].(12)๏ฟฝโ†’=|๏ฟฝโ†’ยท๏ฟฝ๏ฟฝโ†’(๏ฟฝ)-๏ฟฝโ†’(๏ฟฝ)|(13)๏ฟฝโ†’(๏ฟฝ+1)=๏ฟฝ๏ฟฝโ†’(๏ฟฝ)-๏ฟฝโ†’ยท๏ฟฝโ†’(14)๏ฟฝโ†’=2.๏ฟฝ2โ†’(15)๏ฟฝโ†’=2๏ฟฝโ†’ยท๏ฟฝ1โ†’-๏ฟฝโ†’Where ๏ฟฝโ†’indicates the position vector of gray wolf, ๏ฟฝ๏ฟฝโ†’ defines the vector of prey, t indicates the current iteration, and ๏ฟฝโ†’and ๏ฟฝโ†’are coefficient vectors. To force the search agent to diverge from the prey, we use ๏ฟฝโ†’ with random values greater than 1 or less than -1. In addition, Cโ†’ contains random values in the range [0,2], and ๏ฟฝโ†’ 1 and ๏ฟฝ2โ†’ are random vectors in [0,1]. The second considered technique is the Moth Flame Optimizer (MFO) algorithm. This method revolves around the mothsโ€™ navigation mechanism, which is realized by positioning themselves and maintaining a fixed angle relative to the moon while flying. This effective mechanism helps moths to fly in a straight path. However, when the source of light is artificial, maintaining an angle with the light leads to a spiral flying path towards the source that causes the mothโ€™s death [47]. In MFO algorithm, moths and flames are both solutions. The moths are actual search agents that fly in hyper-dimensional space by changing their position vectors, and the flames are considered pins that moths drop when searching the search space [48]. The problemโ€™s variables are the position of moths in the space. Each moth searches around a flame and updates it in case of finding a better solution. The fitness value is the return value of each mothโ€™s fitness (objective) function. The position vector of each moth is passed to the fitness function, and the output of the fitness function is assigned to the corresponding moth. With this mechanism, a moth never loses its best solution [49]. Some attributes of this algorithm are as follows:

  • โ€ขIt takes different values to converge moth in any point around the flame.
  • โ€ขDistance to the flame is lowered to be eventually minimized.
  • โ€ขWhen the position gets closer to the flame, the updated positions around the flame become more frequent.

As another method, the Multi-Verse Optimizer is based on a multiverse theory which proposes there are other universes besides the one in which we all live. According to this theory, there are more than one big bang in the universe, and each big bang leads to the birth of a new universe [50]. Multi-Verse Optimizer (MVO) is mainly inspired by three phenomena in cosmology: white holes, black holes, and wormholes. A white hole has never been observed in our universe, but physicists believe the big bang could be considered a white hole [51]. Black holes, which behave completely in contrast to white holes, attract everything including light beams with their extremely high gravitational force [52]. In the multiverse theory, wormholes are time and space tunnels that allow objects to move instantly between any two corners of a universe (or even simultaneously from one universe to another) [53]. Based on these three concepts, mathematical models are designed to perform exploration, exploitation, and local search, respectively. The concept of white and black holes is implied as an exploration phase, while the concept of wormholes is considered as an exploitation phase by MVO. Additionally, each solution is analogous to a universe, and each variable in the solution represents an object in that universe. Furthermore, each solution is assigned an inflation rate, and the time is used instead of iterations. Following are the universe rules in MVO:

  • โ€ขThe possibility of having white hole increases with the inflation rate.
  • โ€ขThe possibility of having black hole decreases with the inflation rate.
  • โ€ขObjects tend to pass through black holes more frequently in universes with lower inflation rates.
  • โ€ขRegardless of inflation rate, wormholes may cause objects in universes to move randomly towards the best universe. [54]

Modeling the white/black hole tunnels and exchanging objects of universes mathematically was accomplished by using the roulette wheel mechanism. With every iteration, the universes are sorted according to their inflation rates, then, based on the roulette wheel, the one with the white hole is selected as the local extremum solution. This is accomplished through the following steps:

Assume that

(16)๏ฟฝ๏ฟฝ๏ฟฝ=๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ1<๏ฟฝ๏ฟฝ(๏ฟฝ๏ฟฝ)๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ1โ‰ฅ๏ฟฝ๏ฟฝ(๏ฟฝ๏ฟฝ)

Where ๏ฟฝ๏ฟฝ๏ฟฝ represents the jth parameter of the ith universe, Ui indicates the ith universe, NI(Ui) is normalized inflation rate of the ith universe, r1 is a random number in [0,1], and j xk shows the jth parameter of the kth universe selected by a roulette wheel selection mechanism [54]. It is assumed that wormhole tunnels always exist between a universe and the best universe formed so far. This mechanism is as follows:(17)๏ฟฝ๏ฟฝ๏ฟฝ=if๏ฟฝ2<๏ฟฝ๏ฟฝ๏ฟฝ:๏ฟฝ๏ฟฝ+๏ฟฝ๏ฟฝ๏ฟฝร—((๏ฟฝ๏ฟฝ๏ฟฝ-๏ฟฝ๏ฟฝ๏ฟฝ)ร—๏ฟฝ4+๏ฟฝ๏ฟฝ๏ฟฝ)๏ฟฝ3<0.5๏ฟฝ๏ฟฝ-๏ฟฝ๏ฟฝ๏ฟฝร—((๏ฟฝ๏ฟฝ๏ฟฝ-๏ฟฝ๏ฟฝ๏ฟฝ)ร—๏ฟฝ4+๏ฟฝ๏ฟฝ๏ฟฝ)๏ฟฝ3โ‰ฅ0.5๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ:๏ฟฝ๏ฟฝ๏ฟฝwhere Xj indicates the jth parameter of the best universe formed so far, TDR and WEP are coefficients, where Xj indicates the jth parameter of the best universelbjshows the lower bound of the jth variable, ubj is the upper bound of the jth variable, and r2, r3, and r4 are random numbers in [1][54].

Finally, one of the newest optimization algorithms is WOA. The WOA algorithm simulates the movement of prey and the whaleโ€™s discipline when looking for their prey. Among several species, Humpback whales have a specific method of hunting [55]. Humpback whales can recognize the location of prey and encircle it before hunting. The optimal design position in the search space is not known a priori, and the WOA algorithm assumes that the best candidate solution is either the target prey or close to the optimum. This foraging behavior is called the bubble-net feeding method. Two maneuvers are associated with bubbles: upward spirals and double loops. A unique behavior exhibited only by humpback whales is bubble-net feeding. In fact, The WOA algorithm starts with a set of random solutions. At each iteration, search agents update their positions for either a randomly chosen search agent or the best solution obtained so far [56][55]. When the best search agent is determined, the other search agents will attempt to update their positions toward that agent. It is important to note that humpback whales swim around their prey simultaneously in a circular, shrinking circle and along a spiral-shaped path. By using a mathematical model, the spiral bubble-net feeding maneuver is optimized. The following equation represents this behavior:(18)๏ฟฝโ†’(๏ฟฝ+1)=๏ฟฝโ€ฒโ†’ยท๏ฟฝblยทcos(2๏ฟฝ๏ฟฝ)+๏ฟฝโˆ—โ†’(๏ฟฝ)

Where:(19)๏ฟฝโ€ฒโ†’=|๏ฟฝโˆ—โ†’(๏ฟฝ)-๏ฟฝโ†’(๏ฟฝ)|

Xโ†’(t+ 1) indicates the distance of the it h whale to the prey (best solution obtained so far),๏ฟฝ is a constant for defining the shape of the logarithmic spiral, l is a random number in [โˆ’1, 1], and dot (.) is an element-by-element multiplication [55].

Comparing the four above-mentioned methods, simulations are run with 10 search agents for 400 iterations. In Figure 15, there are 20 plots the optimal values of different parameters in optimization algorithms. The five parameters of this study are freeboard, bottom elevations, number of ribs on the converter, rib thickness, and rib Height. The optimal value for each was found by optimization algorithms, naming WOA, MVO, MFO, and GWO. By looking through the first row, the freeboard parameter converges to its maximum possible value in the optimization process of GWO after 300 iterations. Similarly, MFO finds the same result as GWO. In contrast, the freeboard converges to its minimum possible value in MVO optimizing process, which indicates positioning the converter under the water. Furthermore, WOA found the optimal value of freeboard as around 0.02 after almost 200 iterations. In the second row, the bottom elevation is found at almost 0.11 (m) in all algorithms; however, the curves follow different trends in each algorithm. The third row shows the number of ribs, where results immediately reveal that it should be over 4. All algorithms coincide at 5 ribs as the optimal number in this process. The fourth row displays the trends of algorithms to find optimal rib thickness. MFO finds the optimal value early and sets it to around 0.022, while others find the same value in higher iterations. Finally, regarding the rib height, MVO, MFO, and GWO state that the optimal value is 0.06 meters, but WOA did not find a higher value than 0.039.

4.2. HCMVO Bi-level Approach

Despite several strong search characteristics of MVO and its high performance in various optimization problems, it suffers from a few deficiencies in local and global search mechanisms. For instance, it is trapped in the local optimum when wormholes stochastically generate many solutions near the best universe achieved throughout iterations, especially in solving complex multimodal problems with high dimensions [57]. Furthermore, MVO needs to be modified by an escaping strategy from the local optima to enhance the global search abilities. To address these shortages, we propose a fast and effective meta-algorithm (HCMVO) to combine MVO with a Random-restart hill-climbing local search. This meta-algorithm uses MVO on the upper level to develop global tracking and provide a range of feasible and proper solutions. The hill-climbing algorithm is designed to develop a comprehensive neighborhood search around the best-found solution proposed by the upper-level (MVO) when MVO is faced with a stagnation issue or falling into a local optimum. The performance threshold is formulated as follows.(20)ฮ”๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝTHD=โˆ‘๏ฟฝ=1๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝTH๏ฟฝ๏ฟฝ-๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝTH๏ฟฝ๏ฟฝ-1๏ฟฝwhere BestTHDis the best-found solution per generation, andM is related to the domain of iterations to compute the average performance of MVO. If the proposed best solution by the local search is better than the initial one, the global best of MVO will be updated. HCMVO iteratively runs hill climbing when the performance of MVO goes down, each time with an initial condition to prepare for escaping such undesirable situations. In order to get a better balance between exploration and exploitation, the search step size linearly decreases as follows:(21)๏ฟฝ๏ฟฝ=๏ฟฝ๏ฟฝ-๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝMa๏ฟฝiter๏ฟฝ๏ฟฝ+1where iter and Maxiter are the current iteration and maximum number of evaluation, respectively. ๏ฟฝ๏ฟฝ stands for the step size of the neighborhood search. Meanwhile, this strategy can improve the convergence rate of MVO compared with other algorithms.

Algorithm 1 shows the technical details of the proposed optimization method (HCMVO). The initial solution includes freeboard (๏ฟฝ), bottom elevation (๏ฟฝ), number of ribs (Nr), rib thickness (๏ฟฝ), and rib height(๏ฟฝ).

5. Conclusion

The high trend of diminishing worldwide energy resources has entailed a great crisis upon vulnerable societies. To withstand this effect, developing renewable energy technologies can open doors to a more reliable means, among which the wave energy converters will help the coastal residents and infrastructure. This paper set out to determine the optimized design for such devices that leads to the highest possible power output. The main goal of this research was to demonstrate the best design for an oscillating surge wave energy converter using a novel metaheuristic optimization algorithm. In this regard, the methodology was devised such that it argued the effects of influential parameters, including wave characteristics, WEC design, and interaction criteria.

To begin with, a numerical model was developed in Flow 3D software to simulate the response of the flap of a wave energy converter to incoming waves, followed by a validation study based upon a well-reputed experimental study to verify the accuracy of the model. Secondly, the hydrodynamics of the flap was investigated by incorporating the turbulence. The effect of depth, wave height, and wave period are also investigated in this part. The influence of two novel ideas on increasing the wave-converter interaction was then assessed: i) designing a flap with different widths in the upper and lower part, and ii) adding ribs on the surface of the flap. Finally, four trending single-objective metaheuristic optimization methods

Empty CellAlgorithm 1: Hill Climb Multiverse Optimization
01:procedure HCMVO
02:๏ฟฝ=30,๏ฟฝ=5โ–น๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ
03:๏ฟฝ=ใ€ˆF1,B1,N,R,H1ใ€‰,โ€ฆใ€ˆFN,B2,N,R,HNใ€‰โ‡’lb1Nโฉฝ๏ฟฝโฉฝubN
04:Initialize parameters๏ฟฝER,๏ฟฝDR,๏ฟฝEP,Best๏ฟฝ,๏ฟฝ๏ฟฝ๏ฟฝite๏ฟฝ๏ฟฝโ–นWormhole existence probability (WEP)
05:๏ฟฝ๏ฟฝ=๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ(๏ฟฝ๏ฟฝ)
06:๏ฟฝ๏ฟฝ=Normalize the inflation rate๏ฟฝ๏ฟฝ
07:for iter in[1,โ‹ฏ,๏ฟฝ๏ฟฝ๏ฟฝiter]do
08:for๏ฟฝin[1,โ‹ฏ,๏ฟฝ]do
09:Update๏ฟฝEP,๏ฟฝDR,Black๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝIndex=๏ฟฝ
10:for๏ฟฝ๏ฟฝ๏ฟฝ[1,โ‹ฏ,๏ฟฝ]๏ฟฝ๏ฟฝ
11:๏ฟฝ1=๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ()
12:if๏ฟฝ1โ‰ค๏ฟฝ๏ฟฝ(๏ฟฝ๏ฟฝ)then
13:White HoleIndex=Roulette๏ฟฝheelSelection(-๏ฟฝ๏ฟฝ)
14:๏ฟฝ(Black HoleIndex,๏ฟฝ)=๏ฟฝ๏ฟฝ(White HoleIndex,๏ฟฝ)
15:end if
16:๏ฟฝ2=๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ([0,๏ฟฝ])
17:if๏ฟฝ2โ‰ค๏ฟฝEPthen
18:๏ฟฝ3=๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ(),๏ฟฝ4=๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ()
19:if๏ฟฝ3<0.5then
20:๏ฟฝ1=((๏ฟฝ๏ฟฝ(๏ฟฝ)-๏ฟฝ๏ฟฝ(๏ฟฝ))ร—๏ฟฝ4+๏ฟฝ๏ฟฝ(๏ฟฝ))
21:๏ฟฝ(๏ฟฝ,๏ฟฝ)=Best๏ฟฝ(๏ฟฝ)+๏ฟฝDRร—๏ฟฝ
22:else
23:๏ฟฝ(๏ฟฝ,๏ฟฝ)=Best๏ฟฝ(๏ฟฝ)-๏ฟฝDRร—๏ฟฝ
24:end if
25:end if
26:end for
27:end for
28:๏ฟฝHD=๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ([๏ฟฝ1,๏ฟฝ2,โ‹ฏ,๏ฟฝNp])
29:Bes๏ฟฝTH๏ฟฝitr=๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝHD
30:ฮ”BestTHD=โˆ‘๏ฟฝ=1๏ฟฝBestTII๏ฟฝ๏ฟฝ-BestTII๏ฟฝ๏ฟฝ-1๏ฟฝ
31:ifฮ”BestTHD<๏ฟฝ๏ฟฝthenโ–นPerform hill climbing local search
32:BestTHD=๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ-๏ฟฝlim๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝTHD
33:end if
34:end for
35:return๏ฟฝ,BestTHDโ–นFinal configuration
36:end procedure

The implementation details of the hill-climbing algorithm applied in HCMPA can be seen in Algorithm 2. One of the critical parameters isg, which denotes the resolution of the neighborhood search around the proposed global best by MVO. If we set a small step size for hill-climbing, the convergence speed will be decreased. On the other hand, a large step size reinforces the exploration ability. Still, it may reduce the exploitation ability and in return increase the act of jumping from a global optimum or surfaces with high-potential solutions. Per each decision variable, the neighborhood search evaluates two different direct searches, incremental or decremental. After assessing the generated solutions, the best candidate will be selected to iterate the search algorithm. It is noted that the hill-climbing algorithm should not be applied in the initial iteration of the optimization process due to the immense tendency for converging to local optima. Meanwhile, for optimizing largescale problems, hill-climbing is not an appropriate selection. In order to improve understanding of the proposed hybrid optimization algorithmโ€™s steps, the flowchart of HCMVO is designed and can be seen in Figure 16.

Figure 17 shows the observed capture factor (which is the absorbed energy with respect to the available energy) by each optimization algorithm from iterations 1 to 400. The algorithms use ten search agents in their modified codes to find the optimal solutions. While GWO and MFO remain roughly constant after iterations 54 and 40, the other three algorithms keep improving the capture factor. In this case, HCMVO and MVO worked very well in the optimizing process with a capture factor obtained by the former as 0.594 and by the latter as 0.593. MFO almost found its highest value before the iteration 50, which means the exploration part of the algorithm works out well. Similarly, HCMVO does the same. However, it keeps finding the better solution during the optimization process until the last iteration, indicating the strong exploitation part of the algorithm. GWO reveals a weakness in exploration and exploitation because not only does it evoke the least capture factor value, but also the curve remains almost unchanged throughout 350 iterations.

Figure 18 illustrates complex interactions between the five optimization parameters and the capture factor for HCMVO (a), MPA (b), and MFO (c) algorithms. The first interesting observation is that there is a high level of nonlinear relationships among the setting parameters that can make a multi-modal search space. The dark blue lines represent the best-found configuration throughout the optimisation process. Based on both HCMVO (a) and MVO (b), we can infer that the dark blue lines concentrate in a specific range, showing the high convergence ability of both HCMVO and MVO. However, MFO (c) could not find the exact optimal range of the decision variables, and the best-found solutions per generation distribute mostly all around the search space.

Empty CellAlgorithm 1: Hill Climb Multiverse Optimization
01:procedure HCMVO
02:Initialization
03:Initialize the constraints๏ฟฝ๏ฟฝ1๏ฟฝ,๏ฟฝ๏ฟฝ1๏ฟฝ
04:๏ฟฝ1๏ฟฝ=Mi๏ฟฝ1๏ฟฝ+๏ฟฝ๏ฟฝ๏ฟฝ1๏ฟฝ/๏ฟฝโ–นCompute the step size,๏ฟฝis search resolution
05:So๏ฟฝ1=ใ€ˆ๏ฟฝ,๏ฟฝ,๏ฟฝ,๏ฟฝ,๏ฟฝใ€‰โ–น๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ
06:๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ1=๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝSo๏ฟฝ1โ–น๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝโ„Ž๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ
07:Main loop
08:for iterโ‰ค๏ฟฝ๏ฟฝ๏ฟฝita=do
09:๏ฟฝ๏ฟฝ๏ฟฝ=๏ฟฝ๏ฟฝ๏ฟฝยฑ๏ฟฝ๏ฟฝ
10:while๏ฟฝโ‰ค๏ฟฝ๏ฟฝ๏ฟฝ(Sol1)do
11:๏ฟฝ๏ฟฝ๏ฟฝ=๏ฟฝ๏ฟฝ๏ฟฝ+๏ฟฝ,โ–น๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝโ„Ž๏ฟฝ๏ฟฝ๏ฟฝโ„Ž๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝโ„Ž
12:fitness๏ฟฝ๏ฟฝiter=๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ
13:t = t+1
14:end while
15:ใ€ˆ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ,๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝmaxใ€‰=๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ
16:๏ฟฝ๏ฟฝ๏ฟฝitev=๏ฟฝ๏ฟฝ๏ฟฝInde๏ฟฝmaxโ–น๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝโ„Ž๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝโ„Ž๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ
17:๏ฟฝ๏ฟฝ=๏ฟฝ๏ฟฝ-๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝMax๏ฟฝ๏ฟฝ+1โ–น๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ
18:end for
19:return๏ฟฝ๏ฟฝ๏ฟฝiter,๏ฟฝ๏ฟฝ๏ฟฝ๏ฟฝ
20:end procedure

were utilized to illuminate the optimum values of the design parameters, and the best method was chosen to develop a new algorithm that performs both local and global search methods.

The correlation between hydrodynamic parameters and the capture factor of the converter was supported by the results. For any given water depth, the capture factor increases as the wave period increases, until a certain wave period value (6 seconds) is reached, after which the capture factor gradually decreases. It is expected since the flap cannot oscillate effectively when the wavelength is too short for a certain water depth. Conversely, when the wavelength is too long, the capture factor decreases. Furthermore, under a constant wave period, increasing the water depth does not affect the capture factor. Regarding the sensitivity analysis, the study found that increasing the flap bottom elevation causes turbulence flow behind the flap and limitation of rotation, which leads to less interaction with the incoming waves. Furthermore, while keeping the flap bottom elevation constant, increasing the freeboard improves the capture factor. Overtopping happens when the freeboard is negative and the flap is below the water surface, which has a detrimental influence on converter performance. Furthermore, raising the freeboard causes the wave impact to become more violent, which increases converter performance.

In the last part, we discussed the search process of each algorithm and visualized their performance and convergence curves as they try to find the best values for decision variables. Among the four selected metaheuristic algorithms, the Multi-verse Optimizer proved to be the most effective in achieving the best answer in terms of the WEC capture factor. However, the MVO needed modifications regarding its escape approach from the local optima in order to improve its global search capabilities. To overcome these constraints, we presented a fast and efficient meta-algorithm (HCMVO) that combines MVO with a Random-restart hill-climbing local search. On a higher level, this meta-algorithm employed MVO to generate global tracking and present a range of possible and appropriate solutions. Taken together, the results demonstrated that there is a significant degree of nonlinearity among the setup parameters that might result in a multimodal search space. Since MVO was faced with a stagnation issue or fell into a local optimum, we constructed a complete neighborhood search around the best-found solution offered by the upper level. In sum, the newly-developed algorithm proved to be highly effective for the problem compared to other similar optimization methods. The strength of the current findings may encourage future investigation on design optimization of wave energy converters using developed geometry as well as the novel approach.

CRediT authorship contribution statement

Erfan Amini: Conceptualization, Methodology, Validation, Data curation, Writing โ€“ original draft, Writing โ€“ review & editing, Visualization. Mahdieh Nasiri: Conceptualization, Methodology, Validation, Data curation, Writing โ€“ original draft, Writing โ€“ review & editing, Visualization. Navid Salami Pargoo: Writing โ€“ original draft, Writing โ€“ review & editing. Zahra Mozhgani: Conceptualization, Methodology. Danial Golbaz: Writing โ€“ original draft. Mehrdad Baniesmaeil: Writing โ€“ original draft. Meysam Majidi Nezhad: . Mehdi Neshat: Supervision, Conceptualization, Writing โ€“ original draft, Writing โ€“ review & editing, Visualization. Davide Astiaso Garcia: Supervision. Georgios Sylaios: Supervision.

Declaration of Competing Interest

The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.

Acknowledgement

This research has been carried out within ILIAD (Inte-grated Digital Framework for Comprehensive Maritime Data and Information Services) project that received funding from the European Unionโ€™s H2020 programme.

Data availability

Data will be made available on request.

References

Image (1) the view of vortex breaker morning glory spillway in operation

ํ๋ฆ„์˜ ์ˆ˜๋ฆฌํ•™์— ๋Œ€ํ•œ ์™€๋ฅ˜ ์ฐจ๋‹จ๊ธฐ์˜ ์˜ํ–ฅ ์กฐ์‚ฌ

Investigating the impact of the vortex breaker on the hydraulics of the flow
(empirical hydraulic coefficient) passing over the morning glory spillway
Roozbeh Aghamajidi1 1– Assistant Professor, Faculty of Engineering, Islamic Azad University, Sepidan Unit, Fars, Iran
Received: 05 November 2022; Revised: 11 December 2022; Accepted: 10 January 2023; Published: 11 January
2023

Abstract

In recent decades, many dams have been built. Due to the high need for water and the increasing soil
erosion in different areas, the need and sensation to build a dam is quite obvious. In 1900, the number
of large dams did not exceed 50. However, between 1950 and 1986, the number of large dams (more
than 15 meters high) was more than 39,000. Since the 70s, the construction of dams has been
developing more and more. This expansion has been more visible in the Asian, Central and South
American regions. According to the construction purpose, each dam structure must be able to pass the
volume of excess water caused by the flood, and for this purpose, various structures such as spillways
are used. The spillways are different according to the type of exploitation and the type of project. In
other words, there are different types of leaks. Which are one of these types of shaft spillway. The
spillway of a morning glory consists of a circular crest that directs the flow to an inclined or vertical
axis. The mentioned axis is connected to a conduct way with a low gradient. In this research, in order
to investigate the performance of both vortex breakers on the hydraulic spillway of morning glory,
several tests have been conducted with various types of vortex breakers. The results show that the best
vorticity channel with a low height and length is an arrangement of 6, which increases the flow rate by
23%. It should be noted that increasing the thickness of the vortex breaker by more than 7% of the
spillway radius does not have much effect on the increase of the hydraulic coefficient.

Image (1) the view of old stepped morning glory spillway in operation
Image (1) the view of old stepped morning glory spillway in operation

์ตœ๊ทผ ์ˆ˜์‹ญ ๋…„ ๋™์•ˆ ๋งŽ์€ ๋Œ์ด ๊ฑด์„ค๋˜์—ˆ์Šต๋‹ˆ๋‹ค. ๋ฌผ์— ๋Œ€ํ•œ ๋†’์€ ์ˆ˜์š”์™€ ์—ฌ๋Ÿฌ ์ง€์—ญ์—์„œ ์ฆ๊ฐ€ํ•˜๋Š” ํ† ์–‘ ์นจ์‹์œผ๋กœ ์ธํ•ด ๋Œ ๊ฑด์„ค์˜ ํ•„์š”์„ฑ๊ณผ ๊ฐ๊ฐ์€ ๋งค์šฐ ๋ถ„๋ช…ํ•ฉ๋‹ˆ๋‹ค. 1900๋…„์—๋Š” ๋Œ€ํ˜• ๋Œ์˜ ์ˆ˜๊ฐ€ 50๊ฐœ๋ฅผ ๋„˜์ง€ ์•Š์•˜์ง€๋งŒ 1950๋…„์—์„œ 1986๋…„ ์‚ฌ์ด์— ๋Œ€ํ˜• ๋Œ(๋†’์ด 15๋ฏธํ„ฐ ์ด์ƒ)์˜ ์ˆ˜๋Š” 39,000๊ฐœ๊ฐ€ ๋„˜์—ˆ์Šต๋‹ˆ๋‹ค. 70๋…„๋Œ€ ์ดํ›„ ๋Œ ๊ฑด์„ค์€ ์ ์  ๋” ๋ฐœ์ „ํ•ด ์™”์Šต๋‹ˆ๋‹ค.

์ด๋Ÿฌํ•œ ํ™•์žฅ์€ ์•„์‹œ์•„, ์ค‘๋‚จ๋ฏธ ์ง€์—ญ์—์„œ ๋” ๋‘๋“œ๋Ÿฌ์กŒ์Šต๋‹ˆ๋‹ค. ๊ฐ ๋Œ ๊ตฌ์กฐ๋ฌผ์€ ์‹œ๊ณต๋ชฉ์ ์— ๋”ฐ๋ผ ํ™์ˆ˜๋กœ ์ธํ•œ ๊ณผ์ž‰์ˆ˜๋Ÿ‰์„ ํ†ต๊ณผํ•  ์ˆ˜ ์žˆ์–ด์•ผ ํ•˜๋ฉฐ ์ด๋ฅผ ์œ„ํ•ด ์—ฌ์ˆ˜๋กœ ๋“ฑ ๋‹ค์–‘ํ•œ ๊ตฌ์กฐ๋ฌผ์ด ์‚ฌ์šฉ๋œ๋‹ค. ์—ฌ์ˆ˜๋กœ๋Š” ๊ฐœ๋ฐœ ์œ ํ˜•๊ณผ ํ”„๋กœ์ ํŠธ ์œ ํ˜•์— ๋”ฐ๋ผ ๋‹ค๋ฆ…๋‹ˆ๋‹ค. ์ฆ‰, ๋‹ค์–‘ํ•œ ์œ ํ˜•์˜ ๋ˆ„์ถœ์ด ์žˆ์Šต๋‹ˆ๋‹ค.

์ƒคํ”„ํŠธ ์—ฌ์ˆ˜๋กœ์˜ ์ด๋Ÿฌํ•œ ์œ ํ˜• ์ค‘ ํ•˜๋‚˜์ž…๋‹ˆ๋‹ค. ๋‚˜ํŒ”๊ฝƒ์˜ ์—ฌ์ˆ˜๋กœ๋Š” ํ๋ฆ„์„ ๊ฒฝ์‚ฌ ๋˜๋Š” ์ˆ˜์ง ์ถ•์œผ๋กœ ํ–ฅํ•˜๊ฒŒ ํ•˜๋Š” ์›ํ˜• ๋งˆ๋ฃจ๋กœ ๊ตฌ์„ฑ๋ฉ๋‹ˆ๋‹ค. ์–ธ๊ธ‰๋œ ์ถ•์€ ๊ธฐ์šธ๊ธฐ๊ฐ€ ๋‚ฎ์€ ์ „๋„ ๋ฐฉ์‹์— ์—ฐ๊ฒฐ๋ฉ๋‹ˆ๋‹ค. ๋ณธ ์—ฐ๊ตฌ์—์„œ๋Š” ๋‚˜ํŒ”๊ฝƒ ์ˆ˜๋กœ์—์„œ ๋‘ ๊ฐ€์ง€ ์™€๋ฅ˜ ์ฐจ๋‹จ๊ธฐ์˜ ์„ฑ๋Šฅ์„ ์กฐ์‚ฌํ•˜๊ธฐ ์œ„ํ•ด ๋‹ค์–‘ํ•œ ์œ ํ˜•์˜ ์™€๋ฅ˜ ์ฐจ๋‹จ๊ธฐ๋กœ ์—ฌ๋Ÿฌ ํ…Œ์ŠคํŠธ๋ฅผ ์ˆ˜ํ–‰ํ–ˆ์Šต๋‹ˆ๋‹ค.

๊ทธ ๊ฒฐ๊ณผ ๋†’์ด์™€ ๊ธธ์ด๊ฐ€ ๋‚ฎ์€ ์ตœ์ ์˜ vorticity ์ฑ„๋„์€ 6๊ฐœ ๋ฐฐ์—ด๋กœ ์œ ๋Ÿ‰์ด 23% ์ฆ๊ฐ€ํ•˜๋Š” ๊ฒƒ์œผ๋กœ ๋‚˜ํƒ€๋‚ฌ๋‹ค. ์™€๋ฅ˜ ์ฐจ๋‹จ๊ธฐ์˜ ๋‘๊ป˜๋ฅผ ์—ฌ์ˆ˜๋กœ ๋ฐ˜๊ฒฝ์˜ 7% ์ด์ƒ ์ฆ๊ฐ€์‹œํ‚ค๋Š” ๊ฒƒ์€ ์ˆ˜๋ฆฌ ๊ณ„์ˆ˜์˜ ์ฆ๊ฐ€์— ํฐ ์˜ํ–ฅ์„ ๋ฏธ์น˜์ง€ ์•Š๋Š”๋‹ค๋Š” ์ ์— ์œ ์˜ํ•ด์•ผ ํ•ฉ๋‹ˆ๋‹ค.

Keywords:

Morning Glory Spillway, Vortex Breaker, Arrangement, Hydraulic Behavior

Figure 15. Velocity distribution of impinging jet on a wall under different Reynolds numbers.

Hydraulic Characteristics of Continuous Submerged Jet Impinging on a Wall by Using Numerical Simulation and PIV Experiment

byย Hongbo Miย 1,2, Chuan Wangย 1,3, Xuanwen Jiaย 3,*, Bo Huย 2, Hongliang Wangย 4, Hui Wangย 3ย and Yong Zhuย 5

1College of Mechatronics Engineering, Hainan Vocational University of Science and Technology, Haikou 571126, China

2Department of Energy and Power Engineering, Tsinghua University, Beijing 100084, China

3College of Hydraulic Science and Engineering, Yangzhou University, Yangzhou 225009, China

4School of Aerospace and Mechanical Engineering/Flight College, Changzhou Institute of Technology, Changzhou 213032, China

5National Research Center of Pumps, Jiangsu University, Zhenjiang 212013, China

*Author to whom correspondence should be addressed.Sustainability2023,ย 15(6), 5159;ย https://doi.org/10.3390/su15065159

Received: 30 January 2023ย /ย Revised: 4 March 2023ย /ย Accepted: 10 March 2023ย /ย Published: 14 March 2023(This article belongs to the Special Issueย Advanced Technologies of Renewable Energy and Water Management for Sustainable Environment

Abstract

Due to their high efficiency, low heat loss and associated sustainability advantages, impinging jets have been used extensively in marine engineering, geotechnical engineering and other engineering practices. In this paper, the flow structure and impact characteristics of impinging jets with different Reynolds numbers and impact distances are systematically studied by Flow-3D based on PIV experiments. In the study, the relevant state parameters of the jets are dimensionlessly treated, obtaining not only the linear relationship between the length of the potential nucleation zone and the impinging distance, but also the linear relationship between the axial velocity and the axial distance in the impinging zone. In addition, after the jet impinges on the flat plate, the vortex action range caused by the wall-attached flow of the jet gradually decreases inward with the increase of the impinging distance. By examining the effect of Reynolds number Re on the hydraulic characteristics of the submerged impact jet, it can be found that the structure of the continuous submerged impact jet is relatively independent of the Reynolds number. At the same time, the final simulation results demonstrate the applicability of the linear relationship between the length of the potential core region and the impact distance. This study provides methodological guidance and theoretical support for relevant engineering practice and subsequent research on impinging jets, which has strong theoretical and practical significance.

Keywords: 

PIV;ย Flow-3D;ย impinging jet;ย hydraulic characteristics;ย impinging distance

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Figure 1. Geometric model.

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Figure 2.ย Model grid schematic.

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Figure 3.ย (a) Schematic diagram of the experimental setup; (b) PIV images of vertical impinging jets with velocity fields.

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Figure 4. (a) Velocity distribution verification at the outlet of the jet pipe; (b) Distribution of flow angle in the mid-axis of the jet [39].

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Figure 5. Along-range distribution of the dimensionless axial velocity of the jet at different impact distances.Figure 6 shows the variation of H

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Figure 6.ย Relationship between the distribution of potential core region and the impact heightย H/D.

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Figure 7. The relationship between the potential core length 

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Figure 8.ย Along-range distribution of the flow angleย ฯ†ย of the jet at different impact distances.

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Figure 9.ย Velocity distribution along the axis of the jet at different impinging regions.

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Figure 10. The absolute value distribution of slope under different impact distances.

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Figure 11. Velocity distribution of impinging jet on wall under different impinging distances.

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Figure 12.ย Along-range distribution of the dimensionless axial velocity of the jet at different Reynolds numbers.

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Figure 13. Along-range distribution of the flow angle ฯ† of the jet at different Reynolds numbers.

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Figure 14. Velocity distribution along the jet axis at different Reynolds numbers.

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Figure 15. Velocity distribution of impinging jet on a wall under different Reynolds numbers.

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Mi, H.; Wang, C.; Jia, X.; Hu, B.; Wang, H.; Wang, H.; Zhu, Y. Hydraulic Characteristics of Continuous Submerged Jet Impinging on a Wall by Using Numerical Simulation and PIV Experiment. Sustainability 202315, 5159. https://doi.org/10.3390/su15065159

AMA Style

Mi H, Wang C, Jia X, Hu B, Wang H, Wang H, Zhu Y. Hydraulic Characteristics of Continuous Submerged Jet Impinging on a Wall by Using Numerical Simulation and PIV Experiment. Sustainability. 2023; 15(6):5159. https://doi.org/10.3390/su15065159Chicago/Turabian Style

Mi, Hongbo, Chuan Wang, Xuanwen Jia, Bo Hu, Hongliang Wang, Hui Wang, and Yong Zhu. 2023. “Hydraulic Characteristics of Continuous Submerged Jet Impinging on a Wall by Using Numerical Simulation and PIV Experiment” Sustainability 15, no. 6: 5159. https://doi.org/10.3390/su15065159

Figure 5 A schematic of the water model of reactor URO 200.

Physical and Numerical Modeling of the Impeller Construction Impact on the Aluminum Degassing Process

์•Œ๋ฃจ๋ฏธ๋Š„ ํƒˆ๊ธฐ ๊ณต์ •์— ๋ฏธ์น˜๋Š” ์ž„ํŽ ๋Ÿฌ ๊ตฌ์„ฑ์˜ ๋ฌผ๋ฆฌ์  ๋ฐ ์ˆ˜์น˜์  ๋ชจ๋ธ๋ง

Kamil Kuglin,1 Michaล‚ Szucki,2 Jacek Pieprzyca,3 Simon Genthe,2 Tomasz Merder,3 and Dorota Kalisz1,*

Mikael Ersson, Academic Editor

Author information Article notes Copyright and License information Disclaimer

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Data Availability Statement

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Abstract

This paper presents the results of tests on the suitability of designed heads (impellers) for aluminum refining. The research was carried out on a physical model of the URO-200, followed by numerical simulations in the FLOW 3D program. Four design variants of impellers were used in the study. The degree of dispersion of the gas phase in the model liquid was used as a criterion for evaluating the performance of each solution using different process parameters, i.e., gas flow rate and impeller speed. Afterward, numerical simulations in Flow 3D software were conducted for the best solution. These simulations confirmed the results obtained with the water model and verified them.

Keywords: aluminum, impeller construction, degassing process, numerical modeling, physical modeling

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1. Introduction

Constantly increasing requirements concerning metallurgical purity in terms of hydrogen content and nonmetallic inclusions make casting manufacturers use effective refining techniques. The answer to this demand is the implementation of the aluminum refining technique making use of a rotor with an original design guaranteeing efficient refining [1,2,3,4]. The main task of the impeller (rotor) is to reduce the contamination of liquid metal (primary and recycled aluminum) with hydrogen and nonmetallic inclusions. An inert gas, mainly argon or a mixture of gases, is introduced through the rotor into the liquid metal to bring both hydrogen and nonmetallic inclusions to the metal surface through the flotation process. Appropriately and uniformly distributed gas bubbles in the liquid metal guarantee achieving the assumed level of contaminant removal economically. A very important factor in deciding about the obtained degassing effect is the optimal rotor design [5,6,7,8]. Thanks to the appropriate geometry of the rotor, gas bubbles introduced into the liquid metal are split into smaller ones, and the spinning movement of the rotor distributes them throughout the volume of the liquid metal bath. In this solution impurities in the liquid metal are removed both in the volume and from the upper surface of the metal. With a well-designed impeller, the costs of refining aluminum and its alloys can be lowered thanks to the reduced inert gas and energy consumption (optimal selection of rotor rotational speed). Shorter processing time and a high degree of dehydrogenation decrease the formation of dross on the metal surface (waste). A bigger produced dross leads to bigger process losses. Consequently, this means that the choice of rotor geometry has an indirect impact on the degree to which the generated waste is reduced [9,10].

Another equally important factor is the selection of process parameters such as gas flow rate and rotor speed [11,12]. A well-designed gas injection system for liquid metal meets two key requirements; it causes rapid mixing of the liquid metal to maintain a uniform temperature throughout the volume and during the entire process, to produce a chemically homogeneous metal composition. This solution ensures effective degassing of the metal bath. Therefore, the shape of the rotor, the arrangement of the nozzles, and their number are significant design parameters that guarantee the optimum course of the refining process. It is equally important to complete the mixing of the metal bath in a relatively short time, as this considerably shortens the refining process and, consequently, reduces the process costs. Another important criterion conditioning the implementation of the developed rotor is the generation of fine diffused gas bubbles which are distributed throughout the metal volume, and whose residence time will be sufficient for the bubbles to collide and adsorb the contaminants. The process of bubble formation by the spinning rotors differs from that in the nozzles or porous molders. In the case of a spinning rotor, the shear force generated by the rotor motion splits the bubbles into smaller ones. Here, the rotational speed, mixing force, surface tension, and fluid density have a key effect on the bubble size. The velocity of the bubbles, which depends mainly on their size and shape, determines their residence time in the reactor and is, therefore, very important for the refining process, especially since gas bubbles in liquid aluminum may remain steady only below a certain size [13,14,15].

The impeller designs presented in the article were developed to improve the efficiency of the process and reduce its costs. The impellers used so far have a complicated structure and are very pricey. The success of the conducted research will allow small companies to become independent of external supplies through the possibility of making simple and effective impellers on their own. The developed structures were tested on the water model. The results of this study can be considered as pilot.

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2. Materials and Methods

Rotors were realized with the SolidWorks computer design technique and a 3D printer. The developed designs were tested on a water model. Afterward, the solution with the most advantageous refining parameters was selected and subjected to calculations with the Flow3D package. As a result, an impeller was designed for aluminum refining. Its principal lies in an even distribution of gas bubbles in the entire volume of liquid metal, with the largest possible participation of the bubble surface, without disturbing the metal surface. This procedure guarantees the removal of gaseous, as well as metallic and nonmetallic, impurities.

2.1. Rotor Designs

The developed impeller constructions, shown in Figure 1Figure 2Figure 3 and Figure 4, were printed on a 3D printer using the PLA (polylactide) material. The impeller design models differ in their shape and the number of holes through which the inert gas flows. Figure 1Figure 2 and Figure 3 show the same impeller model but with a different number of gas outlets. The arrangement of four, eight, and 12 outlet holes was adopted in the developed design. A triangle-shaped structure equipped with three gas outlet holes is presented in Figure 4.

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Figure 1

A 3D modelโ€”impeller with four holesโ€”variant B4.

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Figure 2

A 3D modelโ€”impeller with eight holesโ€”variant B8.

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Figure 3

A 3D modelโ€”impeller with twelve holesโ€”variant B12.

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Figure 4

A 3D modelโ€”โ€˜red triangleโ€™ impeller with three holesโ€”variant RT3.

2.2. Physical Models

Investigations were carried out on a water model of the URO 200 reactor of the barbotage refining process (see Figure 5).

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Figure 5

A schematic of the water model of reactor URO 200.

The URO 200 reactor can be classified as a cyclic reactor. The main element of the device is a rotor, which ends the impeller. The whole system is attached to a shaft via which the refining gas is supplied. Then, the shaft with the rotor is immersed in the liquid metal in the melting pot or the furnace chamber. In URO 200 reactors, the refining process lasts 600 s (10 min), the gas flow rate that can be obtained ranges from 5 to 20 dm3ยทminโˆ’1, and the speed at which the rotor can move is 0 to 400 rpm. The permissible quantity of liquid metal for barbotage refining is 300 kg or 700 kg [8,16,17]. The URO 200 has several design solutions which improve operation and can be adapted to the existing equipment in the foundry. These solutions include the following [8,16]:

  • URO-200XRโ€”used for small crucible furnaces, the capacity of which does not exceed 250 kg, with no control system and no control of the refining process.
  • URO-200SAโ€”used to service several crucible furnaces of capacity from 250 kg to 700 kg, fully automated and equipped with a mechanical rotor lift.
  • URO-200KAโ€”used for refining processes in crucible furnaces and allows refining in a ladle. The process is fully automated, with a hydraulic rotor lift.
  • URO-200KXโ€”a combination of the XR and KA models, designed for the ladle refining process. Additionally, refining in heated crucibles is possible. The unit is equipped with a manual hydraulic rotor lift.
  • URO-200PAโ€”designed to cooperate with induction or crucible furnaces or intermediate chambers, the capacity of which does not exceed one ton. This unit is an integral part of the furnace. The rotor lift is equipped with a screw drive.

Studies making use of a physical model can be associated with the observation of the flow and circulation of gas bubbles. They require meeting several criteria regarding the similarity of the process and the object characteristics. The similarity conditions mainly include geometric, mechanical, chemical, thermal, and kinetic parameters. During simulation of aluminum refining with inert gas, it is necessary to maintain the geometric similarity between the model and the real object, as well as the similarity related to the flow of liquid metal and gas (hydrodynamic similarity). These quantities are characterized by the Reynolds, Weber, and Froude numbers. The Froude number is the most important parameter characterizing the process, its magnitude is the same for the physical model and the real object. Water was used as the medium in the physical modeling. The factors influencing the choice of water are its availability, relatively low cost, and kinematic viscosity at room temperature, which is very close to that of liquid aluminum.

The physical model studies focused on the flow of inert gas in the form of gas bubbles with varying degrees of dispersion, particularly with respect to some flow patterns such as flow in columns and geysers, as well as disturbance of the metal surface. The most important refining parameters are gas flow rate and rotor speed. The barbotage refining studies for the developed impeller (variants B4, B8, B12, and RT3) designs were conducted for the following process parameters:

  • Rotor speed: 200, 300, 400, and 500 rpm,
  • Ideal gas flow: 10, 20, and 30 dm3ยทminโˆ’1,
  • Temperature: 293 K (20 ยฐC).

These studies were aimed at determining the most favorable variants of impellers, which were then verified using the numerical modeling methods in the Flow-3D program.

2.3. Numerical Simulations with Flow-3D Program

Testing different rotor impellers using a physical model allows for observing the phenomena taking place while refining. This is a very important step when testing new design solutions without using expensive industrial trials. Another solution is modeling by means of commercial simulation programs such as ANSYS Fluent or Flow-3D [18,19]. Unlike studies on a physical model, in a computer program, the parameters of the refining process and the object itself, including the impeller design, can be easily modified. The simulations were performed with the Flow-3D program version 12.03.02. A three-dimensional system with the same dimensions as in the physical modeling was used in the calculations. The isothermal flow of liquidโ€“gas bubbles was analyzed. As in the physical model, three speeds were adopted in the numerical tests: 200, 300, and 500 rpm. During the initial phase of the simulations, the velocity field around the rotor generated an appropriate direction of motion for the newly produced bubbles. When the required speed was reached, the generation of randomly distributed bubbles around the rotor was started at a rate of 2000 per second. Table 1 lists the most important simulation parameters.

Table 1

Values of parameters used in the calculations.

ParameterValueUnit
Maximum number of gas particles1,000,000
Rate of particle generation20001ยทsโˆ’1
Specific gas constant287.058Jยทkgโˆ’1ยทKโˆ’1
Atmospheric pressure1.013 ร— 105Pa
Water density1000kgยทmโˆ’3
Water viscosity0.001kgยทmโˆ’1ยทsโˆ’1
Boundary condition on the wallsNo-slip
Size of computational cell0.0034m

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In the case of the CFD analysis, the numerical solutions require great care when generating the computational mesh. Therefore, computational mesh tests were performed prior to the CFD calculations. The effect of mesh density was evaluated by taking into account the velocity of water in the tested object on the measurement line A (height of 0.065 m from the bottom) in a characteristic cross-section passing through the object axis (see Figure 6). The mesh contained 3,207,600, 6,311,981, 7,889,512, 11,569,230, and 14,115,049 cells.

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Figure 6

The velocity of the water depending on the size of the computational grid.

The quality of the generated computational meshes was checked using the criterion skewness angle QEAS [18]. This criterion is described by the following relationship:

QEAS=max{ฮฒmaxโˆ’ฮฒeq180โˆ’ฮฒeq,ฮฒeqโˆ’ฮฒminฮฒeq},

(1)

where ฮฒmaxฮฒmin are the maximal and minimal angles (in degrees) between the edges of the cell, and ฮฒeq is the angle corresponding to an ideal cell, which for cubic cells is 90ยฐ.

Normalized in the interval [0;1], the value of QEAS should not exceed 0.75, which identifies the permissible skewness angle of the generated mesh. For the computed meshes, this value was equal to 0.55โ€“0.65.

Moreover, when generating the computational grids in the studied facility, they were compacted in the areas of the highest gradients of the calculated values, where higher turbulence is to be expected (near the impeller). The obtained results of water velocity in the studied object at constant gas flow rate are shown in Figure 6.

The analysis of the obtained water velocity distributions (see Figure 6) along the line inside the object revealed that, with the density of the grid of nodal points, the velocity changed and its changes for the test cases of 7,889,512, 11,569,230, and 14,115,049 were insignificant. Therefore, it was assumed that a grid containing not less than 7,900,000 (7,889,512) cells would not affect the result of CFD calculations.

A single-block mesh of regular cells with a size of 0.0034 m was used in the numerical calculations. The total number of cells was approximately 7,900,000 (7,889,512). This grid resolution (see Figure 7) allowed the geometry of the system to be properly represented, maintaining acceptable computation time (about 3 days on a workstation with 2ร— CPU and 12 computing cores).

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Figure 7

Structured equidistant mesh used in numerical calculations: (a) mesh with smoothed, surface cells (the so-called FAVOR method) used in Flow-3D; (b) visualization of the applied mesh resolution.

The calculations were conducted with an explicit scheme. The timestep was selected by the program automatically and controlled by stability and convergence. From the moment of the initial velocity field generation (start of particle generation), it was 0.0001 s.

When modeling the degassing process, three fluids are present in the system: water, gas supplied through the rotor head (impeller), and the surrounding air. Modeling such a multiphase flow is a numerically very complex issue. The necessity to overcome the liquid backpressure by the gas flowing out from the impeller leads to the formation of numerical instabilities in the volume of fluid (VOF)-based approach used by Flow-3D software. Therefore, a mixed description of the analyzed flow was used here. In this case, water was treated as a continuous medium, while, in the case of gas bubbles, the discrete phase model (DPM) model was applied. The way in which the air surrounding the system was taken into account is later described in detail.

The following additional assumptions were made in the modeling:

  • โ€”The liquid phase was considered as an incompressible Newtonian fluid.
  • โ€”The effect of chemical reactions during the refining process was neglected.
  • โ€”The composition of each phase (gas and liquid) was considered homogeneous; therefore, the viscosity and surface tension were set as constants.
  • โ€”Only full turbulence existed in the liquid, and the effect of molecular viscosity was neglected.
  • โ€”The gas bubbles were shaped as perfect spheres.
  • โ€”The mutual interaction between gas bubbles (particles) was neglected.

2.3.1. Modeling of Liquid Flow 

The motion of the real fluid (continuous medium) is described by the Navierโ€“Stokes Equation [20].

dudt=โˆ’1ฯโˆ‡p+ฮฝโˆ‡2u+13ฮฝโˆ‡(โˆ‡โ‹… u)+F,

(2)

where du/dt is the time derivative, u is the velocity vector, t is the time, and F is the term accounting for external forces including gravity (unit components denoted by XYZ).

In the simulations, the fluid flow was assumed to be incompressible, in which case the following equation is applicable:

โˆ‚uโˆ‚t+(uโ‹…โˆ‡)u=โˆ’1ฯโˆ‡p+ฮฝโˆ‡2u+F.

(3)

Due to the large range of liquid velocities during flows, the turbulence formation process was included in the modeling. For this purpose, the kโ€“ฮต model turbulence kinetic energy k and turbulence dissipation ฮต were the target parameters, as expressed by the following equations [21]:

โˆ‚(ฯk)โˆ‚t+โˆ‚(ฯkvi)โˆ‚xi=โˆ‚โˆ‚xj[(ฮผ+ฮผtฯƒk)โ‹…โˆ‚kโˆ‚xi]+Gk+Gbโˆ’ฯฮตโˆ’Ym+Sk,

(4)

โˆ‚(ฯฮต)โˆ‚t+โˆ‚(ฯฮตui)โˆ‚xi=โˆ‚โˆ‚xj[(ฮผ+ฮผtฯƒฮต)โ‹…โˆ‚kโˆ‚xi]+C1ฮตฮตk(Gk+G3ฮตGb)+C2ฮตฯฮต2k+Sฮต,

(5)

where ฯ is the gas density, ฯƒฮบ and ฯƒฮต are the Prandtl turbulence numbers, k and ฮต are constants of 1.0 and 1.3, and Gk and Gb are the kinetic energy of turbulence generated by the average velocity and buoyancy, respectively.

As mentioned earlier, there are two gas phases in the considered problem. In addition to the gas bubbles, which are treated here as particles, there is also air, which surrounds the system. The boundary of phase separation is in this case the free surface of the water. The shape of the free surface can change as a result of the forming velocity field in the liquid. Therefore, it is necessary to use an appropriate approach to free surface tracking. The most commonly used concept in liquidโ€“gas flow modeling is the volume of fluid (VOF) method [22,23], and Flow-3D uses a modified version of this method called TrueVOF. It introduces the concept of the volume fraction of the liquid phase fl. This parameter can be used for classifying the cells of a discrete grid into areas filled with liquid phase (fl = 1), gaseous phase, or empty cells (fl = 0) and those through which the phase separation boundary (fl โˆˆ (0, 1)) passes (free surface). To determine the local variations of the liquid phase fraction, it is necessary to solve the following continuity equation:

dfldt=0.

(6)

Then, the fluid parameters in the region of coexistence of the two phases (the so-called interface) depend on the volume fraction of each phase.

ฯ=flฯl+(1โˆ’fl)ฯg,

(7)

ฮฝ=flฮฝl+(1โˆ’fl)ฮฝg,

(8)

where indices l and g refer to the liquid and gaseous phases, respectively.

The parameter of fluid velocity in cells containing both phases is also determined in the same way.

u=flul+(1โˆ’fl)ug.

(9)

Since the processes taking place in the surrounding air can be omitted, to speed up the calculations, a single-phase, free-surface model was used. This means that no calculations were performed in the gas cells (they were treated as empty cells). The liquid could fill them freely, and the air surrounding the system was considered by the atmospheric pressure exerted on the free surface. This approach is often used in modeling foundry and metallurgical processes [24].

2.3.2. Modeling of Gas Bubble Flow 

As stated, a particle model was used to model bubble flow. Spherical particles (gas bubbles) of a given size were randomly generated in the area marked with green in Figure 7b. In the simulations, the gas bubbles were assumed to have diameters of 0.016 and 0.02 m corresponding to the gas flow rates of 10 and 30 dm3ยทminโˆ’1, respectively.

Experimental studies have shown that, as a result of turbulent fluid motion, some of the bubbles may burst, leading to the formation of smaller bubbles, although merging of bubbles into larger groupings may also occur. Therefore, to be able to observe the behavior of bubbles of different sizes (diameter), the calculations generated two additional particle types with diameters twice smaller and twice larger, respectively. The proportion of each species in the system was set to 33.33% (Table 2).

Table 2

Data assumed for calculations.

NoRotor Speed (Rotational Speed)
rpm
Bubbles Diameter
m
Corresponding Gas Flow Rate
dm3ยทminโˆ’1
NoRotor Speed (Rotational Speed)
rpm
Bubbles Diameter
m
Corresponding Gas Flow Rate
dm3ยทminโˆ’1
A2000.01610D2000.0230
0.0080.01
0.0320.04
B3000.01610E3000.0230
0.0080.01
0.0320.04
C5000.01610F5000.0230
0.0080.01
0.0320.04

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The velocity of the particle results from the generated velocity field (calculated from Equation (3) in the liquid ul around it and its velocity resulting from the buoyancy force ub. The effect of particle radius r on the terminal velocity associated with buoyancy force can be determined according to Stokesโ€™ law.

ub=29 (ฯgโˆ’ฯl)ฮผlgr2,

(10)

where g is the acceleration (9.81).

The DPM model was used for modeling the two-phase (waterโ€“air) flow. In this model, the fluid (water) is treated as a continuous phase and described by the Navierโ€“Stokes equation, while gas bubbles are particles flowing in the model fluid (discrete phase). The trajectories of each bubble in the DPM system are calculated at each timestep taking into account the mass forces acting on it. Table 3 characterizes the DPM model used in our own research [18].

Table 3

Characteristic of the DPM model.

MethodEquations
Eulerโ€“LagrangeBalance equation:
dugdt=FD(uโˆ’ug)+g(ฯฑgโˆ’ฯฑ)ฯฑg+F.
FD (u โˆ’ up) denotes the drag forces per mass unit of a bubble, and the expression for the drag coefficient FD is of the form
FD=18ฮผCDReฯฑโ‹…gd2g24.
The relative Reynolds number has the form
Reโ‰กฯdg|ugโˆ’u|ฮผ.
On the other hand, the force resulting from the additional acceleration of the model fluid has the form
F=12dฯdtฯg(uโˆ’ug),
where ug is the gas bubble velocity, u is the liquid velocity, dg is the bubble diameter, and CD is the drag coefficient.

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3. Results and Discussion

3.1. Calculations of Power and Mixing Time by the Flowing Gas Bubbles

One of the most important parameters of refining with a rotor is the mixing power induced by the spinning rotor and the outflowing gas bubbles (via impeller). The mixing power of liquid metal in a ladle of height (h) by gas injection can be determined from the following relation [15]:

pgVm=ฯโ‹…gโ‹…uB,

(11)

where pg is the mixing power, Vm is the volume of liquid metal in the reactor, ฯ is the density of liquid aluminum, and uB is the average speed of bubbles, given below.

uB=nโ‹…Rโ‹…TAcโ‹…Pmโ‹…t,

(12)

where n is the number of gas moles, R is the gas constant (8.314), Ac is the cross-sectional area of the reactor vessel, T is the temperature of liquid aluminum in the reactor, and Pm is the pressure at the middle tank level. The pressure at the middle level of the tank is calculated by a function of the mean logarithmic difference.

Pm=(Pa+ฯโ‹…gโ‹…h)โˆ’Paln(Pa+ฯโ‹…gโ‹…h)Pa,

(13)

where Pa is the atmospheric pressure, and h is the the height of metal in the reactor.

Themelis and Goyal [25] developed a model for calculating mixing power delivered by gas injection.

pg=2Qโ‹…Rโ‹…Tโ‹…ln(1+mโ‹…ฯโ‹…gโ‹…hP),

(14)

where Q is the gas flow, and m is the mass of liquid metal.

Zhang [26] proposed a model taking into account the temperature difference between gas and alloy (metal).

pg=QRTgVm[ln(1+ฯโ‹…gโ‹…hPa)+(1โˆ’TTg)],

(15)

where Tg is the gas temperature at the entry point.

Data for calculating the mixing power resulting from inert gas injection into liquid aluminum are given below in Table 4. The design parameters were adopted for the model, the parameters of which are shown in Figure 5.

Table 4

Data for calculating mixing power introduced by an inert gas.

ParameterValueUnit
Height of metal column0.7m
Density of aluminum2375kgยทmโˆ’3
Process duration20s
Gas temperature at the injection site940K
Cross-sectional area of ladle0.448m2
Mass of liquid aluminum546.25kg
Volume of ladle0.23M3
Temperature of liquid aluminum941.15K

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Table 5 presents the results of mixing power calculations according to the models of Themelis and Goyal and of Zhang for inert gas flows of 10, 20, and 30 dm3ยทminโˆ’1. The obtained calculation results significantly differed from each other. The difference was an order of magnitude, which indicates that the model is highly inaccurate without considering the temperature of the injected gas. Moreover, the calculations apply to the case when the mixing was performed only by the flowing gas bubbles, without using a rotor, which is a great simplification of the phenomenon.

Table 5

Mixing power calculated from mathematical models.

Mathematical ModelMixing Power (Wยทtโˆ’1)
for a Given Inert Gas Flow (dm3ยทminโˆ’1)
102030
Themelis and Goyal11.4923.3335.03
Zhang0.821.662.49

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The mixing time is defined as the time required to achieve 95% complete mixing of liquid metal in the ladle [27,28,29,30]. Table 6 groups together equations for the mixing time according to the models.

Table 6

Models for calculating mixing time.

AuthorsModelRemarks
Szekely [31]ฯ„=800ฮตโˆ’0.4ฮตโ€”Wยทtโˆ’1
Chiti and Paglianti [27]ฯ„=CVQlVโ€”volume of reactor, m3
Qlโ€”flow intensity, m3ยทsโˆ’1
Iguchi and Nakamura [32]ฯ„=1200โ‹…Qโˆ’0.4D1.97hโˆ’1.0ฯ…0.47ฯ…โ€”kinematic viscosity, m2ยทsโˆ’1
Dโ€”diameter of ladle, m
hโ€”height of metal column, m
Qโ€”liquid flow intensity, m3ยทsโˆ’1

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Figure 8 and Figure 9 show the mixing time as a function of gas flow rate for various heights of the liquid column in the ladle and mixing power values.

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Figure 8

Mixing time as a function of gas flow rate for various heights of the metal column (Iguchi and Nakamura model).

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Figure 9

Mixing time as a function of mixing power (Szekly model).

3.2. Determining the Bubble Size

The mechanisms controlling bubble size and mass transfer in an alloy undergoing refining are complex. Strong mixing conditions in the reactor promote impurity mass transfer. In the case of a spinning rotor, the shear force generated by the rotor motion separates the bubbles into smaller bubbles. Rotational speed, mixing force, surface tension, and liquid density have a strong influence on the bubble size. To characterize the kinetic state of the refining process, parameters k and A were introduced. Parameters kA, and uB can be calculated using the below equations [33].

k=2Dโ‹…uBdBโ‹…ฯ€โˆ’โˆ’โˆ’โˆ’โˆ’โˆ’โˆš,

(16)

A=6Qโ‹…hdBโ‹…uB,

(17)

uB=1.02gโ‹…dB,โˆ’โˆ’โˆ’โˆ’โˆ’โˆš

(18)

where D is the diffusion coefficient, and dB is the bubble diameter.

After substituting appropriate values, we get

dB=3.03ร—104(ฯ€D)โˆ’2/5gโˆ’1/5h4/5Q0.344Nโˆ’1.48.

(19)

According to the last equation, the size of the gas bubble decreases with the increasing rotational speed (see Figure 10).

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Figure 10

Effect of rotational speed on the bubble diameter.

In a flow of given turbulence intensity, the diameter of the bubble does not exceed the maximum size dmax, which is inversely proportional to the rate of kinetic energy dissipation in a viscous flow ฮต. The size of the gas bubble diameter as a function of the mixing energy, also considering the Weber number and the mixing energy in the negative power, can be determined from the following equations [31,34]:

  • โ€”Sevik and Park:

dBmax=We0.6krโ‹…(ฯƒโ‹…103ฯโ‹…10โˆ’3)0.6โ‹…(10โ‹…ฮต)โˆ’0.4โ‹…10โˆ’2.

(20)

  • โ€”Evans:

dBmax=โŽกโŽฃWekrโ‹…ฯƒโ‹…1032โ‹…(ฯโ‹…10โˆ’3)13โŽคโŽฆ35 โ‹…(10โ‹…ฮต)โˆ’25โ‹…10โˆ’2.

(21)

The results of calculating the maximum diameter of the bubble dBmax determined from Equation (21) are given in Table 7.

Table 7

The results of calculating the maximum diameter of the bubble using Equation (21).

ModelMixing Energy
ฤบ (m2ยทsโˆ’3)
Weber Number (Wekr)
0.591.01.2
Zhang and Taniguchi
dmax
0.10.01670.02300.026
0.50.00880.01210.013
1.00.00670.00910.010
1.50.00570.00780.009
Sevik and Park
dBmax
0.10.2650.360.41
0.50.1390.190.21
1.00.1060.140.16
1.50.0900.120.14
Evans
dBmax
0.10.2470.3400.38
0.50.1300.1780.20
1.00.0980.1350.15
1.50.0840.1150.13

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3.3. Physical Modeling

The first stage of experiments (using the URO-200 water model) included conducting experiments with impellers equipped with four, eight, and 12 gas outlets (variants B4, B8, B12). The tests were carried out for different process parameters. Selected results for these experiments are presented in Figure 11Figure 12Figure 13 and Figure 14.

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Figure 11

Impeller variant B4โ€”gas bubbles dispersion registered for a gas flow rate of 10 dm3ยทminโˆ’1 and rotor speed of (a) 200, (b) 300, (c) 400, and (d) 500 rpm.

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Figure 12

Impeller variant B8โ€”gas bubbles dispersion registered for a gas flow rate of 10 dm3ยทminโˆ’1 and rotor speed of (a) 200, (b) 300, (c) 400, and (d) 500 rpm.

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Figure 13

Gas bubble dispersion registered for different processing parameters (impeller variant B12).

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Figure 14

Gas bubble dispersion registered for different processing parameters (impeller variant RT3).

The analysis of the refining variants presented in Figure 11Figure 12Figure 13 and Figure 14 reveals that the proposed impellers design model is not useful for the aluminum refining process. The number of gas outlet orifices, rotational speed, and flow did not affect the refining efficiency. In all the variants shown in the figures, very poor dispersion of gas bubbles was observed in the object. The gas bubble flow had a columnar character, and so-called dead zones, i.e., areas where no inert gas bubbles are present, were visible in the analyzed object. Such dead zones were located in the bottom and side zones of the ladle, while the flow of bubbles occurred near the turning rotor. Another negative phenomenon observed was a significant agitation of the water surface due to excessive (rotational) rotor speed and gas flow (see Figure 13, cases 20; 400, 30; 300, 30; 400, and 30; 500).

Research results for a โ€˜red triangleโ€™ impeller equipped with three gas supply orifices (variant RT3) are presented in Figure 14.

In this impeller design, a uniform degree of bubble dispersion in the entire volume of the modeling fluid was achieved for most cases presented (see Figure 14). In all tested variants, single bubbles were observed in the area of the water surface in the vessel. For variants 20; 200, 30; 200, and 20; 300 shown in Figure 14, the bubble dispersion results were the worst as the so-called dead zones were identified in the area near the bottom and sidewalls of the vessel, which disqualifies these work parameters for further applications. Interestingly, areas where swirls and gas bubble chains formed were identified only for the inert gas flows of 20 and 30 dm3ยทminโˆ’1 and 200 rpm in the analyzed model. This means that the presented model had the best performance in terms of dispersion of gas bubbles in the model liquid. Its design with sharp edges also differed from previously analyzed models, which is beneficial for gas bubble dispersion, but may interfere with its suitability in industrial conditions due to possible premature wear.

3.4. Qualitative Comparison of Research Results (CFD and Physical Model)

The analysis (physical modeling) revealed that the best mixing efficiency results were obtained with the RT3 impeller variant. Therefore, numerical calculations were carried out for the impeller model with three outlet orifices (variant RT3). The CFD results are presented in Figure 15 and Figure 16.

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Figure 15

Simulation results of the impeller RT3, for given flows and rotational speeds after a time of 1 s: simulation variants (a) A, (b) B, (c) C, (d) D, (e) E, and (f) F.

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Figure 16

Simulation results of the impeller RT3, for given flows and rotational speeds after a time of 5.4 s.: simulation variants (a) A, (b) B, (c) C, (d) D, (e) E, and (f) F.

CFD results are presented for all analyzed variants (impeller RT3) at two selected calculation timesteps of 1 and 5.40 s. They show the velocity field of the medium (water) and the dispersion of gas bubbles.

Figure 15 shows the initial refining phase after 1 s of the process. In this case, the gas bubble formation and flow were observed in an area close to contact with the rotor. Figure 16 shows the phase when the dispersion and flow of gas bubbles were advanced in the reactor area of the URO-200 model.

The quantitative evaluation of the obtained results of physical and numerical model tests was based on the comparison of the degree of gas dispersion in the model liquid. The degree of gas bubble dispersion in the volume of the model liquid and the areas of strong turbulent zones formation were evaluated during the analysis of the results of visualization and numerical simulations. These two effects sufficiently characterize the required course of the process from the physical point of view. The known scheme of the below description was adopted as a basic criterion for the evaluation of the degree of dispersion of gas bubbles in the model liquid.

  • Minimal dispersionโ€”single bubbles ascending in the region of their formation along the ladle axis; lack of mixing in the whole bath volume.
  • Accurate dispersionโ€”single and well-mixed bubbles ascending toward the bath mirror in the region of the ladle axis; no dispersion near the walls and in the lower part of the ladle.
  • Uniform dispersionโ€”most desirable; very good mixing of fine bubbles with model liquid.
  • Excessive dispersionโ€”bubbles join together to form chains; large turbulence zones; uneven flow of gas.

The numerical simulation results give a good agreement with the experiments performed with the physical model. For all studied variants (used process parameters), the single bubbles were observed in the area of water surface in the vessel. For variants presented in Figure 13 (200 rpm, gas flow 20 and dm3ยทminโˆ’1) and relevant examples in numerical simulation Figure 16, the worst bubble dispersion results were obtained because the dead zones were identified in the area near the bottom and sidewalls of the vessel, which disqualifies these work parameters for further use. The areas where swirls and gas bubble chains formed were identified only for the inert gas flows of 20 and 30 dm3ยทminโˆ’1 and 200 rpm in the analyzed model (physical model). This means that the presented impeller model had the best performance in terms of dispersion of gas bubbles in the model liquid. The worst bubble dispersion results were obtained because the dead zones were identified in the area near the bottom and side walls of the vessel, which disqualifies these work parameters for further use.

Figure 17 presents exemplary results of model tests (CFD and physical model) with marked gas bubble dispersion zones. All variants of tests were analogously compared, and this comparison allowed validating the numerical model.

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Figure 17

Compilations of model research results (CFD and physical): Aโ€”single gas bubbles formed on the surface of the modeling liquid, Bโ€”excessive formation of gas chains and swirls, Cโ€”uniform distribution of gas bubbles in the entire volume of the tank, and Dโ€”dead zones without gas bubbles, no dispersion. (a) Variant B; (b) variant F.

It should be mentioned here that, in numerical simulations, it is necessary to make certain assumptions and simplifications. The calculations assumed three particle size classes (Table 2), which represent the different gas bubbles that form due to different gas flow rates. The maximum number of particles/bubbles (Table 1) generated was assumed in advance and related to the computational capabilities of the computer. Too many particles can also make it difficult to visualize and analyze the results. The size of the particles, of course, affects their behavior during simulation, while, in the figures provided in the article, the bubbles are represented by spheres (visualization of the results) of the same size. Please note that, due to the adopted Lagrangianโ€“Eulerian approach, the simulation did not take into account phenomena such as bubble collapse or fusion. However, the obtained results allow a comprehensive analysis of the behavior of gas bubbles in the system under consideration.

The comparative analysis of the visualization (quantitative) results obtained with the water model and CFD simulations (see Figure 17) generated a sufficient agreement from the point of view of the trends. A precise quantitative evaluation is difficult to perform because of the lack of a refraction compensating system in the water model. Furthermore, in numerical simulations, it is not possible to determine the geometry of the forming gas bubbles and their interaction with each other as opposed to the visualization in the water model. The use of both research methods is complementary. Thus, a direct comparison of images obtained by the two methods requires appropriate interpretation. However, such an assessment gives the possibility to qualitatively determine the types of the present gas bubble dispersion, thus ultimately validating the CFD results with the water model.

A summary of the visualization results for impellers RT3, i.e., analysis of the occurring gas bubble dispersion types, is presented in Table 8.

Table 8

Summary of visualization results (impeller RT3)โ€”different types of gas bubble dispersion.

No Exp.ABCDEF
Gas flow rate, dm3ยทminโˆ’11030
Impeller speed, rpm200300500200300500
Type of dispersionAccurateUniformUniform/excessiveMinimalExcessiveExcessive

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Tests carried out for impeller RT3 confirmed the high efficiency of gas bubble distribution in the volume of the tested object at a low inert gas flow rate of 10 dm3ยทminโˆ’1. The most optimal variant was variant B (300 rpm, 10 dm3ยทminโˆ’1). However, the other variants A and C (gas flow rate 10 dm3ยทminโˆ’1) seemed to be favorable for this type of impeller and are recommended for further testing. The above process parameters will be analyzed in detail in a quantitative analysis to be performed on the basis of the obtained efficiency curves of the degassing process (oxygen removal). This analysis will give an unambiguous answer as to which process parameters are the most optimal for this type of impeller; the results are planned for publication in the next article.

It should also be noted here that the high agreement between the results of numerical calculations and physical modelling prompts a conclusion that the proposed approach to the simulation of a degassing process which consists of a single-phase flow model with a free surface and a particle flow model is appropriate. The simulation results enable us to understand how the velocity field in the fluid is formed and to analyze the distribution of gas bubbles in the system. The simulations in Flow-3D software can, therefore, be useful for both the design of the impeller geometry and the selection of process parameters.

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4. Conclusions

The results of experiments carried out on the physical model of the device for the simulation of barbotage refining of aluminum revealed that the worst results in terms of distribution and dispersion of gas bubbles in the studied object were obtained for the black impellers variants B4, B8, and B12 (multi-orifice impellersโ€”four, eight, and 12 outlet holes, respectively).

In this case, the control of flow, speed, and number of gas exit orifices did not improve the process efficiency, and the developed design did not meet the criteria for industrial tests. In the case of the โ€˜red triangleโ€™ impeller (variant RT3), uniform gas bubble dispersion was achieved throughout the volume of the modeling fluid for most of the tested variants. The worst bubble dispersion results due to the occurrence of the so-called dead zones in the area near the bottom and sidewalls of the vessel were obtained for the flow variants of 20 dm3ยทminโˆ’1 and 200 rpm and 30 dm3ยทminโˆ’1 and 200 rpm. For the analyzed model, areas where swirls and gas bubble chains were formed were found only for the inert gas flow of 20 and 30 dm3ยทminโˆ’1 and 200 rpm. The model impeller (variant RT3) had the best performance compared to the previously presented impellers in terms of dispersion of gas bubbles in the model liquid. Moreover, its design differed from previously presented models because of its sharp edges. This can be advantageous for gas bubble dispersion, but may negatively affect its suitability in industrial conditions due to premature wearing.

The CFD simulation results confirmed the results obtained from the experiments performed on the physical model. The numerical simulation of the operation of the โ€˜red triangleโ€™ impeller model (using Flow-3D software) gave good agreement with the experiments performed on the physical model. This means that the presented model impeller, as compared to other (analyzed) designs, had the best performance in terms of gas bubble dispersion in the model liquid.

In further work, the developed numerical model is planned to be used for CFD simulations of the gas bubble distribution process taking into account physicochemical parameters of liquid aluminum based on industrial tests. Consequently, the obtained results may be implemented in production practice.

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Funding Statement

This paper was created with the financial support grants from the AGH-UST, Faculty of Foundry Engineering, Poland (16.16.170.654 and 11/990/BK_22/0083) for the Faculty of Materials Engineering, Silesian University of Technology, Poland.

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Author Contributions

Conceptualization, K.K. and D.K.; methodology, J.P. and T.M.; validation, M.S. and S.G.; formal analysis, D.K. and T.M.; investigation, J.P., K.K. and S.G.; resources, M.S., J.P. and K.K.; writingโ€”original draft preparation, D.K. and T.M.; writingโ€”review and editing, D.K. and T.M.; visualization, J.P., K.K. and S.G.; supervision, D.K.; funding acquisition, D.K. and T.M. All authors have read and agreed to the published version of the manuscript.

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Institutional Review Board Statement

Not applicable.

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Informed Consent Statement

Not applicable.

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Data Availability Statement

Data are contained within the article.

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Conflicts of Interest

The authors declare no conflict of interest.

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Footnotes

Publisherโ€™s Note: MDPI stays neutral with regard to jurisdictional claims in published maps and institutional affiliations.

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Figure 1.| Physical models of the vertical drop, backdrop and stepped drop developed in the Technical University of Lisbon.

Numerical modelling of air-water flows in sewer drops

ํ•˜์ˆ˜๊ตฌ ๋ฐฉ์šธ์˜ ๊ณต๊ธฐ-๋ฌผ ํ๋ฆ„ ์ˆ˜์น˜ ๋ชจ๋ธ๋ง

Paula Beceiro (corresponding author)
Maria do Cรฉu Almeida
Hydraulic and Environment Department (DHA), National Laboratory for Civil Engineering, Avenida do Brasil 101, 1700-066 Lisbon, Portugal
E-mail: pbeceiro@lnec.pt
Jorge Matos
Department of Civil Engineering, Arquitecture and Geosources,
Technical University of Lisbon (IST), Avenida Rovisco Pais 1, 1049-001 Lisbon, Portugal

ABSTRACT

๋ฌผ ํ๋ฆ„์— ์šฉ์กด ์‚ฐ์†Œ(DO)์˜ ์กด์žฌ๋Š” ํ•ด๋กœ์šด ์˜ํ–ฅ์˜ ๋ฐœ์ƒ์„ ๋ฐฉ์ง€ํ•˜๋Š” ๋ฐ ์œ ์ตํ•œ ๊ฒƒ์œผ๋กœ ์ธ์‹๋˜๋Š” ํ˜ธ๊ธฐ์„ฑ ์กฐ๊ฑด์„ ๋ณด์žฅํ•˜๋Š” ์ค‘์š”ํ•œ ์š”์†Œ์ž…๋‹ˆ๋‹ค.

ํ•˜์ˆ˜๋„ ์‹œ์Šคํ…œ์—์„œ ํ๋ฅด๋Š” ํ์ˆ˜์— DO๋ฅผ ํ†ตํ•ฉํ•˜๋Š” ๊ฒƒ์€ ๊ณต๊ธฐ-์•ก์ฒด ๊ฒฝ๊ณ„๋ฉด ๋˜๋Š” ๋ฐฉ์šธ์ด๋‚˜ ์ ‘ํ•ฉ๋ถ€์™€ ๊ฐ™์€ ํŠน์ด์ ์˜ ์กด์žฌ๋กœ ์ธํ•ด ํ˜ผ์ž…๋œ ๊ณต๊ธฐ๋ฅผ ํ†ตํ•œ ์—ฐ์† ์žฌ๋ฐฉ์ถœ์˜ ์˜ํ–ฅ์„ ์ •๋Ÿ‰ํ™”ํ•˜๊ธฐ ์œ„ํ•ด ๊ด‘๋ฒ”์œ„ํ•˜๊ฒŒ ์กฐ์‚ฌ๋œ ํ”„๋กœ์„ธ์Šค์ž…๋‹ˆ๋‹ค. ๊ณต๊ธฐ ํ˜ผ์ž… ๋ฐ ํ›„์† ํ™˜๊ธฐ๋ฅผ ํ–ฅ์ƒ์‹œํ‚ค๊ธฐ ์œ„ํ•œ ํ•˜์ˆ˜๊ตฌ ๋“œ๋กญ์˜ ์œ„์น˜๋Š” ํ•˜์ˆ˜๊ตฌ์˜ ํ˜ธ๊ธฐ์„ฑ ์กฐ๊ฑด์„ ์ด‰์ง„ํ•˜๋Š” ํšจ๊ณผ์ ์ธ ๋ฐฉ๋ฒ•์ž…๋‹ˆ๋‹ค.

๋ณธ ๋…ผ๋ฌธ์—์„œ๋Š” ์ˆ˜์ง ๋‚™ํ•˜, ๋ฐฐ๊ฒฝ ๋ฐ ๊ณ„๋‹จ์‹ ๋‚™ํ•˜๋ฅผ CFD(์ „์‚ฐ์œ ์ฒด์—ญํ•™) ์ฝ”๋“œ FLOW-3Dยฎ๋ฅผ ์‚ฌ์šฉํ•˜์—ฌ ๋ชจ๋ธ๋งํ•˜์—ฌ ์ด๋Ÿฌํ•œ ์œ ํ˜•์˜ ๊ตฌ์กฐ๋ฌผ์˜ ์กด์žฌ๋กœ ์ธํ•ด ๋ฐœ์ƒํ•˜๋Š” ๋‚œ๋ฅ˜๋กœ ์ธํ•œ ๊ณต๊ธฐ-๋ฌผ ํ๋ฆ„์„ ํ‰๊ฐ€ํ–ˆ์Šต๋‹ˆ๋‹ค. ์ด์šฉ ๊ฐ€๋Šฅํ•œ ์‹คํ—˜์  ์—ฐ๊ตฌ์— ๊ธฐ์ดˆํ•œ ์ˆ˜๋ ฅํ•™์  ๋ณ€์ˆ˜์˜ ํ‰๊ฐ€์™€ ๊ณต๊ธฐ ํ˜ผ์ž…์˜ ๋ถ„์„์ด ์ˆ˜ํ–‰๋˜์—ˆ์Šต๋‹ˆ๋‹ค.

์ด๋Ÿฌํ•œ ๊ตฌ์กฐ๋ฌผ์— ๋Œ€ํ•œ CFD ๋ชจ๋ธ์˜ ๊ฒฐ๊ณผ๋Š” Soares(2003), Afonso(2004) ๋ฐ Azevedo(2006)๊ฐ€ ๊ฐœ๋ฐœํ•œ ํ•ด๋‹น ๋ฌผ๋ฆฌ์  ๋ชจ๋ธ์—์„œ ์–ป์€ ๋ฐฉ๋ฅ˜, ์••๋ ฅ ํ—ค๋“œ ๋ฐ ์ˆ˜์‹ฌ์˜ ์ธก์ •์„ ์‚ฌ์šฉํ•˜์—ฌ ๊ฒ€์ฆ๋˜์—ˆ์Šต๋‹ˆ๋‹ค.

์œ ์•• ๊ฑฐ๋™์— ๋Œ€ํ•ด ๋งค์šฐ ์ž˜ ๋งž์•˜์Šต๋‹ˆ๋‹ค. ์ˆ˜์น˜ ๋ชจ๋ธ์„ ๊ฒ€์ฆํ•œ ํ›„ ๊ณต๊ธฐ ์—ฐํ–‰ ๋ถ„์„์„ ์ˆ˜ํ–‰ํ–ˆ์Šต๋‹ˆ๋‹ค.

The presence of dissolved oxygen (DO) in water flows is an important factor to ensure the aerobic conditions recognised as beneficial to prevent the occurrence of detrimental effects. The incorporation of DO in wastewater flowing in sewer systems is a process widely investigated in order to quantify the effect of continuous reaeration through the air-liquid interface or air entrained due the presence of singularities such as drops or junctions. The location of sewer drops to enhance air entrainment and subsequently reaeration is an effective practice to promote aerobic conditions in sewers. In the present paper, vertical drops, backdrops and stepped drop was modelled using the computational fluid dynamics (CFD) code FLOW-3Dยฎ to evaluate the air-water flows due to the turbulence induced by the presence of this type of structures. The assessment of the hydraulic variables and an analysis of the air entrainment based in the available experimental studies were carried out. The results of the CFD models for these structures were validated using measurements of discharge, pressure head and water depth obtained in the corresponding physical models developed by Soares (2003), Afonso (2004) and Azevedo (2006). A very good fit was obtained for the hydraulic behaviour. After validation of numerical models, analysis of the air entrainment was carried out.

Key words | air entrainment, computational fluid dynamics (CFD), sewer drops

Figure 1.| Physical models of the vertical drop, backdrop and stepped drop developed in the Technical University of Lisbon.
Figure 1.| Physical models of the vertical drop, backdrop and stepped drop developed in the Technical University of Lisbon.
Figure 3. Comparison between the experimental and numerical pressure head along of the invert of the outlet pipe.
Figure 3. Comparison between the experimental and numerical pressure head along of the invert of the outlet pipe.
Figure 4. Average void fraction along the longitudinal axis of the outlet pipe for the lower discharges in the vertical drop and backdrop.
Figure 4. Average void fraction along the longitudinal axis of the outlet pipe for the lower discharges in the vertical drop and backdrop.

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Fig. 6 LH2 isotherms at 1020 s.

์•ก์ฒด-์ˆ˜์†Œ ํƒฑํฌ๋ฅผ ์œ„ํ•œ ๊ฒฐํ•ฉ๋œ ์—ด์—ญํ•™-์œ ์ฒด-์—ญํ•™ ์†”๋ฃจ์…˜

Coupled thermodynamic-fluid-dynamic solution for a liquid-hydrogen tank

G. D. Grayson

Published Online:23 May 2012 https://doi.org/10.2514/3.26706

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Introduction

ROPELLANT ์—ด ์„ฑ์ธตํ™” ๋ฐ ์™ธ๋ถ€ ๊ต๋ž€์— ๋Œ€ํ•œ ์œ ์ฒด ์—ญํ•™์  ๋ฐ˜์‘์€ ๋ฐœ์‚ฌ์ฒด์™€ ์šฐ์ฃผ์„  ๋ชจ๋‘์—์„œ ์ค‘์š”ํ•ฉ๋‹ˆ๋‹ค. ๊ณผ๊ฑฐ์—๋Š” ๊ฒฐํ•ฉ๋œ ์†”๋ฃจ์…˜์„ ์ œ๊ณตํ•  ์ˆ˜ ์žˆ๋Š” ์ถฉ๋ถ„ํ•œ ๊ณ„์‚ฐ ๊ธฐ์ˆ ์ด ๋ถ€์กฑํ•˜์—ฌ ์ด๋Ÿฌํ•œ ๋ฌธ์ œ๋ฅผ ๊ฐœ๋ณ„์ ์œผ๋กœ ํ•ด๊ฒฐํ–ˆ์Šต๋‹ˆ๋‹ค.1

์ด๋กœ ์ธํ•ด ๋ชจ๋ธ๋ง ๊ธฐ์ˆ ์˜ ๋ถˆํ™•์‹ค์„ฑ์„ ํ—ˆ์šฉํ•˜๊ธฐ ์œ„ํ•ด ํฐ ์•ˆ์ „ ๊ณ„์ˆ˜๋ฅผ ๊ฐ€์ง„ ์‹œ์Šคํ…œ์ด ๊ณผ๋„ํ•˜๊ฒŒ ์„ค๊ณ„๋˜์—ˆ์Šต๋‹ˆ๋‹ค. ๊ณ ์ค‘๋ ฅ ํ™˜๊ฒฝ๊ณผ ์ €์ค‘๋ ฅ ํ™˜๊ฒฝ ๋ชจ๋‘์—์„œ ์ž‘๋™ํ•˜๋„๋ก ์„ค๊ณ„๋œ ๋ฏธ๋ž˜ ์‹œ์Šคํ…œ์€ ๊ธฐ์ˆ ์ ์œผ๋กœ๋‚˜ ์žฌ์ •์ ์œผ๋กœ ์‹คํ˜„ ๊ฐ€๋Šฅํ•˜๋„๋ก ๊ณผ์ž‰ ์„ค๊ณ„ ๋ฐ ์•ˆ์ „ ์š”์†Œ๊ฐ€ ๋œ ํ•„์š”ํ•ฉ๋‹ˆ๋‹ค.

์ด๋Ÿฌํ•œ ์œ ์ฒด ์‹œ์Šคํ…œ์€ ์—ด์—ญํ•™ ๋ฐ ์œ ์ฒด ์—ญํ•™์ด ๋ชจ๋‘ ์ค‘์š”ํ•œ ํ™˜๊ฒฝ์—์„œ ๋ชจ๋ธ์˜ ๊ธฐ๋Šฅ์„ ๊ด‘๋ฒ”์œ„ํ•˜๊ฒŒ ๊ฒ€์ฆํ•œ ํ›„์—๋งŒ ๊ณ ์ถฉ์‹ค๋„ ์ˆ˜์น˜ ๋ชจ๋ธ์„ ๊ธฐ๋ฐ˜์œผ๋กœ ํ•  ์ˆ˜ ์žˆ์Šต๋‹ˆ๋‹ค. ์ƒ์šฉ ์ปดํ“จํ„ฐ ์ฝ”๋“œ FLOW-3D2๋Š” ์œ ์ฒด ์—ญํ•™ ๋ฐ ์—ด ๋ชจ๋ธ๋ง ๋ชจ๋‘์—์„œ ๊ฐ€๋Šฅ์„ฑ์„ ๋ณด์—ฌ์ฃผ์—ˆ์œผ๋ฉฐ,1 ๋”ฐ๋ผ์„œ ์—ด์—ญํ•™-์œ ์ฒด-์—ญํ•™ ์—”์ง€๋‹ˆ์–ด๋ง ๋ฌธ์ œ์—์„œ ๊ฒฐํ•ฉ๋œ ์งˆ๋Ÿ‰, ์šด๋™๋Ÿ‰ ๋ฐ ์—๋„ˆ์ง€ ๋ฐฉ์ •์‹์„ ํ‘ธ๋Š” ๋ฐ ์ ํ•ฉํ•จ์„ ์‹œ์‚ฌํ•ฉ๋‹ˆ๋‹ค.

๋ฐœ์‚ฌ์ฒด์˜ ๋ณต์žกํ•œ ์•ก์ฒด ๊ฐ€์Šค ์‹œ์Šคํ…œ์— ๋Œ€ํ•œ ํฌ๊ด„์ ์ธ ์†”๋ฃจ์…˜์„ ๋‹ฌ์„ฑํ•˜๊ธฐ ์œ„ํ•œ ์ฒซ ๋ฒˆ์งธ ๋‹จ๊ณ„๋กœ ์•ก์ฒด ์œ ์ฒด ์—ญํ•™๊ณผ ์—ด์—ญํ•™์„ ํ†ตํ•ฉํ•˜๋Š” ์ œ์•ˆ๋œ ์ƒ๋‹จ ๋‹จ๊ณ„ ์•ก์ฒด-์ˆ˜์†Œ(Lit) ํƒฑํฌ์˜ ๊ฐ„๋‹จํ•œ ๋ชจ๋ธ์ด ์—ฌ๊ธฐ์— ์ œ์‹œ๋ฉ๋‹ˆ๋‹ค. FLOW-3D FLOW-3D ํ”„๋กœ๊ทธ๋žจ์€ Los Alamos Scientific Laboratory์—์„œ ์‹œ์ž‘๋˜์—ˆ์œผ๋ฉฐ ๋งˆ์ปค ๋ฐ ์…€ ๋ฐฉ๋ฒ•์—์„œ ํŒŒ์ƒ๋œ ๊ฒƒ์ž…๋‹ˆ๋‹ค.3 ํ˜„์žฌ ์ƒํƒœ๋กœ ๊ฐ€์ ธ์˜ค๊ธฐ ์œ„ํ•ด ์ˆ˜๋…„์— ๊ฑธ์ณ ๊ด‘๋ฒ”์œ„ํ•œ ์ฝ”๋“œ ์ˆ˜์ •์ด ์ด๋ฃจ์–ด์กŒ์Šต๋‹ˆ๋‹ค.2

ํ”„๋กœ๊ทธ๋žจ์€ ๋‹ค์Œ๊ณผ ๊ฐ™์Šต๋‹ˆ๋‹ค. ์ผ๋ฐ˜ Navier-Stokes ๋ฐฉ์ •์‹์„ ํ’€๊ธฐ ์œ„ํ•ด ์ˆ˜์น˜ ๊ทผ์‚ฌ์˜ ์ค‘์•™ ์œ ํ•œ ์ฐจ๋ถ„ ๋ฐฉ๋ฒ•์„ ์‚ฌ์šฉํ•˜๋Š” 3์ฐจ์› ์œ ์ฒด ์—ญํ•™ ์†”๋ฒ„์ž…๋‹ˆ๋‹ค. ๋ชจ๋ฉ˜ํ…€ ๋ฐ ์—๋„ˆ์ง€ ๋ฐฉ์ •์‹์˜ ์„น์…˜์€ ํŠน์ • ์‘์šฉ ํ”„๋กœ๊ทธ๋žจ์— ๋”ฐ๋ผ ํ™œ์„ฑํ™” ๋˜๋Š” ๋น„ํ™œ์„ฑํ™”ํ•  ์ˆ˜ ์žˆ์Šต๋‹ˆ๋‹ค.

์ฝ”๋“œ๋Š” 1994๋…„ 9์›” 13์ผ ์ ‘์ˆ˜๋ฅผ ์ธ์šฉํ•˜๊ธฐ ์œ„ํ•ด ๋ฌด์•ก์ฒด ํ‘œ๋ฉด, ๋ณต์žกํ•œ ์šฉ๊ธฐ ๊ธฐํ•˜ํ•™, ์—ฌ๋Ÿฌ ์ ์„ฑ ๋ชจ๋ธ, ํ‘œ๋ฉด ์žฅ๋ ฅ, ๋‹ค๊ณต์„ฑ ๋งค์ฒด๋ฅผ ํ†ตํ•œ ํ๋ฆ„ ๋ฐ ์‘๊ณ ์™€ ํ•จ๊ป˜ ์••์ถ•์„ฑ ๋˜๋Š” ๋น„์••์ถ•์„ฑ ์œ ๋™ ๊ฐ€์ •์„ ์ œ๊ณตํ•ฉ๋‹ˆ๋‹ค. 1995๋…„ 1์›” 15์ผ์— ๋ฐ›์€ ๊ฐœ์ •; 1995๋…„ 2์›” 17์ผ ์ถœํŒ ์Šน์ธ.

ROPELLANT thermal stratification and fluid-dynamic response to external disturbances are of concern in both launch vehicles and spacecraft. In the past these problems have been addressed separately for want of sufficient computational technology to provide for coupled solutions.1 This has resulted in overdesigned systems with large safety factors to allow for the uncertainty in modeling techniques. Future systems designed to perform in both highand low-gravity environments will require less overdesign and safety factors to be technically and financially feasible. Such fluid systems can be based on high-fidelity numerical models only after extensive validation of the models’ capabilities in environments where both the thermodynamics and the fluid dynamics are important. The commercial computer code FLOW-3D2 has shown promise in both fluid-dynamic and thermal modeling,1 thus suggesting suitability for solving the coupled mass, momentum, and energy equations in thermodynamic-fluid-dynamic engineering problems. As a first step to achieving a comprehensive solution for complex liquidgas systems in a launch vehicle, a simple model of a proposed upper-stage liquid-hydrogen (Lit) tank incorporating the liquid fluid dynamics and thermodynamics is presented here. FLOW-3D The FLOW-3D program originated at the Los Alamos Scientific Laboratory and is a derivative of the marker-and-cell method.3 Extensive code modifications have been made over the years to bring it to its present state.2 The program is a three-dimensional fluiddynamic solver that uses a central finite-difference method of numerical approximation to solve the general Navier-Stokes equations. Sections of the momentum and energy equations can be enabled or disabled depending on the particular application. The code provides compressible or incompressible flow assumptions with liquid free surfaces, complex container geometries, several viscosity models, surface tension, flow though porous media, and solidification, to cite Received Sept. 13, 1994; revision received Jan. 15, 1995; accepted for publication Feb. 17, 1995. Copyright ยฉ 1995 by the American Institute of Aeronautics and Astronautics, Inc. All rights reserved. *Engineer/Scientist, Propulsion Analysis and Hydraulics, Space Transportation Division, MS 13-3, 5301 Bolsa Avenue. Member AIAA. a few of the possibilities. Further information on FLOW-3D’s capabilities and details of the numerical algorithms can be found in Ref. 2

Fig. 1 Axial-acceleration history.
Fig. 1 Axial-acceleration history.
Fig. 2 Heat flux histories.
Fig. 2 Heat flux histories.
Fig. 3 LHi isotherms at 50 s.
Fig. 3 LHi isotherms at 50 s.
Fig. 4 LH2 isotherms at 300 s
Fig. 4 LH2 isotherms at 300 s
Fig. 5 LH2 isotherms at 880 s.
Fig. 5 LH2 isotherms at 880 s.
Fig. 6 LH2 isotherms at 1020 s.
Fig. 6 LH2 isotherms at 1020 s.
Fig. 7 Tank-outlet temperature history.
Fig. 7 Tank-outlet temperature history.
Figura 7. Influencia del modelo de turbulencia. Qmodelo=27.95l/s.

Flow-3D๋ฅผ ์‚ฌ์šฉํ•˜์—ฌ ์ „์‚ฐ์œ ์ฒด์—ญํ•™(CFD)์„ ์ ์šฉํ•œ ๋น ๋ฅธ ๋‹จ๊ณ„์˜ ํ”Œ๋Ÿฌ์‹œ ์œ ๋™ ์ˆ˜์น˜ ๋ชจ๋ธ๋ง

Numerical Modeling of Flush Flow in a Rapid Step Applying Computational Fluid Dynamics (CFD) Using Flow-3D.

๋ ˆ๋ธŒ ํด๋ฆฌํ….ย (Quito)ย [์˜จ๋ผ์ธ].ย 2018, vol.41, n.2, pp.53-64.ย ISSN 2477-8990.

์ด ํ”„๋กœ์ ํŠธ์˜ ์ฃผ์š” ๋ชฉํ‘œ๋Š” FLOW-3D๋ฅผ ์‚ฌ์šฉํ•˜์—ฌ ๊ณ„๋‹จ์‹ ์—ฌ์ˆ˜๋กœ์—์„œ ์Šคํ‚ค๋ฐ ํ๋ฆ„์˜ ์ˆ˜์น˜ ๋ชจ๋ธ๋ง์„ ๊ฐœ๋ฐœํ•˜๋Š” ๊ฒƒ์ž…๋‹ˆ๋‹ค.ย ์ด๋Ÿฌํ•œ ๊ตฌ์กฐ์˜ ์„ค๊ณ„๋Š” ๋ฌผ๋ฆฌ์  ๋ชจ๋ธ๋ง์—์„œ ์–ป์€ ๊ฒฝํ—˜์  ํ‘œํ˜„๊ณผ CFD ์ฝ”๋“œ๋ฅผ ์ง€์›ํ•˜๋Š” ๊ณ„๋‹จ์‹ ์—ฌ์ˆ˜๋กœ๋ฅผ ํ†ตํ•œ ํ๋ฆ„์˜ ์ˆ˜์น˜ ๋ชจ๋ธ๋ง์—์„œ ๋ณด์™„ ์—ฐ๊ตฌ๋ฅผ ๊ธฐ๋ฐ˜์œผ๋กœ ํ•ฉ๋‹ˆ๋‹ค.ย ์ˆ˜์น˜ ๋ชจ๋ธ์€ ๊ท ์ผํ•œ ์˜์—ญ์˜ ์œ ์†๊ณผ ๊ณ„๋‹จ ์—ฌ์ˆ˜๋กœ์˜ ๋งˆ์ฐฐ ๊ณ„์ˆ˜๋ฅผ ์ถ”์ •ํ•˜๋Š” ๋ฐ ์‚ฌ์šฉ๋ฉ๋‹ˆ๋‹ค(ฯด = 45ยบ, Hd=4.61m).ย ํ๋ฆ„์— ๋Œ€ํ•œ ์ž๋™ ํ†ต๊ธฐ์˜ ํ‘œํ˜„์€ ๋ณต์žกํ•˜๋ฏ€๋กœ ํ”„๋กœ๊ทธ๋žจ์€ ๊ณต๊ธฐ ์—ฐํ–‰ ๋ชจ๋ธ์„ ์‚ฌ์šฉํ•˜์—ฌ ํŠน์ • ์ œํ•œ์ด ์žˆ๋Š” ์†”๋ฃจ์…˜์— ๊ทผ์ ‘ํ•ฉ๋‹ˆ๋‹ค.

The main objective of this project is to develop the numerical modeling of the skimming flow in a stepped spillway using FLOW-3D. The design of these structures is based on the use of empirical expressions obtained from physical modeling and complementary studies in the numerical modeling of flow over the stepped spillway with support of CFD code. The numerical model is used to estimate the flow velocity in the uniform region and the friction coefficient of the stepped spillway (ฯด = 45ยบ, Hd=4.61m). The representation of auto aeration a flow is complex, so the program approximates the solution with certain limitations, using an air entrainment model; drift flux model and turbulence model k-ิ‘ RNG. The results obtained with numerical modeling and physical modeling at the beginning of natural auto aeration of flow and depth of the biphasic flow in the uniform region presents deviations above to 10% perhaps the flow is highly turbulent.

Keywords : Stepped spillway; skimming flow; air entrainment; drift flux; numerical modeling; FLOW-3D.

Keywords : ๊ณ„๋‹จ์‹ ์—ฌ์ˆ˜๋กœ; ์Šคํ‚ค๋ฐ ํ๋ฆ„; ๊ณต๊ธฐ ์—ฐํ–‰; ๋“œ๋ฆฌํ”„ํŠธ ํ”Œ๋Ÿญ์Šค; ์ˆ˜์น˜ ๋ชจ๋ธ๋ง; ํ๋ฆ„-3D.ยท 

์ŠคํŽ˜์ธ์–ด๋กœ ๋œ ์ดˆ๋กย ยท ์ŠคํŽ˜์ธ์–ดย ๋กœ ๋œ ํ…์ŠคํŠธย ยทย ์ŠคํŽ˜์ธ์–ด๋กœ ๋œ ํ…์ŠคํŠธ(ย pdfย )ย 

Figure 1. Grazing flow over a rapid step.
Figure 1. Grazing flow over a rapid step.
Figura 2. Principales regiones existentes en un flujo rasante.
Figura 2. Principales regiones existentes en un flujo rasante.
Figure 3. Dimensions of the El Batรกn stepped rapid.
Figure 3. Dimensions of the El Batรกn stepped rapid.
Figure 4. 3D physical model of the El Batรกn stepped rapid
Figure 4. 3D physical model of the El Batรกn stepped rapid
Figura 7. Influencia del modelo de turbulencia. Qmodelo=27.95l/s.
Figura 7. Influencia del modelo de turbulencia. Qmodelo=27.95l/s.

REFERENCIAS

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en caรญdas en colectores.โ€, Laboratรณrio Nacional de Engenharia Civil, I.
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spillwaysโ€, Environ Fluid Mechanics.
Castro M. (2015) โ€œAnรกlisis Dimensional y Modelaciรณn fรญsica en Hidrรกulicaโ€.
Escuela Politรฉcnica Nacional. Quito Ecuador. 50 p.
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rรกpidas con perfil escalonado y liso de la quebrada el Batรกn Fase I y Fase
IIโ€, Escuela Politรฉcnica Nacional, Quito Ecuador.
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Mรฉtodo de Volรบmenes Finitosโ€. Barcelona: Revertรฉ.
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Figure 2. Different PKW Types.

A review of Piano Key Weir as a superior alternative for dam rehabilitation

๋Œ ๋ณต๊ตฌ๋ฅผ ์œ„ํ•œ ์šฐ์ˆ˜ํ•œ ๋Œ€์•ˆ์œผ๋กœ์„œ์˜ Piano Key Weir์— ๋Œ€ํ•œ ๊ฒ€ํ† 

Amiya Abhash &

K. K. Pandey

Pages 541-551 | Received 03 Mar 2020, Accepted 07 May 2020, Published online: 21 May 2020

ABSTRACT

Dams fall in โ€˜installations containing dangerous forcesโ€™ because of their massive impact on the environment and civilian life and property as per International humanitarian law. As such, it becomes vital for hydraulic engineers to refurbish various solutions for dam rehabilitation. This paper presents a review of a new type of weir installation called Piano Key Weir (PKW), which is becoming popular around the world for its higher spillway capacity both for existing and new dam spillway installations. This paper reviews the geometry along with structural integrity, discharging capacity, economic aspects, aeration requirements, sediment transport and erosion aspects of Piano Key Weir (PKW) as compared with other traditional spillway structures and alternatives from literature. The comparison with other alternatives shows PKW to be an excellent alternative for dam risk mitigation owing to its high spillway capabilities and economy, along with its use in both existing and new hydraulic structures.

๋Œ์€ ๊ตญ์ œ ์ธ๋„๋ฒ•์— ๋”ฐ๋ผ ํ™˜๊ฒฝ๊ณผ ๋ฏผ๊ฐ„์ธ ์ƒํ™œ ๋ฐ ์žฌ์‚ฐ์— ๋ง‰๋Œ€ํ•œ ์˜ํ–ฅ์„ ๋ฏธ์น˜๊ธฐ ๋•Œ๋ฌธ์— ‘์œ„ํ—˜ํ•œ ํž˜์„ ํฌํ•จํ•˜๋Š” ์‹œ์„ค๋ฌผ’์— ์†ํ•ฉ๋‹ˆ๋‹ค. ๋”ฐ๋ผ์„œ ์œ ์•• ์—”์ง€๋‹ˆ์–ด๋Š” ๋Œ ๋ณต๊ตฌ๋ฅผ ์œ„ํ•œ ๋‹ค์–‘ํ•œ ์†”๋ฃจ์…˜์„ ์žฌ์ •๋น„ํ•ด์•ผ ํ•ฉ๋‹ˆ๋‹ค.

์ด ๋ฐฑ์„œ์—์„œ๋Š” PKW(Piano Key Weir)๋ผ๋Š” ์ƒˆ๋กœ์šด ์œ ํ˜•์˜ ๋‘‘ ์„ค์น˜์— ๋Œ€ํ•œ ๊ฒ€ํ† ๋ฅผ ์ œ๊ณตํ•ฉ๋‹ˆ๋‹ค. PKW๋Š” ๊ธฐ์กด ๋ฐ ์‹ ๊ทœ ๋Œ ๋ฐฉ์ˆ˜๋กœ ์„ค์น˜ ๋ชจ๋‘์—์„œ ๋” ๋†’์€ ๋ฐฉ์ˆ˜๋กœ ์šฉ๋Ÿ‰์œผ๋กœ ์ „ ์„ธ๊ณ„์ ์œผ๋กœ ์ธ๊ธฐ๋ฅผ ์–ป๊ณ  ์žˆ์Šต๋‹ˆ๋‹ค.

์ด ๋ฐฑ์„œ์—์„œ๋Š” ๊ตฌ์กฐ์  ๋ฌด๊ฒฐ์„ฑ, ๋ฐฐ์ถœ ์šฉ๋Ÿ‰, ๊ฒฝ์ œ์  ์ธก๋ฉด, ํญ๊ธฐ ์š”๊ตฌ ์‚ฌํ•ญ, ํ‡ด์ ๋ฌผ ์šด๋ฐ˜ ๋ฐ PKW(Piano Key Weir)์˜ ์นจ์‹ ์ธก๋ฉด๊ณผ ํ•จ๊ป˜ ๋‹ค๋ฅธ ์ „ํ†ต์ ์ธ ์—ฌ์ˆ˜๋กœ ๊ตฌ์กฐ ๋ฐ ๋ฌธํ—Œ์˜ ๋Œ€์•ˆ๊ณผ ๋น„๊ตํ•˜์—ฌ ๊ธฐํ•˜ํ•™์„ ๊ฒ€ํ† ํ•ฉ๋‹ˆ๋‹ค.

๋‹ค๋ฅธ ๋Œ€์•ˆ๊ณผ์˜ ๋น„๊ต๋Š” PKW๊ฐ€ ๋†’์€ ์—ฌ์ˆ˜๋กœ ๊ธฐ๋Šฅ๊ณผ ๊ฒฝ์ œ์„ฑ์œผ๋กœ ์ธํ•ด ๋Œ ์œ„ํ—˜ ์™„ํ™”๋ฅผ ์œ„ํ•œ ํƒ์›”ํ•œ ๋Œ€์•ˆ์ด๋ฉฐ ๊ธฐ์กด ๋ฐ ์ƒˆ๋กœ์šด ์ˆ˜๋ ฅ ๊ตฌ์กฐ๋ฌผ ๋ชจ๋‘์— ์‚ฌ์šฉ๋จ์„ ๋ณด์—ฌ์ค๋‹ˆ๋‹ค.

KEYWORDS: 

Figure 2. Different PKW Types.
Figure 2. Different PKW Types.

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Figure 4. Field gate discharge experiment.

FLOW-3D Model Development for the Analysis of the Flow Characteristics of Downstream Hydraulic Structures

ํ•˜๋ฅ˜ ์œ ์•• ๊ตฌ์กฐ๋ฌผ์˜ ์œ ๋™ ํŠน์„ฑ ๋ถ„์„์„ ์œ„ํ•œ FLOW-3D ๋ชจ๋ธ ๊ฐœ๋ฐœ

Beom-Jin Kim 1, Jae-Hong Hwang 2 and Byunghyun Kim 3,*
1 Advanced Structures and Seismic Safety Research Division, Korea Atomic Energy Research Institute,
Daejeon 34057, Korea
2 Korea Water Resources Corporation (K-Water), Daejeon 34350, Korea
3 Department of Civil Engineering, Kyungpook National University, Daegu 41566, Korea

  • Correspondence: bhkimc@knu.ac.kr; Tel.: +82-53-950-7819

Abstract

Hydraulic structures installed in rivers inevitably create a water level difference between upstream and downstream regions. The potential energy due to this difference in water level is converted into kinetic energy, causing high-velocity flow and hydraulic jumps in the river. As a result, problems such as scouring and sloping downstream may occur around the hydraulic structures. In this study, a FLOW-3D model was constructed to perform a numerical analysis of the ChangnyeongHaman weir in the Republic of Korea. The constructed model was verified based on surface velocity measurements from a field gate operation experiment. In the simulation results, the flow discharge differed from the measured value by 9โ€“15 m3/s, from which the accuracy was evaluated to be 82โ€“87%. The flow velocity was evaluated with an accuracy of 92% from a difference of 0.01 to 0.16 m/s. Following this verification, a flow analysis of the hydraulic structures was performed according to boundary conditions and operation conditions for numerous scenarios. Since 2018, the ChangnyeongHaman weir gate has been fully opened due to the implementation of Koreaโ€™s eco-environmental policy; therefore, in this study, the actual gate operation history data prior to 2018 was applied and evaluated. The evaluation conditions were a 50% open gate condition and the flow discharge of two cases with a large difference in water level. As a result of the analysis, the actual operating conditions showed that the velocity and the Froude number were lower than the optimal conditions, confirming that the selected design was appropriate. It was also found that in the bed protection section, the average flow velocity was high when the water level difference was large, whereas the bottom velocity was high when the gate opening was large. Ultimately, through the reviewed status survey data in this study, the downstream flow characteristics of hydraulic structures along with adequacy verification techniques, optimal design techniques such as procedures for design, and important considerations were derived. Based on the current results, the constructed FLOW-3D-based model can be applied to creating or updating flow analysis guidelines for future repair and reinforcement measures as well as hydraulic structure design.

ํ•˜์ฒœ์— ์„ค์น˜๋˜๋Š” ์ˆ˜๋ ฅ๊ตฌ์กฐ๋ฌผ์€ ํ•„์—ฐ์ ์œผ๋กœ ์ƒ๋ฅ˜์™€ ํ•˜๋ฅ˜์˜ ์ˆ˜์œ„์ฐจ๋ฅผ ๋ฐœ์ƒ์‹œํ‚จ๋‹ค. ์ด๋Ÿฌํ•œ ์ˆ˜์œ„์ฐจ๋กœ ์ธํ•œ ์œ„์น˜์—๋„ˆ์ง€๋Š” ์šด๋™์—๋„ˆ์ง€๋กœ ๋ณ€ํ™˜๋˜์–ด ํ•˜์ฒœ์˜ ๊ณ ์†์œ ๋™๊ณผ ์ˆ˜์••์ ํ”„๋ฅผ ์ผ์œผํ‚จ๋‹ค. ๊ทธ ๊ฒฐ๊ณผ ์ˆ˜๋ ฅ๊ตฌ์กฐ๋ฌผ ์ฃผ๋ณ€์—์„œ ํ•˜๋ฅ˜์˜ ์„ธ๊ตด, ๊ฒฝ์‚ฌ ๋“ฑ์˜ ๋ฌธ์ œ๊ฐ€ ๋ฐœ์ƒํ•  ์ˆ˜ ์žˆ๋‹ค.

๋ณธ ์—ฐ๊ตฌ์—์„œ๋Š” ๋Œ€ํ•œ๋ฏผ๊ตญ ์ฐฝ๋…•ํ•จ์•ˆ๋ณด์˜ ์ˆ˜์น˜ํ•ด์„์„ ์œ„ํ•ด FLOW-3D ๋ชจ๋ธ์„ ๊ตฌ์ถ•ํ•˜์˜€๋‹ค. ๊ตฌ์ถ•๋œ ๋ชจ๋ธ์€ ํ˜„์žฅ ๊ฒŒ์ดํŠธ ์ž‘๋™ ์‹คํ—˜์—์„œ ํ‘œ๋ฉด ์†๋„ ์ธก์ •์„ ๊ธฐ๋ฐ˜์œผ๋กœ ๊ฒ€์ฆ๋˜์—ˆ์Šต๋‹ˆ๋‹ค.

์‹œ๋ฎฌ๋ ˆ์ด์…˜ ๊ฒฐ๊ณผ์—์„œ ์œ ๋Ÿ‰์€ ์ธก์ •๊ฐ’๊ณผ 9~15 m3/s ์ฐจ์ด๊ฐ€ ๋‚˜๊ณ  ์ •ํ™•๋„๋Š” 82~87%๋กœ ํ‰๊ฐ€๋˜์—ˆ๋‹ค. ์œ ์†์€ 0.01~0.16m/s์˜ ์ฐจ์ด์—์„œ 92%์˜ ์ •ํ™•๋„๋กœ ํ‰๊ฐ€๋˜์—ˆ์Šต๋‹ˆ๋‹ค.

๊ฒ€์ฆ ํ›„ ๋‹ค์–‘ํ•œ ์‹œ๋‚˜๋ฆฌ์˜ค์— ๋Œ€ํ•œ ๊ฒฝ๊ณ„์กฐ๊ฑด ๋ฐ ์šด์ „์กฐ๊ฑด์— ๋”ฐ๋ฅธ ์ˆ˜๋ฆฌ๊ตฌ์กฐ๋ฌผ์˜ ์œ ๋™ํ•ด์„์„ ์ˆ˜ํ–‰ํ•˜์˜€๋‹ค. 2018๋…„๋ถ€ํ„ฐ ์ฐฝ๋…•ํ•จ์•ˆ๋ณด ๋ฌธ์€ ํ•œ๊ตญ์˜ ์นœํ™˜๊ฒฝ ์ •์ฑ… ์‹œํ–‰์œผ๋กœ ์ „๋ฉด ๊ฐœ๋ฐฉ๋˜์—ˆ์Šต๋‹ˆ๋‹ค.

๋”ฐ๋ผ์„œ ๋ณธ ์—ฐ๊ตฌ์—์„œ๋Š” 2018๋…„ ์ด์ „์˜ ์‹ค์ œ ๊ฒŒ์ดํŠธ ์šด์˜ ์ด๋ ฅ ๋ฐ์ดํ„ฐ๋ฅผ ์ ์šฉํ•˜์—ฌ ํ‰๊ฐ€ํ•˜์˜€๋‹ค. ํ‰๊ฐ€์กฐ๊ฑด์€ 50% open gate ์กฐ๊ฑด๊ณผ ์ˆ˜์œ„์ฐจ๊ฐ€ ํฐ 2๊ฐ€์ง€ ๊ฒฝ์šฐ์˜ ์œ ์ˆ˜๋ฐฉ๋ฅ˜๋กœ ํ•˜์˜€๋‹ค. ํ•ด์„ ๊ฒฐ๊ณผ ์‹ค์ œ ์šด์ „์กฐ๊ฑด์€ ์†๋„์™€ Froude์ˆ˜๊ฐ€ ์ตœ์ ์กฐ๊ฑด๋ณด๋‹ค ๋‚ฎ์•„ ์„ ์ •๋œ ์„ค๊ณ„๊ฐ€ ์ ํ•ฉํ•จ์„ ํ™•์ธํ•˜์˜€๋‹ค.

๋˜ํ•œ ๋ฒ ๋“œ๋ณดํ˜ธ๊ตฌ๊ฐ„์—์„œ๋Š” ์ˆ˜์œ„์ฐจ๊ฐ€ ํฌ๋ฉด ํ‰๊ท ์œ ์†์ด ๋†’๊ณ , ์ˆ˜๋ฌธ๊ฐœ๊ตฌ๊ฐ€ ํฌ๋ฉด ์ €์ €์œ ์†์ด ๋†’์€ ๊ฒƒ์œผ๋กœ ๋‚˜ํƒ€๋‚ฌ๋‹ค. ์ตœ์ข…์ ์œผ๋กœ ๋ณธ ์—ฐ๊ตฌ์—์„œ ๊ฒ€ํ† ํ•œ ์‹คํƒœ์กฐ์‚ฌ ์ž๋ฃŒ๋ฅผ ํ†ตํ•ด ์ ์ •์„ฑ ๊ฒ€์ฆ๊ธฐ๋ฒ•๊ณผ ํ•จ๊ป˜ ์ˆ˜๋ ฅ๊ตฌ์กฐ๋ฌผ์˜ ํ•˜๋ฅ˜ ์œ ๋™ํŠน์„ฑ, ์„ค๊ณ„์ ˆ์ฐจ ๋“ฑ ์ตœ์  ์„ค๊ณ„๊ธฐ๋ฒ• ๋ฐ ์ค‘์š” ๊ณ ๋ ค์‚ฌํ•ญ์„ ๋„์ถœํ•˜์˜€๋‹ค.

ํ˜„์žฌ์˜ ๊ฒฐ๊ณผ๋ฅผ ๋ฐ”ํƒ•์œผ๋กœ ๊ตฌ์ถ•๋œ FLOW-3D ๊ธฐ๋ฐ˜ ๋ชจ๋ธ์€ ์ˆ˜๋ ฅ๊ตฌ์กฐ ์„ค๊ณ„๋ฟ๋งŒ ์•„๋‹ˆ๋ผ ํ–ฅํ›„ ๋ณด์ˆ˜ ๋ฐ ๋ณด๊ฐ• ์กฐ์น˜๋ฅผ ์œ„ํ•œ ์œ ๋™ํ•ด์„ ๊ฐ€์ด๋“œ๋ผ์ธ ์ƒ์„ฑ ๋˜๋Š” ์—…๋ฐ์ดํŠธ์— ์ ์šฉํ•  ์ˆ˜ ์žˆ์Šต๋‹ˆ๋‹ค.

Figure 1. Effect of downstream riverbed erosion according to the type of weir foundation.
Figure 1. Effect of downstream riverbed erosion according to the type of weir foundation.
Figure 2. Changnyeong-Haman weir depth survey results (June 2015)
Figure 2. Changnyeong-Haman weir depth survey results (June 2015)
Figure 4. Field gate discharge experiment.
Figure 4. Field gate discharge experiment.
Figure 16. Analysis results for Case 7 and Case 8
Figure 16. Analysis results for Case 7 and Case 8

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  28. French, R.H.; French, R.H. Open-Channel Hydraulics; McGraw-Hill: New York, NY, USA, 1985; ISBN 0070221340.
Serife Yurdagul Kumcuโˆ’2โˆ’KSCE Journal of Civil Engineeringthe use of CFD for the assessment of a design, as well as screeningand optimizing of hydraulic structures and cofferdam layouts. Theyconclude that CFD has been successful in optimizing the finalconceptual configuration for the hydraulics design of the project,but recommend that physical modeling still be used as a finalconfirmation.This paper provides experimental studies performed on Kav akDam and analyses the stability of spillway design by usingFLOW-3D model. It compares the hydraulic model tests withFLOW-3D simulation results and gives information on howaccurately a commercially available Computational Fluid Dynamic(CFD) model can predict the spillway discharge capacity andpressure distribution along the spillway bottom surface. 2. Physical ModelA 1/50-scaled undistorted physical model of the Kavsak Damspillway and stilling basin was built and tested at the HydraulicModel Laboratory of State Hydraulic Works of Turkey (DSI).The model was constructed of plexiglas and was fabricated toconform to the distinctive shape of an ogee crest. The spillwayhas 45.8 m in width and 57 m long with a bottom slope of 125%.The length of the stilling basin is about 90 m. During model tests,flow velocities were measured with an ultrasonic flow meter.Pressures on the spillway were measured using a piezometerssรงTable 1. Upstream and Downstream Operating Conditions of theKavsak DamRun Upstream reservoir elevation (m)Downstream tailwater elevation (m)1 306.55 168.002 311.35 174.503 314.00 178.904 316.50 182.55Fig. 1. (a) Original Project Design and Final Project Design after Experimental Investigations and Flow Measurement Sections at theApproach, (b) Top View Experimentally Modified Approach in the Laboratory, (c) Side View of the Experimentally Modified Approachin the Laboratory

Investigation of flow over spillway modeling and comparison between experimental data and CFD analysis

์—ฌ์ˆ˜๋กœ ๋ชจ๋ธ๋ง ๋ฐ ์‹คํ—˜ ๋ฐ์ดํ„ฐ์™€ CFD ํ•ด์„์˜ ๋น„๊ต์— ๋Œ€ํ•œ ์กฐ์‚ฌ

DOI:10.1007/s12205-016-1257-z

Authors:

Serife Yurdagul Kumcu at Necmettin Erbakan รœniversitesi

Serife Yurdagul Kumcu

Abstract and Figures

As a part of design process for hydro-electric generating stations, hydraulic engineers typically conduct some form of model testing. The desired outcome from the testing can vary considerably depending on the specific situation, but often characteristics such as velocity patterns, discharge rating curves, water surface profiles, and pressures at various locations are measured. Due to recent advances in computational power and numerical techniques, it is now also possible to obtain much of this information through numerical modeling. In this paper, hydraulic characteristics of Kavsak Dam and Hydroelectric Power Plant (HEPP), which are under construction and built for producing energy in Turkey, were investigated experimentally by physical model studies. The 1/50-scaled physical model was used in conducting experiments. Flow depth, discharge and pressure data were recorded for different flow conditions. Serious modification was made on the original project with the experimental study. In order to evaluate the capability of the computational fluid dynamics on modeling spillway flow a comparative study was made by using results obtained from physical modeling and Computational Fluid Dynamics (CFD) simulation. A commercially available CFD program, which solves the Reynolds-averaged Navier-Stokes (RANS) equations, was used to model the numerical model setup by defining cells where the flow is partially or completely restricted in the computational space. Discharge rating curves, velocity patterns and pressures were used to compare the results of the physical model and the numerical model. It was shown that there is reasonably good agreement between the physical and numerical models in flow characteristics.

์ˆ˜๋ ฅ ๋ฐœ์ „์†Œ ์„ค๊ณ„ ํ”„๋กœ์„ธ์Šค์˜ ์ผ๋ถ€๋กœ ์ˆ˜๋ ฅ ์—”์ง€๋‹ˆ์–ด๋Š” ์ผ๋ฐ˜์ ์œผ๋กœ ์–ด๋–ค ํ˜•ํƒœ์˜ ๋ชจ๋ธ ํ…Œ์ŠคํŠธ๋ฅผ ์ˆ˜ํ–‰ํ•ฉ๋‹ˆ๋‹ค. ํ…Œ์ŠคํŠธ์—์„œ ์›ํ•˜๋Š” ๊ฒฐ๊ณผ๋Š” ํŠน์ • ์ƒํ™ฉ์— ๋”ฐ๋ผ ์ƒ๋‹นํžˆ ๋‹ค๋ฅผ ์ˆ˜ ์žˆ์ง€๋งŒ ์†๋„ ํŒจํ„ด, ๋ฐฉ์ „ ๋“ฑ๊ธ‰ ๊ณก์„ , ์ˆ˜๋ฉด ํ”„๋กœํŒŒ์ผ ๋ฐ ๋‹ค์–‘ํ•œ ์œ„์น˜์—์„œ์˜ ์••๋ ฅ๊ณผ ๊ฐ™์€ ํŠน์„ฑ์ด ์ธก์ •๋˜๋Š” ๊ฒฝ์šฐ๊ฐ€ ๋งŽ์Šต๋‹ˆ๋‹ค. ์ตœ๊ทผ ๊ณ„์‚ฐ ๋Šฅ๋ ฅ๊ณผ ์ˆ˜์น˜ ๊ธฐ๋ฒ•์˜ ๋ฐœ์ „์œผ๋กœ ์ธํ•ด ์ด์ œ๋Š” ์ˆ˜์น˜ ๋ชจ๋ธ๋ง์„ ํ†ตํ•ด ์ด๋Ÿฌํ•œ ์ •๋ณด์˜ ๋Œ€๋ถ€๋ถ„์„ ์–ป์„ ์ˆ˜๋„ ์žˆ์Šต๋‹ˆ๋‹ค.

๋ณธ ๋…ผ๋ฌธ์—์„œ๋Š” ํ„ฐํ‚ค์—์„œ ์—๋„ˆ์ง€ ์ƒ์‚ฐ์„ ์œ„ํ•ด ๊ฑด์„ค ์ค‘์ธ Kavsak ๋Œ๊ณผ ์ˆ˜๋ ฅ๋ฐœ์ „์†Œ(HEPP)์˜ ์ˆ˜๋ ฅํ•™์  ํŠน์„ฑ์„ ๋ฌผ๋ฆฌ์  ๋ชจ๋ธ ์—ฐ๊ตฌ๋ฅผ ํ†ตํ•ด ์‹คํ—˜์ ์œผ๋กœ ์กฐ์‚ฌํ•˜์˜€๋‹ค. 1/50 ์Šค์ผ€์ผ์˜ ๋ฌผ๋ฆฌ์  ๋ชจ๋ธ์ด ์‹คํ—˜ ์ˆ˜ํ–‰์— ์‚ฌ์šฉ๋˜์—ˆ์Šต๋‹ˆ๋‹ค. ๋‹ค์–‘ํ•œ ํ๋ฆ„ ์กฐ๊ฑด์— ๋Œ€ํ•ด ํ๋ฆ„ ๊นŠ์ด, ๋ฐฐ์ถœ ๋ฐ ์••๋ ฅ ๋ฐ์ดํ„ฐ๊ฐ€ ๊ธฐ๋ก๋˜์—ˆ์Šต๋‹ˆ๋‹ค. ์‹คํ—˜ ์—ฐ๊ตฌ๋ฅผ ํ†ตํ•ด ์›๋ž˜ ํ”„๋กœ์ ํŠธ์— ๋Œ€๋Œ€์ ์ธ ์ˆ˜์ •์ด ์ด๋ฃจ์–ด์กŒ์Šต๋‹ˆ๋‹ค.

๋ฐฐ์ˆ˜๋กœ ํ๋ฆ„ ๋ชจ๋ธ๋ง์— ๋Œ€ํ•œ ์ „์‚ฐ์œ ์ฒด์—ญํ•™์˜ ๋Šฅ๋ ฅ์„ ํ‰๊ฐ€ํ•˜๊ธฐ ์œ„ํ•ด ๋ฌผ๋ฆฌ์  ๋ชจ๋ธ๋ง๊ณผ ์ „์‚ฐ์œ ์ฒด์—ญํ•™(CFD) ์‹œ๋ฎฌ๋ ˆ์ด์…˜ ๊ฒฐ๊ณผ๋ฅผ ์ด์šฉํ•˜์—ฌ ๋น„๊ต ์—ฐ๊ตฌ๋ฅผ ์ˆ˜ํ–‰ํ•˜์˜€์Šต๋‹ˆ๋‹ค. RANS(Reynolds-averaged Navier-Stokes) ๋ฐฉ์ •์‹์„ ํ‘ธ๋Š” ์ƒ์—…์ ์œผ๋กœ ์ด์šฉ ๊ฐ€๋Šฅํ•œ CFD ํ”„๋กœ๊ทธ๋žจ์€ ํ๋ฆ„์ด ๊ณ„์‚ฐ ๊ณต๊ฐ„์—์„œ ๋ถ€๋ถ„์ ์œผ๋กœ ๋˜๋Š” ์™„์ „ํžˆ ์ œํ•œ๋˜๋Š” ์…€์„ ์ •์˜ํ•˜์—ฌ ์ˆ˜์น˜ ๋ชจ๋ธ ์„ค์ •์„ ๋ชจ๋ธ๋งํ•˜๋Š” ๋ฐ ์‚ฌ์šฉ๋˜์—ˆ์Šต๋‹ˆ๋‹ค.

๋ฌผ๋ฆฌ์  ๋ชจ๋ธ๊ณผ ์ˆ˜์น˜ ๋ชจ๋ธ์˜ ๊ฒฐ๊ณผ๋ฅผ ๋น„๊ตํ•˜๊ธฐ ์œ„ํ•ด ๋ฐฐ์ถœ ๋“ฑ๊ธ‰ ๊ณก์„ , ์†๋„ ํŒจํ„ด ๋ฐ ์••๋ ฅ์„ ์‚ฌ์šฉํ–ˆ์Šต๋‹ˆ๋‹ค. ์œ ๋™ ํŠน์„ฑ์—์„œ ๋ฌผ๋ฆฌ์  ๋ชจ๋ธ๊ณผ ์ˆ˜์น˜ ๋ชจ๋ธ ๊ฐ„์— ์ƒ๋‹นํžˆ ์ข‹์€ ์ผ์น˜๊ฐ€ ์žˆ๋Š” ๊ฒƒ์œผ๋กœ ๋‚˜ํƒ€๋‚ฌ์Šต๋‹ˆ๋‹ค.

Serife Yurdagul Kumcuโˆ’2โˆ’KSCE Journal of Civil Engineeringthe use of CFD for the assessment of a design, as well as screeningand optimizing of hydraulic structures and cofferdam layouts. Theyconclude that CFD has been successful in optimizing the finalconceptual configuration for the hydraulics design of the project,but recommend that physical modeling still be used as a finalconfirmation.This paper provides experimental studies performed on Kav akDam and analyses the stability of spillway design by usingFLOW-3D model. It compares the hydraulic model tests withFLOW-3D simulation results and gives information on howaccurately a commercially available Computational Fluid Dynamic(CFD) model can predict the spillway discharge capacity andpressure distribution along the spillway bottom surface. 2. Physical ModelA 1/50-scaled undistorted physical model of the Kavsak Damspillway and stilling basin was built and tested at the HydraulicModel Laboratory of State Hydraulic Works of Turkey (DSI).The model was constructed of plexiglas and was fabricated toconform to the distinctive shape of an ogee crest. The spillwayhas 45.8 m in width and 57 m long with a bottom slope of 125%.The length of the stilling basin is about 90 m. During model tests,flow velocities were measured with an ultrasonic flow meter.Pressures on the spillway were measured using a piezometerssรงTable 1. Upstream and Downstream Operating Conditions of theKavsak DamRun Upstream reservoir elevation (m)Downstream tailwater elevation (m)1 306.55 168.002 311.35 174.503 314.00 178.904 316.50 182.55Fig. 1. (a) Original Project Design and Final Project Design after Experimental Investigations and Flow Measurement Sections at theApproach, (b) Top View Experimentally Modified Approach in the Laboratory, (c) Side View of the Experimentally Modified Approachin the Laboratory
Serife Yurdagul Kumcuโˆ’2โˆ’KSCE Journal of Civil Engineeringthe use of CFD for the assessment of a design, as well as screeningand optimizing of hydraulic structures and cofferdam layouts. Theyconclude that CFD has been successful in optimizing the finalconceptual configuration for the hydraulics design of the project,but recommend that physical modeling still be used as a finalconfirmation.This paper provides experimental studies performed on Kav akDam and analyses the stability of spillway design by usingFLOW-3D model. It compares the hydraulic model tests withFLOW-3D simulation results and gives information on howaccurately a commercially available Computational Fluid Dynamic(CFD) model can predict the spillway discharge capacity andpressure distribution along the spillway bottom surface. 2. Physical ModelA 1/50-scaled undistorted physical model of the Kavsak Damspillway and stilling basin was built and tested at the HydraulicModel Laboratory of State Hydraulic Works of Turkey (DSI).The model was constructed of plexiglas and was fabricated toconform to the distinctive shape of an ogee crest. The spillwayhas 45.8 m in width and 57 m long with a bottom slope of 125%.The length of the stilling basin is about 90 m. During model tests,flow velocities were measured with an ultrasonic flow meter.Pressures on the spillway were measured using a piezometerssรงTable 1. Upstream and Downstream Operating Conditions of theKavsak DamRun Upstream reservoir elevation (m)Downstream tailwater elevation (m)1 306.55 168.002 311.35 174.503 314.00 178.904 316.50 182.55Fig. 1. (a) Original Project Design and Final Project Design after Experimental Investigations and Flow Measurement Sections at theApproach, (b) Top View Experimentally Modified Approach in the Laboratory, (c) Side View of the Experimentally Modified Approachin the Laboratory

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Fig. 1. Averaged error trend.

Assessment of spillway modeling using computational fluid dynamics

์ „์‚ฐ์œ ์ฒด์—ญํ•™์„ ์ด์šฉํ•œ ์—ฌ์ˆ˜๋กœ ๋ชจ๋ธ๋ง ํ‰๊ฐ€

Authors: Paul G. Chanel and John C. Doering AUTHORS INFO & AFFILIATIONS

Publication: Canadian Journal of Civil Engineering

3 December 2008

Abstract

Throughout the design and planning period for future hydroelectric generating stations, hydraulic engineers are increasingly integrating computational fluid dynamics (CFD) into the process. As a result, hydraulic engineers are interested in the reliability of CFD software to provide accurate flow data for a wide range of structures, including a variety of different spillways. In the literature, CFD results have generally been in agreement with physical model experimental data. Despite past success, there has not been a comprehensive assessment that looks at the ability of CFD to model a range of different spillway configurations, including flows with various gate openings. In this article, Flow-3D is used to model the discharge over ogee-crested spillways. The numerical model results are compared with physical model studies for three case study evaluations. The comparison indicates that the accuracy of Flow-3D is related to the parameterย P/Hd.

๋ฏธ๋ž˜์˜ ์ˆ˜๋ ฅ ๋ฐœ์ „์†Œ๋ฅผ ์œ„ํ•œ ์„ค๊ณ„ ๋ฐ ๊ณ„ํš ๊ธฐ๊ฐ„ ๋™์•ˆ ์œ ์•• ์—”์ง€๋‹ˆ์–ด๋Š” ์ „์‚ฐ์œ ์ฒด์—ญํ•™(CFD)์„ ํ”„๋กœ์„ธ์Šค์— ์ ์  ๋” ๋งŽ์ด ํ†ตํ•ฉํ•˜๊ณ  ์žˆ์Šต๋‹ˆ๋‹ค. ๊ฒฐ๊ณผ์ ์œผ๋กœ ์œ ์•• ์—”์ง€๋‹ˆ์–ด๋Š” ๋‹ค์–‘ํ•œ ์—ฌ์ˆ˜๋กœ๋ฅผ ํฌํ•จํ•˜์—ฌ ๊ด‘๋ฒ”์œ„ํ•œ ๊ตฌ์กฐ์— ๋Œ€ํ•œ ์ •ํ™•ํ•œ ํ๋ฆ„ ๋ฐ์ดํ„ฐ๋ฅผ ์ œ๊ณตํ•˜๋Š” CFD ์†Œํ”„ํŠธ์›จ์–ด์˜ ์‹ ๋ขฐ์„ฑ์— ๊ด€์‹ฌ์„ ๊ฐ–๊ณ  ์žˆ์Šต๋‹ˆ๋‹ค. ๋ฌธํ—Œ์—์„œ CFD ๊ฒฐ๊ณผ๋Š” ์ผ๋ฐ˜์ ์œผ๋กœ ๋ฌผ๋ฆฌ์  ๋ชจ๋ธ ์‹คํ—˜ ๋ฐ์ดํ„ฐ์™€ ์ผ์น˜ํ–ˆ์Šต๋‹ˆ๋‹ค. ๊ณผ๊ฑฐ์˜ ์„ฑ๊ณต์—๋„ ๋ถˆ๊ตฌํ•˜๊ณ  ๋‹ค์–‘ํ•œ ๊ฒŒ์ดํŠธ ๊ฐœ๊ตฌ๋ถ€๊ฐ€ ์žˆ๋Š” ํ๋ฆ„์„ ํฌํ•จํ•˜์—ฌ ๋‹ค์–‘ํ•œ ์—ฌ์ˆ˜๋กœ ๊ตฌ์„ฑ์„ ๋ชจ๋ธ๋งํ•˜๋Š” CFD์˜ ๊ธฐ๋Šฅ์„ ์‚ดํŽด๋ณด๋Š” ํฌ๊ด„์ ์ธ ํ‰๊ฐ€๋Š” ์—†์—ˆ์Šต๋‹ˆ๋‹ค. ์ด ๊ธฐ์‚ฌ์—์„œ๋Š” Flow-3D๋ฅผ ์‚ฌ์šฉํ•˜์—ฌ ogee-crested ๋ฐฉ์ˆ˜๋กœ์˜ ๋ฐฐ์ถœ์„ ๋ชจ๋ธ๋งํ•ฉ๋‹ˆ๋‹ค. ์„ธ ๊ฐ€์ง€ ์‚ฌ๋ก€ ์—ฐ๊ตฌ ํ‰๊ฐ€๋ฅผ ์œ„ํ•ด ์ˆ˜์น˜ ๋ชจ๋ธ ๊ฒฐ๊ณผ๋ฅผ ๋ฌผ๋ฆฌ์  ๋ชจ๋ธ ์—ฐ๊ตฌ์™€ ๋น„๊ตํ•ฉ๋‹ˆ๋‹ค. ๋น„๊ต๋Š” Flow-3D์˜ ์ •ํ™•๋„๊ฐ€ ๋งค๊ฐœ๋ณ€์ˆ˜ P/Hd์™€ ๊ด€๋ จ๋˜์–ด ์žˆ์Œ์„ ๋‚˜ํƒ€๋ƒ…๋‹ˆ๋‹ค.

Rรฉsumรฉ

Les ingรฉnieurs en hydraulique intรจgrent de plus en plus la dynamique des fluides numรฉrique (ยซ CFD ยป) dans le processus de conception et de planification des futures centrales. Ainsi, les ingรฉnieurs en hydraulique sโ€™intรฉressent ร  la fiabilitรฉ du logiciel de ยซ CFD ยป afin de fournir des donnรฉes prรฉcises sur le dรฉbit pour une large gamme de structures, incluant diffรฉrents types dโ€™รฉvacuateurs. Les rรฉsultats de ยซ CFD ยป dans la littรฉrature ont รฉtรฉ globalement sont gรฉnรฉralement en accord avec les donnรฉes expรฉrimentales des essais physiques. Malgrรฉ les succรจs antรฉrieurs, il nโ€™y avait aucune รฉvaluation complรจte de la capacitรฉ des ยซ CFD ยป ร  modรฉliser une plage de configuration des รฉvacuateurs, incluant les dรฉbits ร  diverses ouvertures de vannes. Dans le prรฉsent article, le logiciel Flow-3D est utilisรฉ pour modรฉliser le dรฉbit par des รฉvacuateurs en doucine. Les rรฉsultats du modรจle de calcul sont comparรฉs ร  ceux des essais physiques pour trois รฉtudes de cas. La comparaison montre que la prรฉcision du logiciel Flow-3D est associรฉe au paramรจtre P/Hd.

Fig. 1. Averaged error trend.
Fig. 1. Averaged error trend.

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Sketch of approach channel and spillway of the Kamal-Saleh dam

CFD modeling of flow pattern in spillwayโ€™s approach channel

Sustainable Water Resources Management volume 1, pages245โ€“251 (2015)Cite this article

Abstract

Analysis of behavior and hydraulic characteristics of flow over the dam spillway is a complicated task that takes lots of money and time in water engineering projects planning. To model those hydraulic characteristics, several methods such as physical and numerical methods can be used. Nowadays, by utilizing new methods in computational fluid dynamics (CFD) and by the development of fast computers, the numerical methods have become accessible for use in the analysis of such sophisticated flows. The CFD softwares have the capability to analyze two- and three-dimensional flow fields. In this paper, the flow pattern at the guide wall of the Kamal-Saleh dam was modeled by Flow 3D. The results show that the current geometry of the left wall causes instability in the flow pattern and making secondary and vortex flow at beginning approach channel. This shape of guide wall reduced the performance of weir to remove the peak flood discharge.

๋Œ ์—ฌ์ˆ˜๋กœ ํ๋ฆ„์˜ ๊ฑฐ๋™ ๋ฐ ์ˆ˜๋ฆฌํ•™์  ํŠน์„ฑ ๋ถ„์„์€ ๋ฌผ ๊ณตํ•™ ํ”„๋กœ์ ํŠธ ๊ณ„ํš์— ๋งŽ์€ ๋น„์šฉ๊ณผ ์‹œ๊ฐ„์ด ์†Œ์š”๋˜๋Š” ๋ณต์žกํ•œ ์ž‘์—…์ž…๋‹ˆ๋‹ค. ์ด๋Ÿฌํ•œ ์ˆ˜๋ ฅํ•™์  ํŠน์„ฑ์„ ๋ชจ๋ธ๋งํ•˜๊ธฐ ์œ„ํ•ด ๋ฌผ๋ฆฌ์ , ์ˆ˜์น˜์  ๋ฐฉ๋ฒ•๊ณผ ๊ฐ™์€ ์—ฌ๋Ÿฌ ๊ฐ€์ง€ ๋ฐฉ๋ฒ•์„ ์‚ฌ์šฉํ•  ์ˆ˜ ์žˆ์Šต๋‹ˆ๋‹ค. ์š”์ฆ˜์—๋Š” ์ „์‚ฐ์œ ์ฒด์—ญํ•™(CFD)์˜ ์ƒˆ๋กœ์šด ๋ฐฉ๋ฒ•์„ ํ™œ์šฉํ•˜๊ณ  ๋น ๋ฅธ ์ปดํ“จํ„ฐ์˜ ๊ฐœ๋ฐœ๋กœ ์ด๋Ÿฌํ•œ ์ •๊ตํ•œ ํ๋ฆ„์˜ ํ•ด์„์— ์ˆ˜์น˜ ๋ฐฉ๋ฒ•์„ ์‚ฌ์šฉํ•  ์ˆ˜ ์žˆ๊ฒŒ ๋˜์—ˆ์Šต๋‹ˆ๋‹ค. CFD ์†Œํ”„ํŠธ์›จ์–ด์—๋Š” 2์ฐจ์› ๋ฐ 3์ฐจ์› ์œ ๋™์žฅ์„ ๋ถ„์„ํ•˜๋Š” ๊ธฐ๋Šฅ์ด ์žˆ์Šต๋‹ˆ๋‹ค. ๋ณธ ๋…ผ๋ฌธ์—์„œ๋Š” Kamal-Saleh ๋Œ ์œ ๋„๋ฒฝ์˜ ํ๋ฆ„ ํŒจํ„ด์„ Flow 3D๋กœ ๋ชจ๋ธ๋งํ•˜์˜€๋‹ค. ๊ฒฐ๊ณผ๋Š” ์™ผ์ชฝ ๋ฒฝ์˜ ํ˜„์žฌ ํ˜•์ƒ์ด ํ๋ฆ„ ํŒจํ„ด์˜ ๋ถˆ์•ˆ์ •์„ฑ์„ ์œ ๋ฐœํ•˜๊ณ  ์‹œ์ž‘ ์ ‘๊ทผ ์ฑ„๋„์—์„œ 2์ฐจ ๋ฐ ์™€๋ฅ˜ ํ๋ฆ„์„ ๋งŒ๋“œ๋Š” ๊ฒƒ์„ ๋ณด์—ฌ์ค๋‹ˆ๋‹ค. ์ด๋Ÿฌํ•œ ํ˜•ํƒœ์˜ ์•ˆ๋‚ด๋ฒฝ์€ ์ฒจ๋‘๋ฐฉ๋ฅ˜๋Ÿ‰์„ ์ œ๊ฑฐํ•˜๊ธฐ ์œ„ํ•ด ๋‘‘์˜ ์„ฑ๋Šฅ์„ ์ €ํ•˜์‹œ์ผฐ๋‹ค.

Introduction

Spillways are one of the main structures used in the dam projects. Design of the spillway in all types of dams, specifically earthen dams is important because the inability of the spillway to remove probable maximum flood (PMF) discharge may cause overflow of water which ultimately leads to destruction of the dam (Das and Saikia et al. 2009; E 2013 and Novak et al. 2007). So study on the hydraulic characteristics of this structure is important. Hydraulic properties of spillway including flow pattern at the entrance of the guide walls and along the chute. Moreover, estimating the values of velocity and pressure parameters of flow along the chute is very important (Chanson 2004; Chatila and Tabbara 2004). The purpose of the study on the flow pattern is the effect of wall geometry on the creation transverse waves, flow instability, rotating and reciprocating flow through the inlet of spillway and its chute (Parsaie and Haghiabi 2015ab; Parsaie et al. 2015; Wang and Jiang 2010). The purpose of study on the values of velocity and pressure is to calculate the potential of the structure to occurrence of phenomena such as cavitation (Fattor and Bacchiega 2009; Ma et al. 2010). Sometimes, it can be seen that the spillway design parameters of pressure and velocity are very suitable, but geometry is considered not suitable for conducting walls causing unstable flow pattern over the spillway, rotating flows at the beginning of the spillway and its design reduced the flood discharge capacity (Fattor and Bacchiega 2009). Study on spillway is usually conducted using physical models (Su et al. 2009; Suprapto 2013; Wang and Chen 2009; Wang and Jiang 2010). But recently, with advances in the field of computational fluid dynamics (CFD), study on hydraulic characteristics of this structure has been done with these techniques (Chatila and Tabbara 2004; Zhenwei et al. 2012). Using the CFD as a powerful technique for modeling the hydraulic structures can reduce the time and cost of experiments (Tabbara et al. 2005). In CFD field, the Navierโ€“Stokes equation is solved by powerful numerical methods such as finite element method and finite volumes (Kim and Park 2005; Zhenwei et al. 2012). In order to obtain closed-form Navierโ€“Stokes equations turbulence models, such k โˆ’ ฮต and Re-Normalisation Group (RNG) models have been presented. To use the technique of computational fluid dynamics, software packages such as Fluent and Flow 3D, etc., are provided. Recently, these two software packages have been widely used in hydraulic engineering because the performance and their accuracy are very suitable (Gessler 2005; Kim 2007; Kim et al. 2012; Milรฉsi and Causse 2014; Montagna et al. 2011). In this paper, to assess the flow pattern at Kamal-Saleh guide wall, numerical method has been used. All the stages of numerical modeling were conducted in the Flow 3D software.

Materials and methods

Firstly, a three-dimensional model was constructed according to two-dimensional map that was prepared for designing the spillway. Then a small model was prepared with scale of 1:80 and entered into the Flow 3D software; all stages of the model construction was conducted in AutoCAD 3D. Flow 3D software numerically solved the Navierโ€“Stokes equation by finite volume method. Below is a brief reference on the equations that used in the software. Figure 1 shows the 3D sketch of Kamal-Saleh spillway and Fig. 2 shows the uploading file of the Kamal-Saleh spillway in Flow 3D software.

figure 1
Fig. 1
figure 2
Fig. 2

Review of the governing equations in software Flow 3D

Continuity equation at three-dimensional Cartesian coordinates is given as Eq (1).

vfโˆ‚ฯโˆ‚t+โˆ‚โˆ‚x(uAx)+โˆ‚โˆ‚x(vAy)+โˆ‚โˆ‚x(wAz)=PSORฯ,vfโˆ‚ฯโˆ‚t+โˆ‚โˆ‚x(uAx)+โˆ‚โˆ‚x(vAy)+โˆ‚โˆ‚x(wAz)=PSORฯ,

(1)

where uvz are velocity component in the x, y, z direction; A xA yA z cross-sectional area of the flow; ฯ fluid density; PSOR the source term; v f is the volume fraction of the fluid and three-dimensional momentum equations given in Eq (2).

โˆ‚uโˆ‚t+1vf(uAxโˆ‚uโˆ‚x+vAyโˆ‚uโˆ‚y+wAzโˆ‚uโˆ‚z)=โˆ’1ฯโˆ‚Pโˆ‚x+Gx+fxโˆ‚vโˆ‚t+1vf(uAxโˆ‚vโˆ‚x+vAyโˆ‚vโˆ‚y+wAzโˆ‚vโˆ‚z)=โˆ’1ฯโˆ‚Pโˆ‚y+Gy+fyโˆ‚wโˆ‚t+1vf(uAxโˆ‚wโˆ‚x+vAyโˆ‚wโˆ‚y+wAzโˆ‚wโˆ‚z)=โˆ’1ฯโˆ‚Pโˆ‚y+Gz+fz,โˆ‚uโˆ‚t+1vf(uAxโˆ‚uโˆ‚x+vAyโˆ‚uโˆ‚y+wAzโˆ‚uโˆ‚z)=โˆ’1ฯโˆ‚Pโˆ‚x+Gx+fxโˆ‚vโˆ‚t+1vf(uAxโˆ‚vโˆ‚x+vAyโˆ‚vโˆ‚y+wAzโˆ‚vโˆ‚z)=โˆ’1ฯโˆ‚Pโˆ‚y+Gy+fyโˆ‚wโˆ‚t+1vf(uAxโˆ‚wโˆ‚x+vAyโˆ‚wโˆ‚y+wAzโˆ‚wโˆ‚z)=โˆ’1ฯโˆ‚Pโˆ‚y+Gz+fz,

(2)

where P is the fluid pressure; G xG yG z the acceleration created by body fluids; f xf yf z viscosity acceleration in three dimensions and v f is related to the volume of fluid, defined by Eq. (3). For modeling of free surface profile the VOF technique based on the volume fraction of the computational cells has been used. Since the volume fraction F represents the amount of fluid in each cell, it takes value between 0 and 1.

โˆ‚Fโˆ‚t+1vf[โˆ‚โˆ‚x(FAxu)+โˆ‚โˆ‚y(FAyv)+โˆ‚โˆ‚y(FAzw)]=0โˆ‚Fโˆ‚t+1vf[โˆ‚โˆ‚x(FAxu)+โˆ‚โˆ‚y(FAyv)+โˆ‚โˆ‚y(FAzw)]=0

(3)

Turbulence models

Flow 3D offers five types of turbulence models: Prantl mixing length, k โˆ’ ฮต equation, RNG models, Large eddy simulation model. Turbulence models that have been proposed recently are based on Reynolds-averaged Navierโ€“Stokes equations. This approach involves statistical methods to extract an averaged equation related to the turbulence quantities.

Steps of solving a problem in Flow 3D software

(1) Preparing the 3D model of spillway by AutoCAD software. (2) Uploading the file of 3D model in Flow 3D software and defining the problem in the software and checking the final mesh. (3) Choosing the basic equations that should be solved. (4) Defining the characteristics of fluid. (5) Defining the boundary conditions; it is notable that this software has a wide range of boundary conditions. (6) Initializing the flow field. (7) Adjusting the output. (8) Adjusting the control parameters, choice of the calculation method and solution formula. (9) Start of calculation. Figure 1 shows the 3D model of the Kamal-Saleh spillway; in this figure, geometry of the left and right guide wall is shown.

Figure 2 shows the uploading of the 3D spillway dam in Flow 3D software. Moreover, in this figure the considered boundary condition in software is shown. At the entrance and end of spillway, the flow rate or fluid elevation and outflow was considered as BC. The bottom of spillway was considered as wall and left and right as symmetry.

Model calibration

Calibration of the Flow 3D for modeling the effect of geometry of guide wall on the flow pattern is included for comparing the results of Flow 3D with measured water surface profile. Calibration the Flow 3D software could be conducted in two ways: first, changing the value of upstream boundary conditions is continued until the results of water surface profile of the Flow 3D along the spillway successfully covered the measurement water surface profile; second is the assessment the mesh sensitivity. Analyzing the size of mesh is a trial-and-error process where the size of mesh is evaluated form the largest to the smallest. With fining the size of mesh the accuracy of model is increased; whereas, the cost of computation is increased. In this research, the value of upstream boundary condition was adjusted with measured data during the experimental studies on the scaled model and the mesh size was equal to 1 ร— 1 ร— 1 cm3.

Results and discussion

The behavior of water in spillway is strongly affected by the flow pattern at the entrance of the spillway, the flow pattern formation at the entrance is affected by the guide wall, and choice of an optimized form for the guide wall has a great effect on rising the ability of spillway for easy passing the PMF, so any nonuniformity in flow in the approach channel can cause reduction of spillway capacity, reduction in discharge coefficient of spillway, and even probability of cavitation. Optimizing the flow guiding walls (in terms of length, angle and radius) can cause the loss of turbulence and flow disturbances on spillway. For this purpose, initially geometry proposed for model for the discharge of spillway dam, Kamal-Saleh, 80, 100, and 120 (L/s) were surveyed. These discharges of flow were considered with regard to the flood return period, 5, 100 and 1000 years. Geometric properties of the conducting guidance wall are given in Table 1.Table 1 Characteristics and dimensions of the guidance walls tested

Full size table

Results of the CFD simulation for passing the flow rate 80 (L/s) are shown in Fig. 3. Figure 3 shows the secondary flow and vortex at the left guide wall.

figure 3
Fig. 3

For giving more information about flow pattern at the left and right guide wall, Fig. 4 shows the flow pattern at the right side guide wall and Fig. 5 shows the flow pattern at the left side guide wall.

figure 4
Fig. 4
figure 5
Fig. 5

With regard to Figs. 4 and 5 and observing the streamlines, at discharge equal to 80 (L/s), the right wall has suitable performance but the left wall has no suitable performance and the left wall of the geometric design creates a secondary and circular flow, and vortex motion in the beginning of the entrance of spillway that creates cross waves at the beginning of spillway. By increasing the flow rate (Q = 100 L/s), at the inlet spillway secondary flows and vortex were removed, but the streamline is severely distorted. Results of the guide wall performances at the Q = 100 (L/s) are shown in Fig. 6.

figure 6
Fig. 6

Also more information about the performance of each guide wall can be derived from Figs. 7 and 8. These figures uphold that the secondary and vortex flows were removed, but the streamlines were fully diverted specifically near the left side guide wall.

figure 7
Fig. 7
figure 8
Fig. 8

As mentioned in the past, these secondary and vortex flows and diversion in streamline cause nonuniformity and create cross wave through the spillway. Figure 9 shows the cross waves at the crest of the spillway.

figure 9
Fig. 9

The performance of guide walls at the Q = 120 (L/s) also was assessed. The result of simulation is shown in Fig. 10. Figures 11 and 12 show a more clear view of the streamlines near to right and left side guide wall, respectively. As seen in Fig. 12, the left side wall still causes vortex flow and creation of and diversion in streamline.

figure 10
Fig. 10
figure 11
Fig. 11
figure 12
Fig. 12

The results of the affected left side guide wall shape on the cross wave creation are shown in Fig. 13. As seen from Fig. 3, the left side guide wall also causes cross wave at the spillway crest.

figure 13
Fig. 13

As can be seen clearly in Figs. 9 and 13, by moving from the left side to the right side of the spillway, the cross waves and the nonuniformity in flow is removed. By reviewing Figs. 9 and 13, it is found that the right side guide wall removes the cross waves and nonuniformity. With this point as aim, a geometry similar to the right side guide wall was considered instead of the left side guide wall. The result of simulation for Q = 120 (L/s) is shown in Fig. 14. As seen from this figure, the proposed geometry for the left side wall has suitable performance smoothly passing the flow through the approach channel and spillway.

figure 14
Fig. 14

More information about the proposed shape for the left guide wall is shown in Fig. 15. As seen from this figure, this shape has suitable performance for removing the cross waves and vortex flows.

figure 15
Fig. 15

Figure 16 shows the cross section of flow at the crest of spillway. As seen in this figure, the proposed shape for the left side guide wall is suitable for removing the cross waves and secondary flows.

figure 16
Fig. 16

Conclusion

Analysis of behavior and hydraulic properties of flow over the spillway dam is a complicated task which is cost and time intensive. Several techniques suitable to the purposes of study have been undertaken in this research. Physical modeling, usage of expert experience, usage of mathematical models on simulation flow in one-dimensional, two-dimensional and three-dimensional techniques, are some of the techniques utilized to study this phenomenon. The results of the modeling show that the CFD technique is a suitable tool for simulating the flow pattern in the guide wall. Using this tools helps the designer for developing the optimal shape for hydraulic structure which the flow pattern through them are important.

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  1. Department of Water Engineering, Lorestan University, Khorram Abad, IranAbbas Parsaie, Amir Hamzeh Haghiabi & Amir Moradinejad

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Correspondence to Abbas Parsaie.

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Parsaie, A., Haghiabi, A.H. & Moradinejad, A. CFD modeling of flow pattern in spillwayโ€™s approach channel. Sustain. Water Resour. Manag. 1, 245โ€“251 (2015). https://doi.org/10.1007/s40899-015-0020-9

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  • Received28 April 2015
  • Accepted28 August 2015
  • Published15 September 2015
  • Issue DateSeptember 2015
  • DOIhttps://doi.org/10.1007/s40899-015-0020-9

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Keywords

  • Approach channel
  • Kamal-Saleh dam
  • Guide wall
  • Flow pattern
  • Numerical modeling
  • Flow 3D software
    Figure 3. FLOW-3D results for Strathcona Dam spillway with all gates fully open at an elevated reservoir level during passage of a large flood. Note the effects of poor approach conditions and pier overtopping at the leftmost bay.

    BC Hydro Assesses Spillway Hydraulics with FLOW-3D

    by Faizal Yusuf, M.A.Sc., P.Eng.
    Specialist Engineer in the Hydrotechnical Department at BC Hydro

    BC Hydro, a public electric utility in British Columbia, uses FLOW-3D to investigate complex hydraulics issues at several existing dams and to assist in the design and optimization of proposed facilities.

    Faizal Yusuf, M.A.Sc., P.Eng., Specialist Engineer in the Hydrotechnical department at BC Hydro, presents three case studies that highlight the application of FLOW-3D to different types of spillways and the importance of reliable prototype or physical hydraulic model data for numerical model calibration.

    W.A.C. Bennett Dam
    At W.A.C. Bennett Dam, differences in the spillway geometry between the physical hydraulic model from the 1960s and the prototype make it difficult to draw reliable conclusions on shock wave formation and chute capacity from physical model test results. The magnitude of shock waves in the concrete-lined spillway chute are strongly influenced by a 44% reduction in the chute width downstream of the three radial gates at the headworks, as well as the relative openings of the radial gates. The shock waves lead to locally higher water levels that have caused overtopping of the chute walls under certain historical operations.Prototype spill tests for discharges up to 2,865 m3/s were performed in 2012 to provide surveyed water surface profiles along chute walls, 3D laser scans of the water surface in the chute and video of flow patterns for FLOW-3D model calibration. Excellent agreement was obtained between the numerical model and field observations, particularly for the location and height of the first shock wave at the chute walls (Figure 1).

    W.A.C์—์„œ Bennett Dam, 1960๋…„๋Œ€์˜ ๋ฌผ๋ฆฌ์  ์ˆ˜๋ ฅํ•™ ๋ชจ๋ธ๊ณผ ํ”„๋กœํ† ํƒ€์ž… ์‚ฌ์ด์˜ ์—ฌ์ˆ˜๋กœ ํ˜•์ƒ์˜ ์ฐจ์ด๋กœ ์ธํ•ด ๋ฌผ๋ฆฌ์  ๋ชจ๋ธ ํ…Œ์ŠคํŠธ ๊ฒฐ๊ณผ์—์„œ ์ถฉ๊ฒฉํŒŒ ํ˜•์„ฑ ๋ฐ ์ŠˆํŠธ ์šฉ๋Ÿ‰์— ๋Œ€ํ•œ ์‹ ๋ขฐํ•  ์ˆ˜ ์žˆ๋Š” ๊ฒฐ๋ก ์„ ๋„์ถœํ•˜๊ธฐ ์–ด๋ ต์Šต๋‹ˆ๋‹ค. ์ฝ˜ํฌ๋ฆฌํŠธ ๋ผ์ด๋‹ ๋ฐฉ์ˆ˜๋กœ ๋‚™ํ•˜์‚ฐ์˜ ์ถฉ๊ฒฉํŒŒ ํฌ๊ธฐ๋Š” ๋ฐฉ์‚ฌํ˜• ๊ฒŒ์ดํŠธ์˜ ์ƒ๋Œ€์ ์ธ ๊ฐœ๊ตฌ๋ถ€๋ฟ๋งŒ ์•„๋‹ˆ๋ผ ํ—ค๋“œ์›Œํฌ์— ์žˆ๋Š” 3๊ฐœ์˜ ๋ฐฉ์‚ฌํ˜• ๊ฒŒ์ดํŠธ ํ•˜๋ฅ˜์˜ ์ŠˆํŠธ ํญ์ด 44% ๊ฐ์†Œํ•จ์— ๋”ฐ๋ผ ํฌ๊ฒŒ ์˜ํ–ฅ์„ ๋ฐ›์Šต๋‹ˆ๋‹ค. ์ถฉ๊ฒฉํŒŒ๋Š” ํŠน์ • ์—ญ์‚ฌ์  ์ž‘์—…์—์„œ ์ŠˆํŠธ ๋ฒฝ์˜ ๋ฒ”๋žŒ์„ ์•ผ๊ธฐํ•œ ๊ตญ๋ถ€์ ์œผ๋กœ ๋” ๋†’์€ ์ˆ˜์œ„๋กœ ์ด์–ด์ง‘๋‹ˆ๋‹ค. ์ตœ๋Œ€ 2,865m3/s์˜ ๋ฐฐ์ถœ์— ๋Œ€ํ•œ ํ”„๋กœํ† ํƒ€์ž… ์œ ์ถœ ํ…Œ์ŠคํŠธ๊ฐ€ 2012๋…„์— ์ˆ˜ํ–‰๋˜์–ด ์ŠˆํŠธ ๋ฒฝ์„ ๋”ฐ๋ผ ์กฐ์‚ฌ๋œ ์ˆ˜๋ฉด ํ”„๋กœํ•„, 3D ๋ ˆ์ด์ € ์Šค์บ”์„ ์ œ๊ณตํ–ˆ์Šต๋‹ˆ๋‹ค. FLOW-3D ๋ชจ๋ธ ๋ณด์ •์„ ์œ„ํ•œ ์ŠˆํŠธ์˜ ์ˆ˜๋ฉด ๋ฐ ํ๋ฆ„ ํŒจํ„ด ๋น„๋””์˜ค. ํŠนํžˆ ์ŠˆํŠธ ๋ฒฝ์—์„œ ์ฒซ ๋ฒˆ์งธ ์ถฉ๊ฒฉํŒŒ์˜ ์œ„์น˜์™€ ๋†’์ด์— ๋Œ€ํ•ด ์ˆ˜์น˜ ๋ชจ๋ธ๊ณผ ํ˜„์žฅ ๊ด€์ฐฐ ๊ฐ„์— ํƒ์›”ํ•œ ์ผ์น˜๊ฐ€ ์ด๋ฃจ์–ด์กŒ์Šต๋‹ˆ๋‹ค(๊ทธ๋ฆผ 1).
    Figure 1. Comparison between prototype observations and FLOW-3D for a spill discharge of 2,865 m^3/s at Bennett Dam spillway.
    Figure 1. Comparison between prototype observations and FLOW-3D for a spill discharge of 2,865 m^3/s at Bennett Dam spillway.

    The calibrated FLOW-3D model confirmed that the design flood could be safely passed without overtopping the spillway chute walls as long as all three radial gates are opened as prescribed in existing operating orders with the outer gates open more than the inner gate.

    The CFD model also provided insight into the concrete damage in the spillway chute. Cavitation indices computed from FLOW-3D simulation results were compared with empirical data from the USBR and found to be consistent with the historical performance of the spillway. The numerical analysis supported field inspections, which concluded that deterioration of the concrete conditions in the chute is likely not due to cavitation.

    Strathcona Dam
    FLOW-3D was used to investigate poor approach conditions and uncertainties with the rating curves for Strathcona Dam spillway, which includes three vertical lift gates on the right abutment of the dam. The rating curves for Strathcona spillway were developed from a combination of empirical adjustments and limited physical hydraulic model testing in a flume that did not include geometry of the piers and abutments.

    Numerical model testing and calibration was based on comparisons with prototype spill observations from 1982 when all three gates were fully open, resulting in a large depression in the water surface upstream of the leftmost bay (Figure 2). The approach flow to the leftmost bay is distorted by water flowing parallel to the dam axis and plunging over the concrete retaining wall adjacent to the upstream slope of the earthfill dam. The flow enters the other two bays much more smoothly. In addition to very similar flow patterns produced in the numerical model compared to the prototype, simulated water levels at the gate section matched 1982 field measurements to within 0.1 m.

    ๋ณด์ •๋œ FLOW-3D ๋ชจ๋ธ์€ ์™ธ๋ถ€ ๊ฒŒ์ดํŠธ๊ฐ€ ๋‚ด๋ถ€ ๊ฒŒ์ดํŠธ๋ณด๋‹ค ๋” ๋งŽ์ด ์—ด๋ ค ์žˆ๋Š” ๊ธฐ์กด ์šด์˜ ๋ช…๋ น์— ๊ทœ์ •๋œ ๋Œ€๋กœ 3๊ฐœ์˜ ๋ฐฉ์‚ฌํ˜• ๊ฒŒ์ดํŠธ๊ฐ€ ๋ชจ๋‘ ์—ด๋ฆฌ๋Š” ํ•œ ์—ฌ์ˆ˜๋กœ ๋‚™ํ•˜์‚ฐ ๋ฒฝ์„ ๋„˜์ง€ ์•Š๊ณ  ์„ค๊ณ„ ํ™์ˆ˜๋ฅผ ์•ˆ์ „ํ•˜๊ฒŒ ํ†ต๊ณผํ•  ์ˆ˜ ์žˆ์Œ์„ ํ™•์ธํ–ˆ์Šต๋‹ˆ๋‹ค.

    CFD ๋ชจ๋ธ์€ ๋ฐฉ์ˆ˜๋กœ ๋‚™ํ•˜์‚ฐ์˜ ์ฝ˜ํฌ๋ฆฌํŠธ ์†์ƒ์— ๋Œ€ํ•œ ํ†ต์ฐฐ๋ ฅ๋„ ์ œ๊ณตํ–ˆ์Šต๋‹ˆ๋‹ค. FLOW-3D ์‹œ๋ฎฌ๋ ˆ์ด์…˜ ๊ฒฐ๊ณผ์—์„œ ๊ณ„์‚ฐ๋œ ์บ๋น„ํ…Œ์ด์…˜ ์ง€์ˆ˜๋Š” USBR์˜ ๊ฒฝํ—˜์  ๋ฐ์ดํ„ฐ์™€ ๋น„๊ต๋˜์—ˆ์œผ๋ฉฐ ์—ฌ์ˆ˜๋กœ์˜ ์—ญ์‚ฌ์  ์„ฑ๋Šฅ๊ณผ ์ผ์น˜ํ•˜๋Š” ๊ฒƒ์œผ๋กœ ๋‚˜ํƒ€๋‚ฌ์Šต๋‹ˆ๋‹ค. ์ˆ˜์น˜ ๋ถ„์„์€ ํ˜„์žฅ ๊ฒ€์‚ฌ๋ฅผ ์ง€์›ํ–ˆ์œผ๋ฉฐ, ์ŠˆํŠธ์˜ ์ฝ˜ํฌ๋ฆฌํŠธ ์ƒํƒœ ์•…ํ™”๋Š” ์บ๋น„ํ…Œ์ด์…˜ ๋•Œ๋ฌธ์ด ์•„๋‹ ๊ฐ€๋Šฅ์„ฑ์ด ๋†’๋‹ค๊ณ  ๊ฒฐ๋ก ์ง€์—ˆ์Šต๋‹ˆ๋‹ค.

    Strathcona ๋Œ
    FLOW-3D๋Š” Strathcona Dam ์—ฌ์ˆ˜๋กœ์— ๋Œ€ํ•œ ๋“ฑ๊ธ‰ ๊ณก์„ ์„ ์‚ฌ์šฉํ•˜์—ฌ ์—ด์•…ํ•œ ์ ‘๊ทผ ์กฐ๊ฑด๊ณผ ๋ถˆํ™•์‹ค์„ฑ์„ ์กฐ์‚ฌํ•˜๋Š” ๋ฐ ์‚ฌ์šฉ๋˜์—ˆ์Šต๋‹ˆ๋‹ค. ์—ฌ๊ธฐ์—๋Š” ๋Œ์˜ ์˜ค๋ฅธ์ชฝ ์ ‘ํ•ฉ๋ถ€์— 3๊ฐœ์˜ ์ˆ˜์ง ๋ฆฌํ”„ํŠธ ๊ฒŒ์ดํŠธ๊ฐ€ ํฌํ•จ๋˜์–ด ์žˆ์Šต๋‹ˆ๋‹ค. Strathcona ์—ฌ์ˆ˜๋กœ์— ๋Œ€ํ•œ ๋“ฑ๊ธ‰ ๊ณก์„ ์€ ๊ฒฝํ—˜์  ์กฐ์ •๊ณผ ๊ต๊ฐ ๋ฐ ๊ต๋Œ€์˜ ํ˜•์ƒ์„ ํฌํ•จํ•˜์ง€ ์•Š๋Š” ์ˆ˜๋กœ์—์„œ ์ œํ•œ๋œ ๋ฌผ๋ฆฌ์  ์ˆ˜๋ฆฌ ๋ชจ๋ธ ํ…Œ์ŠคํŠธ์˜ ์กฐํ•ฉ์œผ๋กœ ๊ฐœ๋ฐœ๋˜์—ˆ์Šต๋‹ˆ๋‹ค.

    ์ˆ˜์น˜ ๋ชจ๋ธ ํ…Œ์ŠคํŠธ ๋ฐ ๋ณด์ •์€ ์„ธ ๊ฐœ์˜ ์ˆ˜๋ฌธ์ด ๋ชจ๋‘ ์™„์ „ํžˆ ๊ฐœ๋ฐฉ๋œ 1982๋…„์˜ ํ”„๋กœํ† ํƒ€์ž… ์œ ์ถœ ๊ด€์ธก๊ณผ์˜ ๋น„๊ต๋ฅผ ๊ธฐ๋ฐ˜์œผ๋กœ ํ–ˆ์œผ๋ฉฐ, ๊ทธ ๊ฒฐ๊ณผ ๊ฐ€์žฅ ์™ผ์ชฝ ๋งŒ์˜ ์ƒ๋ฅ˜ ์ˆ˜๋ฉด์— ํฐ ํ•จ๋ชฐ์ด ๋ฐœ์ƒํ–ˆ์Šต๋‹ˆ๋‹ค(๊ทธ๋ฆผ 2). ์ตœ์ขŒ๋‹จ ๋งŒ์œผ๋กœ์˜ ์ ‘๊ทผ ํ๋ฆ„์€ ๋Œ ์ถ•๊ณผ ํ‰ํ–‰ํ•˜๊ฒŒ ํ๋ฅด๋Š” ๋ฌผ๊ณผ ํ™์ฑ„์›€๋Œ์˜ ์ƒ๋ฅ˜ ๊ฒฝ์‚ฌ๋ฉด์— ์ธ์ ‘ํ•œ ์ฝ˜ํฌ๋ฆฌํŠธ ์˜น๋ฒฝ ์œ„๋กœ ๋–จ์–ด์ง€๋Š” ๋ฌผ์— ์˜ํ•ด ์™œ๊ณก๋ฉ๋‹ˆ๋‹ค. ํ๋ฆ„์€ ํ›จ์”ฌ ๋” ์›ํ™œํ•˜๊ฒŒ ๋‹ค๋ฅธ ๋‘ ๋ฒ ์ด๋กœ ๋“ค์–ด๊ฐ‘๋‹ˆ๋‹ค. ํ”„๋กœํ† ํƒ€์ž…๊ณผ ๋น„๊ตํ•˜์—ฌ ์ˆ˜์น˜ ๋ชจ๋ธ์—์„œ ์ƒ์„ฑ๋œ ๋งค์šฐ ์œ ์‚ฌํ•œ ํ๋ฆ„ ํŒจํ„ด ์™ธ์—๋„ ๊ฒŒ์ดํŠธ ์„น์…˜์—์„œ ์‹œ๋ฎฌ๋ ˆ์ด์…˜๋œ ์ˆ˜์œ„๋Š” 1982๋…„ ํ˜„์žฅ ์ธก์ •๊ณผ 0.1m ์ด๋‚ด๋กœ ์ผ์น˜ํ–ˆ์Šต๋‹ˆ๋‹ค.

    Figure 2. Prototype observations and FLOW-3D results for a Strathcona Dam spill in 1982 with all three gates fully open.
    Figure 2. Prototype observations and FLOW-3D results for a Strathcona Dam spill in 1982 with all three gates fully open.

    The calibrated CFD model produces discharges within 5% of the spillway rating curve for the reservoirโ€™s normal operating range with all gates fully open. However, at higher reservoir levels, which may occur during passage of large floods (as shown in Figure 3), the difference between simulated discharges and the rating curves are greater than 10% as the physical model testing with simplified geometry and empirical corrections did not adequately represent the complex approach flow patterns. The FLOW-3D model provided further insight into the accuracy of rating curves for individual bays, gated conditions and the transition between orifice and free surface flow.

    ๋ณด์ •๋œ CFD ๋ชจ๋ธ์€ ๋ชจ๋“  ๊ฒŒ์ดํŠธ๊ฐ€ ์™„์ „ํžˆ ์—ด๋ฆฐ ์ƒํƒœ์—์„œ ์ €์ˆ˜์ง€์˜ ์ •์ƒ ์ž‘๋™ ๋ฒ”์œ„์— ๋Œ€ํ•œ ์—ฌ์ˆ˜๋กœ ๋“ฑ๊ธ‰ ๊ณก์„ ์˜ 5% ์ด๋‚ด์—์„œ ๋ฐฐ์ถœ์„ ์ƒ์„ฑํ•ฉ๋‹ˆ๋‹ค. ๊ทธ๋Ÿฌ๋‚˜ ๋Œ€๊ทœ๋ชจ ํ™์ˆ˜๊ฐ€ ํ†ต๊ณผํ•˜๋Š” ๋™์•ˆ ๋ฐœ์ƒํ•  ์ˆ˜ ์žˆ๋Š” ๋” ๋†’์€ ์ €์ˆ˜์ง€ ์ˆ˜์œ„์—์„œ๋Š”(๊ทธ๋ฆผ 3 ์ฐธ์กฐ) ๋‹จ์ˆœํ™”๋œ ๊ธฐํ•˜ํ•™๊ณผ ๊ฒฝํ—˜์  ์ˆ˜์ •์„ ์‚ฌ์šฉํ•œ ๋ฌผ๋ฆฌ์  ๋ชจ๋ธ ํ…Œ์ŠคํŠธ๊ฐ€ ๊ทธ๋ ‡์ง€ ์•Š์•˜๊ธฐ ๋•Œ๋ฌธ์— ๋ชจ์˜ ๋ฐฐ์ถœ๊ณผ ๋“ฑ๊ธ‰ ๊ณก์„  ๊ฐ„์˜ ์ฐจ์ด๋Š” 10% ์ด์ƒ์ž…๋‹ˆ๋‹ค. ๋ณต์žกํ•œ ์ ‘๊ทผ ํ๋ฆ„ ํŒจํ„ด์„ ์ ์ ˆํ•˜๊ฒŒ ํ‘œํ˜„ํ•ฉ๋‹ˆ๋‹ค. FLOW-3D ๋ชจ๋ธ์€ ๊ฐœ๋ณ„ ๋ฒ ์ด, ๊ฒŒ์ดํŠธ ์กฐ๊ฑด ๋ฐ ์˜ค๋ฆฌํ”ผ์Šค์™€ ์ž์œ  ํ‘œ๋ฉด ํ๋ฆ„ ์‚ฌ์ด์˜ ์ „ํ™˜์— ๋Œ€ํ•œ ๋“ฑ๊ธ‰ ๊ณก์„ ์˜ ์ •ํ™•๋„์— ๋Œ€ํ•œ ์ถ”๊ฐ€ ํ†ต์ฐฐ๋ ฅ์„ ์ œ๊ณตํ–ˆ์Šต๋‹ˆ๋‹ค.

    Figure 3. FLOW-3D results for Strathcona Dam spillway with all gates fully open at an elevated reservoir level during passage of a large flood. Note the effects of poor approach conditions and pier overtopping at the leftmost bay.
    Figure 3. FLOW-3D results for Strathcona Dam spillway with all gates fully open at an elevated reservoir level during passage of a large flood. Note the effects of poor approach conditions and pier overtopping at the leftmost bay.

    John Hart Dam
    The John Hart concrete dam will be modified to include a new free crest spillway to be situated between an existing gated spillway and a low level outlet structure that is currently under construction. Significant improvements in the design of the proposed spillway were made through a systematic optimization process using FLOW-3D.

    The preliminary design of the free crest spillway was based on engineering hydraulic design guides. Concrete apron blocks are intended to protect the rock at the toe of the dam. A new right training wall will guide the flow from the new spillway towards the tailrace pool and protect the low level outlet structure from spillway discharges.

    FLOW-3D model results for the initial and optimized design of the new spillway are shown in Figure 4. CFD analysis led to a 10% increase in discharge capacity, significant decrease in roadway impingement above the spillway crest and improved flow patterns including up to a 5 m reduction in water levels along the proposed right wall. Physical hydraulic model testing will be used to confirm the proposed design.

    ์กด ํ•˜ํŠธ ๋Œ
    John Hart ์ฝ˜ํฌ๋ฆฌํŠธ ๋Œ์€ ํ˜„์žฌ ๊ฑด์„ค ์ค‘์ธ ๊ธฐ์กด ๋ฐฐ์ˆ˜๋กœ์™€ ์ €์ธต ๋ฐฐ์ˆ˜๋กœ ์‚ฌ์ด์— ์œ„์น˜ํ•  ์ƒˆ๋กœ์šด ์ž์œ  ๋งˆ๋ฃจ ๋ฐฐ์ˆ˜๋กœ๋ฅผ ํฌํ•จํ•˜๋„๋ก ์ˆ˜์ •๋  ๊ฒƒ์ž…๋‹ˆ๋‹ค. FLOW-3D๋ฅผ ์‚ฌ์šฉํ•œ ์ฒด๊ณ„์ ์ธ ์ตœ์ ํ™” ํ”„๋กœ์„ธ์Šค๋ฅผ ํ†ตํ•ด ์ œ์•ˆ๋œ ์—ฌ์ˆ˜๋กœ ์„ค๊ณ„์˜ ์ƒ๋‹นํ•œ ๊ฐœ์„ ์ด ์ด๋ฃจ์–ด์กŒ์Šต๋‹ˆ๋‹ค.

    ์ž์œ  ๋งˆ๋ฃจ ์—ฌ์ˆ˜๋กœ์˜ ์˜ˆ๋น„ ์„ค๊ณ„๋Š” ์—”์ง€๋‹ˆ์–ด๋ง ์ˆ˜๋ ฅํ•™ ์„ค๊ณ„ ๊ฐ€์ด๋“œ๋ฅผ ๊ธฐ๋ฐ˜์œผ๋กœ ํ–ˆ์Šต๋‹ˆ๋‹ค. ์ฝ˜ํฌ๋ฆฌํŠธ ์•ž์น˜๋งˆ ๋ธ”๋ก์€ ๋Œ ์„ ๋‹จ๋ถ€์˜ ์•”์„์„ ๋ณดํ˜ธํ•˜๊ธฐ ์œ„ํ•œ ๊ฒƒ์ž…๋‹ˆ๋‹ค. ์ƒˆ๋กœ์šด ์˜ค๋ฅธ์ชฝ ํ›ˆ๋ จ ๋ฒฝ์€ ์ƒˆ ์—ฌ์ˆ˜๋กœ์—์„œ ํ…Œ์ผ๋ ˆ์ด์Šค ํ’€๋กœ ํ๋ฆ„์„ ์•ˆ๋‚ดํ•˜๊ณ  ์—ฌ์ˆ˜๋กœ ๋ฐฐ์ถœ๋กœ๋ถ€ํ„ฐ ๋‚ฎ์€ ์ˆ˜์ค€์˜ ๋ฐฐ์ถœ๊ตฌ ๊ตฌ์กฐ๋ฅผ ๋ณดํ˜ธํ•ฉ๋‹ˆ๋‹ค.

    ์ƒˆ ์—ฌ์ˆ˜๋กœ์˜ ์ดˆ๊ธฐ ๋ฐ ์ตœ์ ํ™”๋œ ์„ค๊ณ„์— ๋Œ€ํ•œ FLOW-3D ๋ชจ๋ธ ๊ฒฐ๊ณผ๋Š” ๊ทธ๋ฆผ 4์— ๋‚˜์™€ ์žˆ์Šต๋‹ˆ๋‹ค. CFD ๋ถ„์„์„ ํ†ตํ•ด ๋ฐฉ๋ฅ˜ ์šฉ๋Ÿ‰์ด 10% ์ฆ๊ฐ€ํ•˜๊ณ  ์—ฌ์ˆ˜๋กœ ๋งˆ๋ฃจ ์œ„์˜ ๋„๋กœ ์ถฉ๋Œ์ด ํฌ๊ฒŒ ๊ฐ์†Œํ–ˆ์œผ๋ฉฐ ์ตœ๋Œ€ ์ œ์•ˆ๋œ ์˜ค๋ฅธ์ชฝ ๋ฒฝ์„ ๋”ฐ๋ผ ์ˆ˜์œ„๊ฐ€ 5m ๊ฐ์†Œํ•ฉ๋‹ˆ๋‹ค. ์ œ์•ˆ๋œ ์„ค๊ณ„๋ฅผ ํ™•์ธํ•˜๊ธฐ ์œ„ํ•ด ๋ฌผ๋ฆฌ์  ์ˆ˜์•• ๋ชจ๋ธ ํ…Œ์ŠคํŠธ๊ฐ€ ์‚ฌ์šฉ๋ฉ๋‹ˆ๋‹ค.

    Figure 4. FLOW-3D model results for the preliminary and optimized layout of the proposed spillway at John Hart Dam.
    Figure 4. FLOW-3D model results for the preliminary and optimized layout of the proposed spillway at John Hart Dam.

    Conclusion

    BC Hydro has been using FLOW-3D to investigate a wide range of challenging hydraulics problems for different types of spillways and water conveyance structures leading to a greatly improved understanding of flow patterns and performance. Prototype data and reliable physical hydraulic model testing are used whenever possible to improve confidence in the numerical model results.

    ๋‹ค์–‘ํ•œ ์œ ํ˜•์˜ ์—ฌ์ˆ˜๋กœ ๋ฐ ๋ฌผ ์ˆ˜์†ก ๊ตฌ์กฐ๋กœ ์ธํ•ด ํ๋ฆ„ ํŒจํ„ด ๋ฐ ์„ฑ๋Šฅ์— ๋Œ€ํ•œ ์ดํ•ด๊ฐ€ ํฌ๊ฒŒ ํ–ฅ์ƒ๋˜์—ˆ์Šต๋‹ˆ๋‹ค. ํ”„๋กœํ† ํƒ€์ž… ๋ฐ์ดํ„ฐ์™€ ์‹ ๋ขฐํ•  ์ˆ˜ ์žˆ๋Š” ๋ฌผ๋ฆฌ์  ์œ ์•• ๋ชจ๋ธ ํ…Œ์ŠคํŠธ๋Š” ์ˆ˜์น˜ ๋ชจ๋ธ ๊ฒฐ๊ณผ์˜ ์‹ ๋ขฐ๋„๋ฅผ ํ–ฅ์ƒ์‹œํ‚ค๊ธฐ ์œ„ํ•ด ๊ฐ€๋Šฅํ•  ๋•Œ๋งˆ๋‹ค ์‚ฌ์šฉ๋ฉ๋‹ˆ๋‹ค.

    About Flow Science, Inc.
    Based in Santa Fe, New Mexico USA, Flow Science was founded in 1980 by Dr. C. W. (Tony) Hirt, who was one of the principals in pioneering the โ€œVolume-of-Fluidโ€ or VOF method while working at the Los Alamos National Lab. FLOW-3D is a direct descendant of this work, and in the subsequent years, we have increased its sophistication with TruVOF, boasting pioneering improvements in the speed and accuracy of tracking distinct liquid/gas interfaces. Today, Flow Science products offer complete multiphysics simulation with diverse modeling capabilities including fluid-structure interaction, 6-DoF moving objects, and multiphase flows. From inception, our vision has been to provide our customers with excellence in flow modeling software and services.

    Figure 10. Flow distribution at the approach channel in PMF based on revised plan design. A. Hydarulic model test; B. Numerical simulation; C. Section view.

    Improvement of hydraulic stability for spillway using CFD model

    Hydraulic model test was used to analyze the rapidly varied flow on the spillway. But, it has some shortcomings such as error of scale effect and expensive costs. Recently, through the development of three dimensional computational fluid dynamics (CFD), rapidly varied flow and turbulence can be simulated. In this study, the applicability of CFD model to simulate flow on the spillway was reviewed. The Karian dam in Indonesia was selected as the study area. The FLOW-3d model, which is well known to simulate a flow having a free surface, was used to analyze flow. The flow stability in approach channel was investigated with the initial plan design, and the results showed that the flow in approach channel is unstable in the initial plan design. To improve flow stability in the spillway, therefore, the revised plan design was formulated. The appropriateness of the revised design was examined by a numerical modeling. The results showed that the flow in spillway is stable in the revised design.

    ์—ฌ์ˆ˜๋กœ์˜ ๊ธ‰๊ฒฉํ•˜๊ฒŒ ๋ณ€ํ™”ํ•˜๋Š” ํ๋ฆ„์„ ๋ถ„์„ํ•˜๊ธฐ ์œ„ํ•ด ์ˆ˜๋ฆฌํ•™์  ๋ชจ๋ธ ํ…Œ์ŠคํŠธ๋ฅผ ์‚ฌ์šฉํ–ˆ์Šต๋‹ˆ๋‹ค. ๊ทธ๋Ÿฌ๋‚˜ ์Šค์ผ€์ผ ํšจ๊ณผ์˜ ์˜ค์ฐจ์™€ ๊ณ ๊ฐ€์˜ ๋น„์šฉ ๋“ฑ์˜ ๋‹จ์ ์ด ์žˆ๋‹ค. ์ตœ๊ทผ์—๋Š” 3์ฐจ์› ์ „์‚ฐ์œ ์ฒด์—ญํ•™(CFD)์˜ ๋ฐœ๋‹ฌ๋กœ ๊ธ‰๋ณ€ํ•˜๋Š” ์œ ๋™๊ณผ ๋‚œ๋ฅ˜๋ฅผ ๋ชจ์‚ฌํ•  ์ˆ˜ ์žˆ๋‹ค. ๋ณธ ์—ฐ๊ตฌ์—์„œ๋Š” ์—ฌ์ˆ˜๋กœ์˜ ํ๋ฆ„์„ ์‹œ๋ฎฌ๋ ˆ์ด์…˜ํ•˜๊ธฐ ์œ„ํ•œ CFD ๋ชจ๋ธ์˜ ์ ์šฉ ๊ฐ€๋Šฅ์„ฑ์„ ๊ฒ€ํ† ํ–ˆ์Šต๋‹ˆ๋‹ค. ์ธ๋„๋„ค์‹œ์•„์˜ Karian ๋Œ์ด ์—ฐ๊ตฌ ์ง€์—ญ์œผ๋กœ ์„ ์ •๋˜์—ˆ์Šต๋‹ˆ๋‹ค. ์ž์œ ํ‘œ๋ฉด์„ ๊ฐ–๋Š” ์œ ๋™์„ ๋ชจ์˜ํ•˜๋Š” ๊ฒƒ์œผ๋กœ ์ž˜ ์•Œ๋ ค์ง„ FLOW-3d ๋ชจ๋ธ์„ ์œ ๋™ํ•ด์„์— ์‚ฌ์šฉํ•˜์˜€๋‹ค. ์ ‘๊ทผ์ˆ˜๋กœ์˜ ํ๋ฆ„ ์•ˆ์ •์„ฑ์€ ์ดˆ๊ธฐ ๊ณ„ํš์„ค๊ณ„์™€ ํ•จ๊ป˜ ์กฐ์‚ฌํ•œ ๊ฒฐ๊ณผ ์ดˆ๊ธฐ ๊ณ„ํš์„ค๊ณ„์—์„œ ์ ‘๊ทผ์ˆ˜๋กœ์˜ ํ๋ฆ„์ด ๋ถˆ์•ˆ์ •ํ•œ ๊ฒƒ์œผ๋กœ ๋‚˜ํƒ€๋‚ฌ๋‹ค. ๋”ฐ๋ผ์„œ ๋ฐฉ์ˆ˜๋กœ์˜ ํ๋ฆ„ ์•ˆ์ •์„ฑ์„ ํ–ฅ์ƒ์‹œํ‚ค๊ธฐ ์œ„ํ•ด ์ˆ˜์ •๋œ ๊ณ„ํš ์„ค๊ณ„๊ฐ€ ๊ณต์‹ํ™”๋˜์—ˆ์Šต๋‹ˆ๋‹ค. ์ˆ˜์ •๋œ ์„ค๊ณ„์˜ ์ ํ•ฉ์„ฑ์„ ์ˆ˜์น˜๋ชจ๋ธ๋ง์„ ํ†ตํ•ด ๊ฒ€ํ† ํ•˜์˜€๋‹ค. ๊ฒฐ๊ณผ๋Š” ์ˆ˜์ •๋œ ์„ค๊ณ„์—์„œ ์—ฌ์ˆ˜๋กœ์˜ ํ๋ฆ„์ด ์•ˆ์ •์ ์ด๋ผ๋Š” ๊ฒƒ์„ ๋ณด์—ฌ์ฃผ์—ˆ์Šต๋‹ˆ๋‹ค.

    Key words

    Spillway, FLOW-3D, approach channel, flow stability, numerical modeling, hydraulic model test.

    Figure 6. Two dimensional flow velocity distribution at the
approach channel (Flow velocity distribution at depth EL. 68.12 m).
    Figure 6. Two dimensional flow velocity distribution at the approach channel (Flow velocity distribution at depth EL. 68.12 m).
    Figure 7. Flow distribution at the approach channel in PMF.
A. Hydraulic model test; B. Numerial simulatio
C. Cross section view.
    Figure 7. Flow distribution at the approach channel in PMF. A. Hydraulic model test; B. Numerial simulatio C. Cross section view.
    Figure 8. Revised approach channel section.
A. Initial plan design; B. Revised plan design.
    Figure 8. Revised approach channel section. A. Initial plan design; B. Revised plan design.
    Figure 9. Two dimensional flow velocity distribution at the approach channel
based on revised plan design (Flow velocity distribution at depth EL. 68.12 m).
    Figure 9. Two dimensional flow velocity distribution at the approach channel based on revised plan design (Flow velocity distribution at depth EL. 68.12 m).
    Figure 10. Flow distribution at the approach channel in PMF based on revised plan design.
A. Hydarulic model test; B. Numerical simulation; C. Section view.
    Figure 10. Flow distribution at the approach channel in PMF based on revised plan design. A. Hydarulic model test; B. Numerical simulation; C. Section view.

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    Numerical analysis of energy dissipator options using computational fluid dynamics modeling โ€” a case study of Mirani Dam

    ์ „์‚ฐ ์œ ์ฒด ์—ญํ•™ ๋ชจ๋ธ๋ง์„ ์‚ฌ์šฉํ•œ ์—๋„ˆ์ง€ ์†Œ์‚ฐ์ž ์˜ต์…˜์˜ ์ˆ˜์น˜์  ํ•ด์„ โ€” Mirani ๋Œ์˜ ์‚ฌ๋ก€ ์—ฐ๊ตฌ

    Arabian Journal of Geosciences volume 15, Article number: 1614 (2022) Cite this article

    Abstract

    ์ด ์—ฐ๊ตฌ์—์„œ FLOW 3D ์ „์‚ฐ ์œ ์ฒด ์—ญํ•™(CFD) ์†Œํ”„ํŠธ์›จ์–ด๋ฅผ ์‚ฌ์šฉํ•˜์—ฌ ํŒŒํ‚ค์Šคํƒ„ Mirani ๋Œ ๋ฐฉ์ˆ˜๋กœ์— ๋Œ€ํ•œ ์—๋„ˆ์ง€ ์†Œ์‚ฐ ์˜ต์…˜์œผ๋กœ ๋ฏธ๊ตญ ๋งค๋ฆฝ์ง€(USBR) ์œ ํ˜• II ๋ฐ USBR ์œ ํ˜• III ์œ ์—ญ์˜ ์„ฑ๋Šฅ์„ ์ถ”์ •ํ–ˆ์Šต๋‹ˆ๋‹ค.ย 3D Reynolds ํ‰๊ท  Navier-Stokes ๋ฐฉ์ •์‹์ด ํ•ด๊ฒฐ๋˜์—ˆ์œผ๋ฉฐ, ์—ฌ๊ธฐ์—๋Š” ์—ฌ์ˆ˜๋กœ ์œ„์˜ ์ž์œ  ํ‘œ๋ฉด ํ๋ฆ„์„ ์บก์ฒ˜ํ•˜๊ธฐ ์œ„ํ•ด ๊ณต๊ธฐ ์œ ์ž…, ๋ฐ€๋„ ํ‰๊ฐ€ ๋ฐ ๋“œ๋ฆฌํ”„ํŠธ-ํ”Œ๋Ÿญ์Šค์— ๋Œ€ํ•œ ํ•˜์œ„ ๊ทธ๋ฆฌ๋“œ ๋ชจ๋ธ์ด ํฌํ•จ๋˜์—ˆ์Šต๋‹ˆ๋‹ค.ย ๋ณธ ์—ฐ๊ตฌ์—์„œ๋Š” 5๊ฐ€์ง€ ๋ชจ๋ธ์„ ๊ณ ๋ คํ•˜์˜€๋‹ค.ย ์ฒซ ๋ฒˆ์งธ ๋ชจ๋ธ์—๋Š” ๊ธธ์ด๊ฐ€ 39.5m์ธ USBR ์œ ํ˜• II ์ •์ˆ˜๊ธฐ๊ฐ€ ์žˆ์Šต๋‹ˆ๋‹ค.ย ๋‘ ๋ฒˆ์งธ ๋ชจ๋ธ์—๋Š” ๊ธธ์ด๊ฐ€ 44.2m์ธ USBR ์œ ํ˜• II ์ •์ˆ˜๊ธฐ๊ฐ€ ์žˆ์Šต๋‹ˆ๋‹ค.ย 3๋ฒˆ์งธ์™€ 4ย ๋ฒˆ์งธ๋ชจ๋ธ์—๋Š” ๊ธธ์ด๊ฐ€ ๊ฐ๊ฐ 48.8m์ธ USBR ์œ ํ˜• II ์ •์ˆ˜์กฐ์™€ 39.5m์˜ USBR ์œ ํ˜• III ์ •์ˆ˜์กฐ๊ฐ€ ์žˆ์Šต๋‹ˆ๋‹ค.ย ๋‹ค์„ฏ ๋ฒˆ์งธ ๋ชจ๋ธ์€ ๋„ค ๋ฒˆ์งธ ๋ชจ๋ธ๊ณผ ๋™์ผํ•˜์ง€๋งŒ ๋งˆ์ฐฐ ๋ฐ ์ŠˆํŠธ ๋ธ”๋ก ๋†’์ด๊ฐ€ 0.3m ์ฆ๊ฐ€ํ–ˆ์Šต๋‹ˆ๋‹ค.ย ์ตœ์ƒ์˜ FLOW 3D ๋ชจ๋ธ ์กฐ๊ฑด์„ ์„ค์ •ํ•˜๊ธฐ ์œ„ํ•ด ๋ฉ”์‰ฌ ๋ฏผ๊ฐ๋„ ๋ถ„์„์„ ์ˆ˜ํ–‰ํ–ˆ์œผ๋ฉฐ ๋ฉ”์‰ฌ ํฌ๊ธฐ 0.9m์—์„œ ์ตœ์†Œ ์˜ค์ฐจ๋ฅผ ์‚ฐ์ถœํ–ˆ์Šต๋‹ˆ๋‹ค.ย ์„ธ ๊ฐ€์ง€ ๊ฒฝ๊ณ„ ์กฐ๊ฑด ์„ธํŠธ๊ฐ€ ํ…Œ์ŠคํŠธ๋˜์—ˆ์œผ๋ฉฐ ์ตœ์†Œ ์˜ค๋ฅ˜๋ฅผ ์ œ๊ณตํ•˜๋Š” ์„ธํŠธ๊ฐ€ ์‚ฌ์šฉ๋˜์—ˆ์Šต๋‹ˆ๋‹ค.ย ์ˆ˜์น˜์  ๊ฒ€์ฆ์€ USBR ์œ ํ˜• II( Lย = 48.8m), USBR ์œ ํ˜• III(ย Lย = 35.5m) ๋ฐ USBR ์œ ํ˜• III ์˜ ๋ฌผ๋ฆฌ์  ๋ชจ๋ธ ์—๋„ˆ์ง€ ์†Œ์‚ฐ์„ย 0.3m ๋ธ”๋ก ๋‹จ์œ„๋กœ ๋น„๊ตํ•˜์—ฌ ์ˆ˜ํ–‰๋˜์—ˆ์Šต๋‹ˆ๋‹ค(ย L= 35.5m).ย ํ†ต๊ณ„ ๋ถ„์„ ๊ฒฐ๊ณผ ํ‰๊ท  ์˜ค์ฐจ๋Š” 2.5%, RMSE(์ œ๊ณฑ ํ‰๊ท  ์ œ๊ณฑ๊ทผ ์˜ค์ฐจ) ์ง€์ˆ˜๋Š” 3% ๋ฏธ๋งŒ์ด์—ˆ์Šต๋‹ˆ๋‹ค.ย ์ˆ˜๋ฆฌํ•™์  ๋ฐ ๊ฒฝ์ œ์„ฑ ๋ถ„์„์„ ๋ฐ”ํƒ•์œผ๋กœ 4ย ๋ฒˆ์งธย ๋ชจ๋ธ์ด ์ตœ์ ํ™”๋œ ์—๋„ˆ์ง€ ์†Œ์‚ฐ๊ธฐ๋กœ ๋ฐํ˜€์กŒ์Šต๋‹ˆ๋‹ค.ย ํก์ˆ˜๋œ ์—๋„ˆ์ง€ ๋ฐฑ๋ถ„์œจ ์ธก๋ฉด์—์„œ ๋ฌผ๋ฆฌ์  ๋ชจ๋ธ๊ณผ ์ˆ˜์น˜์  ๋ชจ๋ธ ๊ฐ„์˜ ์ตœ๋Œ€ ์ฐจ์ด๋Š” 5% ๋ฏธ๋งŒ์ธ ๊ฒƒ์œผ๋กœ ๋‚˜ํƒ€๋‚ฌ์Šต๋‹ˆ๋‹ค.

    In this study, the FLOW 3D computational fluid dynamics (CFD) software was used to estimate the performance of the United States Bureau of Reclamation (USBR) type II and USBR type III stilling basins as energy dissipation options for the Mirani Dam spillway, Pakistan. The 3D Reynolds-averaged Navierโ€“Stokes equations were solved, which included sub-grid models for air entrainment, density evaluation, and driftโ€“flux, to capture free-surface flow over the spillway. Five models were considered in this research. The first model has a USBR type II stilling basin with a length of 39.5 m. The second model has a USBR type II stilling basin with a length of 44.2 m. The 3rd and 4thย models have a USBR type II stilling basin with a length of 48.8 m and a 39.5 m USBR type III stilling basin, respectively. The fifth model is identical to the fourth, but the friction and chute block heights have been increased by 0.3 m. To set up the best FLOW 3D model conditions, mesh sensitivity analysis was performed, which yielded a minimum error at a mesh size of 0.9 m. Three sets of boundary conditions were tested and the set that gave the minimum error was employed. Numerical validation was done by comparing the physical model energy dissipation of USBR type II (Lย = 48.8 m), USBR type III (Lย =35.5 m), and USBR type III with 0.3-m increments in blocks (Lย = 35.5 m). The statistical analysis gave an average error of 2.5% and a RMSE (root mean square error) index of less than 3%. Based on hydraulics and economic analysis, the 4thย model was found to be an optimized energy dissipator. The maximum difference between the physical and numerical models in terms of percentage energy absorbed was found to be less than 5%.

    Keywords

    • Numerical modeling
    • Spillway
    • Hydraulic jump
    • Energy dissipation
    • FLOW 3D

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    Effect of tailwater depth on non-cohesive earth dam failure due to overtopping

    Effect of tailwater depth on non-cohesive earth dam failure due to overtopping

    ๋ฒ”๋žŒ์œผ๋กœ ์ธํ•œ ๋น„์ ์ฐฉ์„ฑ ํ™๋Œ ๋ถ•๊ดด์— ๋Œ€ํ•œ ํ…Œ์ผ์›Œํ„ฐ ๊นŠ์ด์˜ ์˜ํ–ฅ

    ShaimaaAmanaMohamedAbdelrazek RezkbRabieaNasrc

    Abstract

    ๋ณธ ์—ฐ๊ตฌ์—์„œ๋Š” ๋ฒ”๋žŒ์œผ๋กœ ์ธํ•œ ํ† ์‚ฌ๋Œ ๋ถ•๊ดด์— ๋Œ€ํ•œ ํ…Œ์ผ์›Œํ„ฐ ๊นŠ์ด์˜ ์˜ํ–ฅ์„ ์‹คํ—˜์ ์œผ๋กœ ์กฐ์‚ฌํ•˜์˜€๋‹ค. ํ…Œ์ผ์›Œํ„ฐ ๊นŠ์ด์˜ ๋„ค ๊ฐ€์ง€ ๋‹ค๋ฅธ ๊ฐ’์„ ๊ฒ€์‚ฌํ•ฉ๋‹ˆ๋‹ค. ๊ฐ ์‹คํ—˜์— ๋Œ€ํ•ด ๋Œ ์ˆ˜์‹ฌ ์ธก๋Ÿ‰ ํ”„๋กœํŒŒ์ผ์˜ ์ง„ํ™”, ๊ณ ์žฅ ๊ธฐ๊ฐ„, ์นจ์‹ ์ฒด์  ๋ฐ ์œ ์ถœ ์ˆ˜์œ„๊ณก์„ ์„ ๊ด€์ฐฐํ•˜๊ณ  ๊ธฐ๋กํ•ฉ๋‹ˆ๋‹ค.

    ๊ฒฐ๊ณผ๋Š” tailwater ๊นŠ์ด๋ฅผ ๋Š˜๋ฆฌ๋ฉด ๊ณ ์žฅ ์‹œ๊ฐ„์ด ์ตœ๋Œ€ 57% ๊ฐ์†Œํ•˜๊ณ  ์ƒ๋Œ€์ ์œผ๋กœ ์นจ์‹๋œ ๋งˆ๋ฃจ ๋†’์ด๊ฐ€ ์ตœ๋Œ€ 77.6% ๊ฐ์†Œํ•œ๋‹ค๋Š” ๊ฒƒ์„ ๋ณด์—ฌ์ค๋‹ˆ๋‹ค. ๋˜ํ•œ ์ƒ๋Œ€ ๋ฐฐ์ˆ˜ ๊นŠ์ด๊ฐ€ 3, 4, 5์ธ ๊ฒฝ์šฐ ๋ˆ„์  ์นจ์‹ ์ฒด์ ์˜ ๊ฐ์†Œ๋Š” ๊ฐ๊ฐ 23, 36.5 ๋ฐ 75%์ธ ๋ฐ˜๋ฉด ์ตœ๋Œ€ ์œ ์ถœ๋Ÿ‰์˜ ๊ฐ์†Œ๋Š” ๊ฐ๊ฐ 7, 14 ๋ฐ 17.35%์ž…๋‹ˆ๋‹ค.

    ์‹คํ—˜ ๊ฒฐ๊ณผ๋Š” ์นจ์‹ ๊ณผ์ •์„ ๋ณต์ œํ•  ๋•Œ Flow 3D ์†Œํ”„ํŠธ์›จ์–ด์˜ ์„ฑ๋Šฅ์„ ํ‰๊ฐ€ํ•˜๋Š” ๋ฐ ํ™œ์šฉ๋ฉ๋‹ˆ๋‹ค. ์ˆ˜์น˜ ๋ชจ๋ธ์€ ๋น„์‘์ง‘์„ฑ ํ™๋Œ์˜ ์นจ์‹ ๊ณผ์ •์„ ์„ฑ๊ณต์ ์œผ๋กœ ์‹œ๋ฎฌ๋ ˆ์ด์…˜ํ•ฉ๋‹ˆ๋‹ค.

    The influence of tailwater depth on earth dam failure due to overtopping is investigated experimentally in this work. Four different values of tailwater depths are examined. For each experiment, the evolution of the dam bathymetry profile, the duration of failure, the eroded volume, and the outflow hydrograph are observed and recorded. The results reveal that increasing the tailwater depth reduces the time of failure by up to 57% and decreases the relative eroded crest height by up to 77.6%. In addition, for relative tailwater depths equal to 3, 4, and 5, the reduction in the cumulative eroded volume is 23, 36.5, and 75%, while the reduction in peak discharge is 7, 14, and 17.35%, respectively. The experimental results are utilized to evaluate the performance of the Flow 3D software in replicating the erosion process. The numerical model successfully simulates the erosion process of non-cohesive earth dams.

    Keywords

    Earth dam, Eroded volume, Flow 3D model, Non-cohesive soil, Overtopping failure, Tailwater depth

    Notation

    d50

    Mean partical diameterWc

    Optimum water contentZo

    Dam height (cm)do

    Tailwater depth (cm)Zeroded

    Eroded height of the dam measured at distance of 0.7 m from the dam heel (cm)t

    Total time of failure (sec)t1

    Time of crest width erosion (sec)Zcrest

    The crest height (cm)Vtotal

    Total volume of the dam (m3)Veroded

    Cumulative eroded volume (m3)RMSE

    The statistical variable root- mean- square errord

    Degree of agreement indexyu.s.

    The upstream water depth (cm)yd.s

    The downstream water depth (cm)H

    Water surface elevation over sharp crested weir (cm)Q

    Outflow discharge (liter/sec)Qpeak

    Peak discharge (liter/sec)

    1. Introduction

    Earth dams are compacted structures composed of natural materials that are usually mined or quarried from local locations. The failures of the earth dams have proven to be deadly, destructive, and costly. According to People’s Daily, two earthen dams, Yongโ€™an Dam and Xinfa Dam located in Hulun Buir City in North China’s Inner Mongolia failed on 2021, due to a surge in the water level of the Nuomin River caused by heavy rain. The dam breach affected 16,660 people, flooded 325,622 mu of farmland (21708.1 ha), and destroyed 22 bridges, 124 culverts, and 15.6 km of roadways. Also, the failure of south fork dam (earth and rock fill dam) near Johnstown on 1889 is considered the worst U.S dam disaster in terms of loss of life. The dam was overtopped and washed away due to unexpected heavy rains, releasing 20 million tons of water which destroyed Johnstown and resulted in 2209 deaths, [1][2]. Piping or shear sliding, failure due to natural factors, and failure due to overtopping are all possible causes of earth dam failure. However, overtopping failure is the most frequent cause of dam failure. According to The International Committee on Large Dams (ICOLD, 1995), and [3], more than one-third of the total known dam failures were caused by dam overtopping.

    Overtopping occurs as the result of insufficient flood design or freeboard in some cases. Extreme rainstorms can cause floods which can overtop the dam and cause it to fail. The size and geometry of the reservoir or the dam (side slopes, top width, height, etc.), the homogeneity of the material used in the construction of the dam, overtopping depth, and the presence or absence of tailwater are all elements that influence this type of failure which will be illustrated in the following literature. Overtopping failures of earth dams may be divided into several failure mechanisms based on the material composition and the inner structure of the dam. For cohesive earth dams because of low permeability, no seepage exists on the slopes. Erosion often begins at the earth dam toe during turbulent erosion and moves upstream, undercutting the slope, causing the removal of large chunks of materials. While for non-cohesive earth dams the downstream face of the dam flattens progressively and is often said to rotate around a point near the downstream toe [4][5][6] In the last few decades, the study of failures due to overtopping has gained popularity among researchers. The overtopping failure, in fact, has been widely investigated in coastal and river hydraulics and morpho dynamic. In addition, several laboratory experimental studies have been conducted in this field in order to better understand different involved factors. Also, many numerical types of research have been conducted to investigate the process of overtopping failure as well as the elements that influence this type of failure.

    Tabrizi et al. [5] conducted a series of embankment overtopping tests to find the effect of compaction on the failure of a homogenous sand embankment. A plane breach process occurred across the flume width due to the narrow flume width. They measured the downstream hydrographs and embankment surface profile for every case. They concluded that the peak discharge decreased with a high compaction level, while the time to peak increased. Kansoh et al. [6] studied experimentally the failure of compacted homogeneous non-cohesive earthen embankment due to overtopping. They investigated the influence of different shape parameters including the downstream slope, the crest width, and the height of the embankment on the erosion process. The erosion process was initiated by carving a pilot channel into the embankment crest. They evaluated the time of embankment failure for different shape parameters. They concluded that the failure time increases with increasing the downstream slope and the crest width. Zhu et al. [7] investigated experimentally the breaching of five embankments, one constructed with pure sand, and four with different sand-siltโ€“clay mixtures. The erosion pattern was similar across the flume width. They stated that for cohesive soil mixtures the head cut erosion was the most important factor that affected the breach growth, while for non-cohesive soil the breach erosion was affected by shear erosion.

    Amaral et al. [8] studied experimentally the failure by overtopping for two embankments built from silt sand material. They studied the effect of the degree of compaction of the embankment and the geometry of the pilot channel carved at the centre of the dam crest. They studied two shapes of pilot channel a rectangular shape and triangular shape. They stated that the breach development is influenced by a higher degree of compaction, however, the pilot channel geometry did not influence the breach’s final form. Bereta et al. [9] studied experimentally the breach formation of five dam models, three of them were homogenous clay soil while two were sandy-clay mixtures. The erosion process was initiated by cutting a pilot channel at the centre of the dam crest. They observed the initiation of erosion, flow shear erosion, sidewall bottom erosion, and distinguished the soil mechanical slope mass failure from the head cut vertically and laterally during these tests. Verma et al. [10] investigated experimentally a two-dimensional erosion phenomenon due to overtopping by using a wooden fuse plug model and five different soils. They concluded that the erosion process was affected mostly by cohesiveness and degree of compaction. For cohesive soils, a head cut erosion was observed, while for non-cohesive soils surface erosion occurred gradually. Also, the dimensions of fuse plug, type of fill material, reservoir capacity, and inflow were found to affect the behaviour of the overall breaching process.

    Wu and Qin [11] studied the effect of adding coarse grains to the downstream face of a non-cohesive dam as a result of tailings deposition. The process of overtopping during tailings dam failures is analyzed and its effect on delaying the dam-break process and disaster mitigation are investigated. They found that the tested protective measures decreased the breach area, the maximum breaching flow discharge and flow velocity, and the downstream inundated area. Khankandi et al. [12] studied experimentally the effect of reservoir geometry on dam break flow in case of dry and wet bed conditions. They considered four different reservoir shapes, a long reservoir, a wide, a trapezoidal shaped and one with a 90โ—ฆ bend all with identical water volume and horizontal bed. The dam break is simulated by the sudden gate removal using a pneumatic jack. They measured the variation of water level over time with ultrasonic sensors and flow velocity component with an acoustic Doppler velocimeter. Also, the experimental results of water level variation are compared with Ritters solution (1892) [13]. They stated that for dry bed condition the long and 90 bend reservoirs results are close to the analytical solution by ritter also in these two shapes a 1D flow is noticed. However, for wide and trapezoidal reservoirs a 2D effect is significant due to flow contraction at channel entrance.

    Rifai et al. [14] conducted a series of experiments to investigate the effect of tailwater depth on the outflow discharge and breach geometry during non-cohesive homogenous fluvial dikes overtopping failure. They cut an initial notch in the crest at 0.8 m from the upstream end of the dike to initiate overtopping. They compared their results to previous experiments under different main channel inflow discharges combined with a free floodplain. They divided the dike breaching process into three stages: gradual start of overtopping flow resulting in slow initiation of dike erosion, deepening and widening breach due to large flow depth and velocity, finally the flow depth starts stabilizing at its minimal level with or without sustained breach expansion. They stated that breach discharge has lower values than in free floodplain tests. Jiang [15] studied the effect of bed slope on breach parameters and peak discharge in non-cohesive embankment failure. An initial triangular breach with a depth and width of 4 cm was pre-set on one side of the dam. He stated that peak discharge increases with the increase of bed slope and then decreases.

    Ozmen-cagatay et al. [16] studied experimentally flood wave propagation resulted from a sudden dam break event. For dam-break modelling, they used a mechanism that permitted the rapid removal of a vertical plate with a thickness of 4 mm and made of rigid plastic. They conducted three tests, one with dry bed condition and two tests with tailwater depths equal 0.025 m and 0.1 m respectively. They recorded the free surface profile during initial stages of dam break by using digital image processing. Finally, they compared the experimental results with the with a commercially available VOF-based CFD program solving the Reynolds-averaged Navier โ€“Stokes equations (RANS) with the kโ€“ ฦ turbulence model and the shallow water equations (SWEs). They concluded that Wave breaking was delayed with increasing the tailwater depth to initial reservoir depth ratio. They also stated that the SWE approach is sufficient more to represent dam break flows for wet bed condition. Evangelista [17] investigated experimentally and numerically using a depth-integrated two-phase model, the erosion of sand dike caused by the impact of a dam break wave. The dam break is simulated by a sudden opening of an upstream reservoir gate resulting in the overtopping of a downstream trapezoidal sand dike. The evolution of the water wave caused from the gate opening and dike erosion process are recorded by using a computer-controlled camera. The experimental results demonstrated that the progression of the wave front and dike erosion have a considerable influence on each other during the process. In addition, the dike constructed from fine sands was more resistant to erosion than the one built with coarse sand. They also stated that the numerical model can is capable of accurately predicting wave front position and dike erosion. Also, Di Cristo et al. [18] studied the effect of dam break wave propagation on a sand embankment both experimentally and numerically using a two-phase shallow-water model. The evolution of free surface and of the embankment bottom are recorded and used in numerical model assessment. They stated that the model allows reasonable simulation of the experimental trends of the free surface elevation regardeless of the geofailure operator.

    Lots of numerical models have been developed over the past few years to simulate the dam break flooding problem. A one-dimensional model, such as Hec-Ras, DAMBRK and MIKE 11, ect. A two-dimensional model such as iRIC Nay2DH is used in earth embankment breach simulation. Other researchers studied the failure process numerically using (3D) computational fluid dynamics (CFD) models, such as FLOW-3D, and FLUENT. Goharnejad et al. [19] determined the outflow hydrograph which results from the embankment dam break due to overtopping. Hu et al. [20] performed a comparison between Flow-3D and MIKE3 FM numerical models in simulating a dam break event under dry and wet bed conditions with different tailwater depths. Kaurav et al. [21] simulated a planar dam breach process due to overtopping. They conducted a sensitivity analysis to find the effect of dam material, dam height, downstream slope, crest width, and inlet discharge on the erosion process and peak discharge through breach. They concluded that downstream slope has a significant influence on breaching process. Yusof et al. [22] studied the effect of embankment sediment sizes and inflow rates on breaching geometric and hydrodynamic parameters. They stated that the peak outflow hydrograph increases with increasing sediment size and inflow rates while time of failure decreases.

    In the present work, the effect of tailwater depth on earth dam failure during overtopping is studied experimentally. The relation between the eroded volume of the dam and the tailwater depth is presented. Also, the percentage of reduction in peak discharge due to tailwater existence is calculated. An assessment of Flow 3D software performance in simulating the erosion process during earth dam failure is introduced. The statistical variable root- mean- square error, RMSE, and the agreement degree index, d, are used in model assessment.

    2. Material and methods

    The tests are conducted in a straight rectangular flume in the laboratory of Irrigation Engineering and Hydraulics Department, Faculty of Engineering, Alexandria University, Egypt. The flume dimensions are 10 m long, 0.86 m wide, and 0.5 m deep. The front part of the flume is connected to a storage basin 1 m long by 0.86 m wide. The storage basin is connected to a collecting tank for water recirculation during the experiments as shown in Fig. 1Fig. 2. A sharp-crested weir is placed at a distance of 4 m downstream the constructed dam to keep a constant tailwater depth in each experiment and to measure the outflow discharge.

    To measure the eroded volume with time a rods technique is used. This technique consists of two parallel wooden plates with 10 cm distance in between and five rows of stainless-steel rods passing vertically through the wooden plates at a spacing of 20 cm distributed across flume width. Each row consists of four rods with 15 cm spacing between them. Also, a graph board is provided to measure the drop in each rod with time as shown in Fig. 3Fig. 4. After dam construction the rods are carefully rested on the dam, with the first line of rods resting in the middle of the dam crest and then a constant distance of 15 cm between rods lines is maintained.

    A soil sample is taken and tested in the laboratory of the soil mechanics to find the soil geotechnical parameters. The soil particle size distribution is also determined by sieve analysis as shown in Fig. 5. The soil mean diameter d50,equals 0.38 mm and internal friction angle equals 32.6ยฐ.

    2.1. Experimental procedures

    To investigate the effect of the tailwater depth (do), the tailwater depth is changed four times 5, 15, 20, and 25 cm on the sand dam model. The dam profile is 35 cm height, with crest width = 15 cm, the dam base width is 155 cm, and the upstream and downstream slopes are 2:1 as shown in Fig. 6. The dam dimensions are set as the flume permitted to allow observation of the dam erosion process under the available flume dimensions and conditions. All of the conducted experiments have the same dimensions and configurations.

    The optimum water content, Wc, from the standard proctor test is found to be 8 % and the maximum dry unit weight is 19.42 kN/m3. The soil and water are mixed thoroughly to ensure consistency and then placed on three horizontal layers. Each layer is compacted according to ASTM standard with 25 blows by using a rammer (27 cm ร— 20.5 cm) weighing 4 kg. Special attention is paid to the compaction of the soil to guarantee the repeatability of the tests.

    After placing and compacting the three layers, the dam slopes are trimmed carefully to form the trapezoidal shape of the dam. A small triangular pilot channel with 1 cm height and 1:1 side slopes is cut into the dam crest to initiate the erosion process. The position of triangular pilot channel is presented in Fig. 1. Three digital video cameras with a resolution of 1920 ร— 1080 pixels and a frame rate of 60 fps are placed in three different locations. One camera on one side of the flume to record the progress of the dam profile during erosion. Another to track the water level over the sharp-crested rectangular weir placed at the downstream end of the flume. And the third camera is placed above the flume at the downstream side of the dam and in front of the rods to record the drop of the tip of the rods with time as shown previously in Fig. 1.

    Before starting the experiment, the water is pumped into the storage basin by using pump with capacity 360 m3/hr, and then into the upstream section of the flume. The upstream boundary is an inflow condition. The flow discharge provided to the storage basin is kept at a constant rate of 6 L/sec for all experiments, while the downstream boundary is an outflow boundary condition.

    Also, the required tailwater depth for each experiment is filled to the desired depth. A dye container valve is opened to color the water upstream of the dam to make it easy to distinguish the dam profile from the water profile. A wooden board is placed just upstream of the dam to prevent water from overtopping the dam until the water level rises to a certain level above the dam crest and then the wooden board is removed slowly to start the experiment.

    2.2. Repeatability

    To verify the accuracy of the results, each experiment is repeated two times under the same conditions. Fig. 7 shows the relative eroded crest height, Zeroded / Zo, with time for 5 cm tailwater depth. From the Figure, it can be noticed that results for all runs are consistent, and accuracy is achieved.

    3. Numerical model

    The commercially available numerical model, Flow 3D is used to simulate the dam failure due to overtopping for the cases of 15 cm, 20 cm and 25 cm tailwater depths. For numerical model calibration, experimental results for dam surface evolution are used. The numerical model is calibrated for selection of the optimal turbulence model (RNG, K-e, and k-w) and sediment scour equations (Van Rin, Meyer- peter and Muller, and Nielsen) that produce the best results. In this, the flow field is solved by the RNG turbulence model, and the van Rijn equation is used for the sediment scour model. A geometry file is imported before applying the mesh.

    A Mesh sensitivity is analyzed and checked for various cell sizes, and it is found that decreasing the cell size significantly increases the simulation time with insignificant differences in the result. It is noticed that the most important factor influencing cell size selection is the value of the damโ€™s upstream and downstream slopes. For example, the slopes in the dam model are 2:1, thus the cell size ratio in X and Z directions should be 2:1 as well. The cell size in a mesh block is set to be 0.02 m, 0.025 m, and 0.01 m in X, Y and Z directions respectively.

    In the numerical computations, the boundary conditions employed are the walls for sidewalls and the channel bottom. The pressure boundary condition is applied at the top, at the airโ€“water interface, to account for atmospheric pressure on the free surface. The upstream boundary is volume flow rate while the downstream boundary is outflow discharge.

    The initial condition is a fluid region, which is used to define fluid areas both upstream and downstream of the dam. To assess the model accuracy, the statistical variable root- mean- square error, RMSE, and the agreement degree index, d, are calculated as(1)RMSE=1Nโˆ‘i=1N(Pi-Mi)2(2)d=1-โˆ‘Mi-Pi2โˆ‘Mi-Mยฏ+Pi-Pยฏ2

    where N is the number of samples, Pi and Mi are the models and experimental values, P and M are the means of the model and experimental values. The best fit between the experimental and model results would have an RMSE = 0 and degree of agreement, d = 1.

    4. Results of experimental work

    The results of the total time of failure, t (defined as the time from when the water begins to overtop the dam crest until the erosion reaches a steady state, when no erosion occurs), time of crest width erosion t1, cumulative eroded volume Veroded, and peak discharge Qpeak for each experiment are listed in Table 1. The case of 5 cm tailwater depth is considered as a reference case in this work.

    Table 1. Results of experimental work.

    Tailwater depth, do (cm)Total time of failure, t (sec)Time of crest width erosion, t1 (sec)cumulative eroded volume, Veroded (m3)Peak discharge, Qpeak (liter/sec)
    5255220.2113.12
    15165300.1612.19
    20140340.1311.29
    25110390.0510.84

    5. Discussion

    5.1. Side erosion

    The evolution of the bathymetry of the erosion line recorded by the video camera1. The videos are split into frames (60 frames/sec) by the Free Video to JPG Converter v.5.063 build and then converted into an excel spreadsheet using MATLAB code as shown in Fig. 8.

    Fig. 9 shows a sample of numerical model output. Fig. 10Fig. 11Fig. 12 show a dam profile development for different time steps from both experimental and numerical model, for tailwater depths equal 15 cm, 20 cm and 25 cm. Also, the values of RMSE and d for each figure are presented. The comparison shows that the Flow 3D software can simulate the erosion process of non-cohesive earth dam during overtopping with an RMSE value equals 0.023, 0.0218, and 0.0167 and degree of agreement, d, equals 0.95, 0.968, and 0.988 for relative tailwater depths, do/(do)ref, = 3, 4 and 5, respectively. The low values of RMSE and high values of d show that the Flow 3D can effectively simulate the erosion process. From Fig. 10Fig. 11Fig. 12, it can be noticed that the model is not capable of reproducing the head cut, while it can simulate well the degradation of the crest height with a minor difference from experimental work. The reason of this could be due to inability of simulation of all physical conditions which exists in the experimental work, such as channel friction and the grain size distribution of the dam soil which is surely has a great effect on the erosion process and breach development. In the experimental work the grain size distribution is shown in Fig. 5, while the numerical model considers that the soil is uniform and exactly 50 % of the dam particles diameter are equal to the d50 value. Another reason is that the model is not considering the increased resistance of the dam due to the apparent cohesion which happens due to dam saturation [23].

    It is clear from both the experimental and numerical results that for a 5 cm tailwater depth, do/(do)ref = 1.0, erosion begins near the dam toe and continues upward on the downstream slope until it reaches the crest. After eroding the crest width, the crest is lowered, resulting in increased flow rates and the speeding up of the erosion process. While for relative tailwater depths, do/(do)ref = 3, 4, and 5 erosion starts at the point of intersection between the downstream slope and tailwater. The existence of tailwater works as an energy dissipater for the falling water which reduces the erosion process and prevents the dam from failure as shown in Fig. 13. It is found that the time of the failure decreases with increasing the tailwater depth because most of the dam height is being submerged with water which decreases the erosion process. The reduction in time of failure from the referenced case is found to be 35.3, 45, and 57 % for relative tailwater depth, do /(do)ref equals 3, 4, and 5, respectively.

    The relation between the relative eroded crest height, Zeroded /Zo, with time is drawn as shown in Fig. 14. It is found that the relative eroded crest height decreases with increasing tailwater depth by 10, 41, and 77.6 % for relative tailwater depth, do /(do)ref equals 3, 4, and 5, respectively. The time required for the erosion of the crest width, t1, is calculated for each experiment. The relation between relative tailwater depth and relative time of crest width erosion is shown in Fig. 15. It is found that the time of crest width erosion increases linearly with increasing, do /Zo. The percent of increase is 36.4, 54.5 and 77.3 % for relative tailwater depth, do /(do)ref = 3, 4 and 5, respectively.

    Crest height, Zcrest is calculated from the experimental results and the Flow 3D results for relative tailwater depths, do/(do)ref, = 3, 4, and 5. A relation between relative crest height, Zcrest/Zo with time from experimental and numerical results is presented in Fig. 16. From Fig. 16, it is seen that there is a good consistency between the results of numerical model and the experimental results in the case of tracking the erosion of the crest height with time.

    5.2. Upstream and downstream water depths

    It is noticed that at the beginning of the erosion process, both upstream and downstream water depths increase linearly with time as long as erosion of the crest height did not take place. However, when the crest height starts to lower the upstream water depth decreases with time while the downstream water depth increases. At the end of the experiment, the two depths are nearly equal. A relation between relative downstream and upstream water depths with time is drawn for each experiment as shown in Fig. 17.

    5.3. Eroded volume

    A MATLAB code is used to calculate the cumulative eroded volume every time interval for each experiment. The total volume of the dam, Vtotal is 0.256 m3. The cumulative eroded volume, Veroded is 0.21, 0.16, 0.13, and 0.05 m3 for tailwater depths, do = 5, 15, 20, and 25 cm, respectively. Fig. 18 presents the relation between cumulative eroded volume, Veroded and time. From Fig. 18, it is observed that the cumulative eroded volume decreases with increasing the tailwater depth. The reduction in cumulative eroded volume is 23, 36.5, and 75 % for relative tailwater depth, do /(do)ref = 3, 4, and 5, respectively. The relative remained volume of the dam equals 0.18, 0.375, 0.492, and 0.8 for tailwater depths = 5, 15, 20, and 25 cm, respectively. Fig. 19 shows a relation between relative tailwater depth and relative cumulative eroded volume from experimental results. From that figure, it is noticed that the eroded volume decreases exponentially with increasing relative tailwater depth.

    5.4. The outflow discharge

    The inflow discharge provided to the storage tank is maintained constant for all experiments. The water surface elevation, H, over the sharp-crested weir placed at the downstream side is recorded by the video camera 2. For each experiment, the outflow discharge is then calculated by using the sharp-crested rectangular weir equation every 10 sec.

    The outflow discharge is found to increase rapidly until it reaches its peak then it decreases until it is constant. For high values of tailwater depths, the peak discharge becomes less than that in the case of small tailwater depth as shown in Fig. 20 which agrees well with the results of Rifai et al. [14] The reduction in peak discharge is 7, 14, and 17.35 % for relative tailwater depth, do /(do)ref = 3, 4, and 5, respectively.

    The scenario presented in this article in which the tailwater depth rises due to unexpected heavy rainfall, is investigated to find the effect of rising tailwater depth on earth dam failure. The results revealed that rising tailwater depth positively affects the process of dam failure in terms of preventing the dam from complete failure and reducing the outflow discharge.

    6. Conclusions

    The effect of tailwater depth on earth dam failure due to overtopping is investigated experimentally in this work. The study focuses on the effect of tailwater depth on side erosion, upstream and downstream water depths, eroded volume, outflow hydrograph, and duration of the failure process. The Flow 3D numerical software is used to simulate the dam failure, and a comparison is made between the experimental and numerical results to find the ability of this software to simulate the erosion process. The following are the results of the investigation:

    The existence of tailwater with high depths prevents the dam from completely collapsing thereby turning it into a broad crested weir. The failure time decreases with increasing the tailwater depth and the reduction from the reference case is found to be 35.3, 45, and 57 % for relative tailwater depth, do /(do)ref = 3, 4, and 5, respectively. The difference between the upstream and downstream water depths decreases with time till it became almost negligible at the end of the experiment. The reduction in cumulative eroded volume is 23, 36.5, and 75 % for relative tailwater depth, do /(do)ref = 3, 4, and 5, respectively. The peak discharge decreases by 7, 14, and 17.35 % for relative tailwater depth, do /(do)ref = 3, 4, and 5, respectively. The relative eroded crest height decreases linearly with increasing the tailwater depth by 10, 41, and 77.6 % for relative tailwater depth, do /(do)ref = 3, 4, and 5, respectively. The numerical model can reproduce the erosion process with a minor deviation from the experimental results, particularly in terms of tracking the degradation of the crest height with time.

    Declaration of Competing Interest

    The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.

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    Cited by (0)

    My name is Shaimaa Ibrahim Mohamed Aman and I am a teaching assistant in Irrigation and Hydraulics department, Faculty of Engineering, Alexandria University. I graduated from the Faculty of Engineering, Alexandria University in 2013. I had my MSc in Irrigation and Hydraulic Engineering in 2017. My research interests lie in the area of earth dam Failures.

    Peer review under responsibility of Ain Shams University.

    ยฉ 2022 THE AUTHORS. Published by Elsevier BV on behalf of Faculty of Engineering, Ain Shams University.

    Dissipating Culvert End Design for Erosion Control Using CFD Platform FLOW-3D Numerical Simulation Modeling

    CFD ํ”Œ๋žซํผ FLOW-3D ์ˆ˜์น˜ ์‹œ๋ฎฌ๋ ˆ์ด์…˜ ๋ชจ๋ธ๋ง์„ ์‚ฌ์šฉํ•œ ์นจ์‹ ์ œ์–ด๋ฅผ ์œ„ํ•œ ๋ถ„์‚ฐ ์•”๊ฑฐ ์ข…๋‹จ ์„ค๊ณ„

    Dissipating Culvert End Design for Erosion Control Using CFD Platform FLOW-3D Numerical Simulation Modeling

    Saman Mostafazadeh-Fard

    Graduate Research Assistant, Dept. of Civil Engineering, New Mexico State Univ., P.O. Box 30001, MSC 3CE, Las Cruces, NM 88003-8001 (corresponding author). Email: samanmzf@nmsu.edu

    Zohrab Samani

    Professor, Dept. of Civil Engineering, New Mexico State Univ., P.O. Box 30001, MSC 3CE, Las Cruces, NM 88003-8001. Email: zsamani@nmsu.edu

    Abstract

    ์ถ”์ƒ์ ์ธ
    ์•”๊ฑฐ ๋์—์„œ ๋‚˜์˜ค๋Š” ๊ณ ์† ํ๋ฆ„์œผ๋กœ ์ธํ•œ ํ•˜๋ฅ˜ ์นจ์‹ ๋ฐ ์„ธ๊ตด์€ ์ˆ˜๋ ฅ ์—”์ง€๋‹ˆ์–ด๊ฐ€ ์ง๋ฉดํ•œ ์ฃผ์š” ๋ฌธ์ œ ์ค‘ ํ•˜๋‚˜์ž…๋‹ˆ๋‹ค. ๋ณธ ๋…ผ๋ฌธ์˜ ์ฃผ์š” ๋ชฉ์ ์€ ์ผ๋ฐ˜์ ์ธ ์•”๊ฑฐ ๋‹จ๋ถ€์—์„œ ๋‚˜์˜ค๋Š” ๊ณ ์† ํ๋ฆ„์œผ๋กœ ์ธํ•œ ํ•˜๋ฅ˜ ์นจ์‹ ๋ฐ ์„ธ๊ตด์˜ ์œ„ํ—˜์„ ์ค„์ผ ์ˆ˜ ์žˆ๋Š” ๋ถ„์‚ฐ ์•”๊ฑฐ ๋‹จ๋ถ€ ์„ค๊ณ„๋ฅผ ๊ฐœ๋ฐœํ•˜๋Š” ๊ฒƒ์ด์—ˆ์Šต๋‹ˆ๋‹ค. ์ด๋ฅผ ์œ„ํ•ด ์ „์‚ฐ ์œ ์ฒด ์—ญํ•™(CFD) ํ”Œ๋žซํผ FLOW-3D ๋ฒ„์ „ 11.1.0 ์ฝ”๋“œ๋ฅผ ์‹คํ—˜ ์‹คํ–‰[๊ฒฐ์ • ๊ณ„์ˆ˜ R2>0.90 ๋ฐ ํ‰๊ท  ์ œ๊ณฑ๊ทผ ์˜ค์ฐจ(RMSE)<1.9 cm]์„ ๊ธฐ๋ฐ˜์œผ๋กœ ๋ณด์ • ๋ฐ ๊ฒ€์ฆํ–ˆ์Šต๋‹ˆ๋‹ค. ๊ทธ๋Ÿฐ ๋‹ค์Œ ์ฝ”๋“œ๋ฅผ ์‚ฌ์šฉํ•˜์—ฌ ๋‘ ๊ฐ€์ง€ ๋Œ€์•ˆ์ ์ธ ์†Œ๋ฉธ ์•”๊ฑฐ ๋ ์„ค๊ณ„(ALT 1 ๋ฐ ALT 2)๋ฅผ ๊ฐœ๋ฐœํ•˜๊ณ  ํ•˜๋ฅ˜ ์นจ์‹ ๋ฐ ์„ธ๊ตด ์™„ํ™” ๊ฐ€๋Šฅ์„ฑ์„ ๋ถ„์„ํ–ˆ์Šต๋‹ˆ๋‹ค. ๊ฐ๊ฐ์˜ ์ถœ์ˆ˜์œ ์†๊ณผ ์šด๋™์—๋„ˆ์ง€๋ฅผ ์ธก์ •ํ•˜์—ฌ ์ „ํ˜•์ ์ธ ์•”๊ฑฐ๋‹จ๋ถ€(๋Œ€์กฐ)์œ ๋Ÿ‰๊ณผ ๋น„๊ตํ•˜์˜€๋‹ค. ๊ฒฐ๊ณผ์— ๋”ฐ๋ฅด๋ฉด ์ œ์–ด ํ๋ฆ„์—์„œ์˜ ์งˆ๋Ÿ‰ ํ‰๊ท  ์œ ์ฒด ํ‰๊ท  ์šด๋™ ์—๋„ˆ์ง€๋Š” 1.37 j/kg2๋กœ ๊ธฐ๋ก๋˜์—ˆ์œผ๋ฉฐ, ALT 1 ๋ฐ ALT 2 ํ๋ฆ„์—์„œ ๊ฐ๊ฐ 0.83 ๋ฐ 0.73 j/kg2๋กœ ์ธก์ •๋˜์—ˆ์Šต๋‹ˆ๋‹ค. ๋”ฐ๋ผ์„œ ์ œ์–ด ํ๋ฆ„ ํ•˜์—์„œ ํ•˜๋ฅ˜ ์ƒŒ๋“œ๋ฐ•์Šค ๋งค์Šค์˜ ์ œ๊ฑฐ๋Š” ALT 1 ๋ฐ ALT 2 ํ๋ฆ„์— ๋น„ํ•ด ๊ฐ๊ฐ ์•ฝ 11.1% ๋ฐ 4.2% ๋” ๋†’์•˜์Šต๋‹ˆ๋‹ค. FLOW-3D ์ฝ”๋“œ๋Š” ์•”๊ฑฐ ๋ ํ๋ฆ„๊ณผ ํ•˜๋ฅ˜ ์นจ์‹์„ ์˜ˆ์ธกํ•˜๊ณ  ํ•˜๋ฅ˜ ์นจ์‹์„ ์ค„์ผ ์ˆ˜ ์žˆ๋Š” ์ž ์žฌ์  ์†Œ์‚ฐ ์•”๊ฑฐ ๋์„ ์„ค๊ณ„ํ•˜๋Š” ๋ฐ ์‚ฌ์šฉํ•  ์ˆ˜ ์žˆ์Šต๋‹ˆ๋‹ค.

    Downstream erosion and scouring caused by high-velocity flow issuing from culvert ends are one of the main problems faced by hydraulic engineers. The main objective of this paper was to develop a dissipating culvert end design that can reduce the risk of downstream erosion and scour caused by high-velocity flow issuing from typical culvert ends. For this purpose, the computational fluid dynamics (CFD) platform FLOW-3D version 11.1.0 code was calibrated and validated based on the experimental runs [coefficient of determinationย R2>0.90R2>0.90ย and root mean square errorย (RMSE)<1.9โ€‰โ€‰cm(RMSE)<1.9โ€‰โ€‰cm]. Two alternative dissipating culvert end designs (ALT 1 and ALT 2) were then developed using the code, and their potential in mitigation of downstream erosion and scouring was analyzed. The issuing flow velocity and kinetic energy for each were measured and compared with typical culvert end (control) flow. According to the results, mass averaged fluid mean kinetic energy in the control flow was recorded atย 1.37โ€‰โ€‰j/kg21.37โ€‰โ€‰j/kg2ย and was measured at 0.83 andย 0.73โ€‰โ€‰j/kg20.73โ€‰โ€‰j/kg2ย in ALT 1 and ALT 2 flows, respectively. Accordingly, the removal of downstream sandbox mass under control flow was approximately 11.1% and 4.2% higher compared with ALT 1 and ALT 2 flows, respectively. FLOW-3D code can be used to predict culvert end flow and downstream erosion and to design potential dissipating culvert ends that can reduce downstream erosion.

    Dissipating Culvert End Design for Erosion Control Using CFD Platform FLOW-3D Numerical Simulation Modeling
    Dissipating Culvert End Design for Erosion Control Using CFD Platform FLOW-3D Numerical Simulation Modeling
    Propagation of Landslide Surge in Curved River Channel and Its Interaction with Dam

    ๊ตฝ์€ ๊ฐ•๋‘‘ ์‚ฐ์‚ฌํƒœ์˜ ํŒฝ์ฐฝ ์ „ํŒŒ ๋ฐ ๋Œ๊ณผ์˜ ์ƒํ˜ธ ์ž‘์šฉ, ๊ณก์„ ํ•˜์ฒœ์˜ ์‚ฐ์‚ฌํƒœ ํ•ด์ผ ์ „ํŒŒ ๋ฐ ๋Œ๊ณผ์˜ ์ƒํ˜ธ์ž‘์šฉ

    ๊ตฝ์€ ๊ฐ•๋‘‘ ์‚ฐ์‚ฌํƒœ์˜ ํŒฝ์ฐฝ ์ „ํŒŒ ๋ฐ ๋Œ๊ณผ์˜ ์ƒํ˜ธ ์ž‘์šฉ

    ํŽ‘ํ›„์ด, ํ™ฉ์•ผ์ง€์—    

    1. ์ˆ˜์ž์› ๋ณด์กด ๋ฐ ํ™˜๊ฒฝ ํ•™๊ต, Three Gorges University, Yichang, Hubei 443000
    • ๆ”ถ็จฟๆ—ฅๆœŸ:2021-08-19 ไฟฎๅ›žๆ—ฅๆœŸ:2021-09-30 ๅ‘ๅธƒๆ—ฅๆœŸ:2022-10-13
    • ้€š่ฎฏไฝœ่€…: Huang Yajie (1993-), Shangqiu, Henan, ์„์‚ฌ ํ•™์œ„, ๊ทธ์˜ ์—ฐ๊ตฌ ๋ฐฉํ–ฅ์€ ์ˆ˜๋ฆฌ ๊ตฌ์กฐ์ž…๋‹ˆ๋‹ค. ์ด๋ฉ”์ผ: master_hyj@163.com
    • ไฝœ่€…็ฎ€ไป‹:Peng Hui(1976-)๋Š” ํ›„๋ฒ ์ด์„ฑ โ€‹โ€‹์ด์ฐฝ์—์„œ ํƒœ์–ด๋‚˜ ๊ต์ˆ˜, ์˜์‚ฌ, ๋ฐ•์‚ฌ ์ง€๋„๊ต์ˆ˜๋กœ ์ฃผ๋กœ ์ˆ˜๋ ฅ ๊ตฌ์กฐ์˜ ๊ต์œก ๋ฐ ์—ฐ๊ตฌ์— ์ข…์‚ฌํ–ˆ์Šต๋‹ˆ๋‹ค. ์ด๋ฉ”์ผ:hpeng1976@163.com
    • ๅŸบ้‡‘่ต„ๅŠฉ:๊ตญ๊ฐ€ํ•ต์‹ฌ์—ฐ๊ตฌ๊ฐœ๋ฐœ์‚ฌ์—…(2018YFC1508801-4)

    ๊ณก์„ ํ•˜์ฒœ์˜ ์‚ฐ์‚ฌํƒœ ํ•ด์ผ ์ „ํŒŒ ๋ฐ ๋Œ๊ณผ์˜ ์ƒํ˜ธ์ž‘์šฉ

    PENG Hui, HUANG Ya-jie    

    1. ์ค‘๊ตญ ์‚ผํ˜‘๋Œ€ํ•™ ์ˆ˜์ž์›ํ™˜๊ฒฝ๋Œ€ํ•™ ์ด์ฐฝ 443000 ์ค‘๊ตญ
    • Received:2021-08-19 Revised:2021-09-30 Published:2022-10-13

    Abstract

    ์ถ”์ƒ์ ์ธ:์ €์ˆ˜์ง€ ์ œ๋ฐฉ ์‚ฐ์‚ฌํƒœ๋Š” ์ผ๋ฐ˜์ ์ธ ์ง€์งˆํ•™์  ์œ„ํ—˜์œผ๋กœ, ์ œ๋•Œ์— ๋ฏธ๋ฆฌ ๊ฒฝ๊ณ ํ•˜์ง€ ์•Š์œผ๋ฉด ํ•˜์ฒœ์— ํ•ด์ผํŒŒ๊ฐ€ ๋ฐœ์ƒํ•˜์—ฌ ํ•˜์ฒœ ๊ตํ†ต์ด๋‚˜ ์ธ๊ทผ ์ˆ˜์ž์› ๋ณดํ˜ธ ์‹œ์„ค์˜ ์•ˆ์ „์„ ์œ„ํ—˜์— ๋น ๋œจ๋ฆด ์ˆ˜ ์žˆ์Šต๋‹ˆ๋‹ค. ์ €์ˆ˜์ง€ ์ œ๋ฐฉ ์‚ฐ์‚ฌํƒœ๋กœ ์ธํ•œ ํ•ด์ผํŒŒ ์ „ํŒŒ ์ „ํŒŒ Flow-3D๋ฅผ ์ด์šฉํ•˜์—ฌ ํ•˜๋ฅ˜ ๋Œ๊ณผ์˜ ์ƒํ˜ธ์ž‘์šฉ์„ ์‹œ๋ฎฌ๋ ˆ์ด์…˜ ํ•˜์˜€๋‹ค. ์ˆ˜๋ฆฌํ•™์  ๋ฌผ๋ฆฌ์  ๋ชจ๋ธ ์‹œํ—˜์˜ ํƒ€๋‹น์„ฑ๊ณผ ์ •ํ™•์„ฑ์„ ๊ฒ€์ฆํ•˜๊ธฐ ์œ„ํ•˜์—ฌ 3์ฐจ์› ์‚ฐ์‚ฌํƒœ ํ•ด์ง€ ๋ชจ๋ธ์„ ๊ตฌ์ถ•ํ•˜์˜€๋‹ค. ์ˆ˜๋ฉด ๋†’์ด ๋ณ€ํ™”์™€ ์„œ์ง€์˜ ์ „ํŒŒ ๊ณผ์ •์— ๋Œ€ํ•œ ์ˆ˜๋ฆฌํ•™์  ๋ฌผ๋ฆฌ์  ๋ชจ๋ธ ํ…Œ์ŠคํŠธ. ๊ทธ ๋™์•ˆ,๊ฐ€์žฅ ์œ„ํ—˜ํ•œ ์ˆ˜์‹ฌ๊ณผ ์ž…์‚ฌ๊ฐ ์กฐ๊ฑด์€ ๋‹ค์–‘ํ•œ ์กฐ๊ฑด์—์„œ ๋Œ๊ณผ ์‚ฐ์‚ฌํƒœ ํ•ด์ผ ์‚ฌ์ด์˜ ์ƒํ˜ธ ์ž‘์šฉ์„ ๋ถ„์„ํ•˜์—ฌ ์–ป์—ˆ์Šต๋‹ˆ๋‹ค. ์—”์ง€๋‹ˆ์–ด๋ง ์‚ฌ๋ก€๋Š” ์ตœ๋Œ€ ๋™์  ์ˆ˜๋‘๊ฐ€ ํ•ด์ผ ๋†’์ด์˜ ์ˆ˜๋‘๋ณด๋‹ค ์ž‘๊ณ  ๋ฌผ์„ ๋”ฐ๋ผ ๊ฐ์†Œํ•œ๋‹ค๋Š” ๊ฒƒ์„ ๋ณด์—ฌ์ฃผ์—ˆ์Šต๋‹ˆ๋‹ค. ์ด ๊ฒฝ์šฐ, ์„œ์ง€์˜ ์ •์  ์ตœ๋Œ€ ์ˆ˜๋‘์— ๋”ฐ๋ผ ๊ณ„์‚ฐ๋œ ๋Œ์˜ ์‘๋ ฅ์€ ์•ˆ์ „ํ•ฉ๋‹ˆ๋‹ค.

    As a common geological hazard,reservoir bank landslide would most probably induce surge waves in river if not prewarned in time,endangering river traffic or the safety of nearby water conservancy facilities.The propagation of surge wave induced by the landslide of curved river bank in reservoir and its interaction with downstream dam were simulated by using Flow-3D.A three-dimensional landslide surge model was constructed to verify the validity and accuracy of hydraulic physical model test.The result of the three-dimensional numerical simulation was in good agreement with that of hydraulic physical model test in terms of the water surface height change and the propagation process of the surge.In the mean time,the most dangerous water depth and incident angle conditions were obtained by analyzing the interaction between the dam and the landslide surge under different conditions.Engineering examples demonstrated that the maximum dynamic water head was smaller than the water head of surge height,and reduced along the water depth direction.In such cases,the stress of the dam calculated according to the static maximum water head of the surge is safe.

    Key words

    ์Šฌ๋ผ์ด๋“œ ์„œ์ง€,ย ๊ณก์„  ์ˆ˜๋กœํ˜• ์ €์ˆ˜์ง€,ย ์ˆ˜์น˜ ์‹œ๋ฎฌ๋ ˆ์ด์…˜,ย ๋™์  ์ˆ˜์••,ย ์ค‘๋ ฅ ๋Œ, slide surges,ย curved channel type reservoirs,ย numerical simulation,ย dynamic water pressure,ย gravity dam

    Fig. 8. Variation of water surface profile (a) ฮฑ = 0.1; (b) ฮฑ = 0.3; (c) ฮฑ = 0.5; (d) ฮฑ = 0.7.

    Numerical study of the dam-break waves and Favre waves down sloped wet rigid-bed at laboratory scale

    WenjunLiuaBoWangaYakunGuobaState Key Laboratory of Hydraulics and Mountain River Engineering, College of Water Resource and Hydropower, Sichuan University, Chengdu 610065, ChinabFaculty of Engineering & Informatics, University of Bradford, BD7 1DP, UK

    Highlights

    ๊ฒฝ์‚ฌ์ง„ ์Šต์œค์ธต์—์„œ ๋ŒํŒŒ๊ดด์œ ๋™๊ณผ FFavreย ํŒŒ๋ฅผ ์ˆ˜์น˜์ ์œผ๋กœ ์กฐ์‚ฌํ•˜์˜€๋‹ค.
    ์ˆ˜์ง ๋Œ€ ์ˆ˜ํ‰ ์†๋„์˜ ๋น„์œจ์ด ๋จผ์ € ์ •๋Ÿ‰ํ™”๋ฉ๋‹ˆ๋‹ค.
    ์œ ๋™ ์ƒํƒœ๋Š” ์œ ์ƒ ๊ฒฝ์‚ฌ๊ฐ€ ํฐ ํ›„๊ธฐ ๋‹จ๊ณ„์—์„œ ํฌ๊ฒŒ ๋ณ€๊ฒฝ๋ฉ๋‹ˆ๋‹ค.
    Favre ํŒŒ๋„๋Š” ์ˆ˜์ง ์†๋„์™€ ์ˆ˜์ง ๊ฐ€์†๋„์— ํฐ ์˜ํ–ฅ์„ ๋ฏธ์นฉ๋‹ˆ๋‹ค.
    ๋ฒ ๋“œ ์ „๋‹จ์‘๋ ฅ์˜ ๋ณ€ํ™”๋Š” ๋ฒ ๋“œ ๊ธฐ์šธ๊ธฐ์™€ ๊ผฌ๋ฆฌ๋ฌผ์˜ ์˜ํ–ฅ์„ ๋ฐ›์Šต๋‹ˆ๋‹ค.

    Abstract

    The bed slope and the tailwater depth are two important ones among the factors that affect the propagation of the dam-break flood and Favre waves. Most previous studies have only focused on the macroscopic characteristics of the dam-break flows or Favre waves under the condition of horizontal bed, rather than the internal movement characteristics in sloped channel. The present study applies two numerical models, namely, large eddy simulation (LES) and shallow water equations (SWEs) models embedded in the CFD software package FLOW-3D to analyze the internal movement characteristics of the dam-break flows and Favre waves, such as water level, the velocity distribution, the fluid particles acceleration and the bed shear stress, under the different bed slopes and water depth ratios. The results under the conditions considered in this study show that there is a flow state transition in the flow evolution for the steep bed slope even in water depth ratio ฮฑ = 0.1 (ฮฑ is the ratio of the tailwater depth to the reservoir water depth). The flow state transition shows that the wavefront changes from a breaking state to undular. Such flow transition is not observed for the horizontal slope and mild bed slope. The existence of the Favre waves leads to a significant increase of the vertical velocity and the vertical acceleration. In this situation, the SWEs model has poor prediction. Analysis reveals that the variation of the maximum bed shear stress is affected by both the bed slope and tailwater depth. Under the same bed slope (e.g., S0 = 0.02), the maximum bed shear stress position develops downstream of the dam when ฮฑ = 0.1, while it develops towards the end of the reservoir when ฮฑ = 0.7. For the same water depth ratio (e.g., ฮฑ = 0.7), the maximum bed shear stress position always locates within the reservoir at S0 = 0.02, while it appears in the downstream of the dam for S0 = 0 and 0.003 after the flow evolves for a while. The comparison between the numerical simulation and experimental measurements shows that the LES model can predict the internal movement characteristics with satisfactory accuracy. This study improves the understanding of the effect of both the bed slope and the tailwater depth on the internal movement characteristics of the dam-break flows and Favre waves, which also provides a valuable reference for determining the flood embankment height and designing the channel bed anti-scouring facility.

    Fig. 1. Sketch of related variables involved in shallow water model.
    Fig. 1. Sketch of related variables involved in shallow water model.
    Fig. 2. Flume model in numerical simulation.
    Fig. 2. Flume model in numerical simulation.
    Fig. 3. Grid sensitivity analysis (a) water surface profile; (b) velocity profile.
    Fig. 3. Grid sensitivity analysis (a) water surface profile; (b) velocity profile.
    Fig. 4. Sketch of experimental set-up for validating the velocity profile.
    Fig. 4. Sketch of experimental set-up for validating the velocity profile.
    Fig. 5. Sketch of experimental set-up for validating the bed shear stress.
    Fig. 5. Sketch of experimental set-up for validating the bed shear stress.
    Fig. 6. Model validation results (a) variation of the velocity profile; (b) error value of the velocity profile; (c) variation of the bed shear stress; (d) error value of the bed shear stress.
    Fig. 6. Model validation results (a) variation of the velocity profile; (b) error value of the velocity profile; (c) variation of the bed shear stress; (d) error value of the bed shear stress.
    Fig. 7. Schematic diagram of regional division.
    Fig. 7. Schematic diagram of regional division.
    Fig. 8. Variation of water surface profile (a) ฮฑ = 0.1; (b) ฮฑ = 0.3; (c) ฮฑ = 0.5; (d) ฮฑ = 0.7.
    Fig. 8. Variation of water surface profile (a) ฮฑ = 0.1; (b) ฮฑ = 0.3; (c) ฮฑ = 0.5; (d) ฮฑ = 0.7.
    Fig. 8. (continued).
    Fig. 8. (continued).
    Fig. 8. (continued).
    Fig. 8. (continued).
    Fig. 8. (continued).
    Fig. 8. (continued).
    Fig. 9. Froude number for ฮฑ = 0.1 (a) variation with time; (b) variation with wavefront position.
    Fig. 9. Froude number for ฮฑ = 0.1 (a) variation with time; (b) variation with wavefront position.
    Fig. 10. Characteristics of velocity distribution (a) ฮฑ = 0.1; (b) ฮฑ = 0.3; (c) ฮฑ = 0.5; (d) ฮฑ = 0.7.
    Fig. 10. Characteristics of velocity distribution (a) ฮฑ = 0.1; (b) ฮฑ = 0.3; (c) ฮฑ = 0.5; (d) ฮฑ = 0.7.
    Fig. 11. Average proportion of the vertical velocity (a) ฮฑ = 0.1; (b) ฮฑ = 0.3; (c) ฮฑ = 0.5; (d) ฮฑ = 0.7.
    Fig. 11. Average proportion of the vertical velocity (a) ฮฑ = 0.1; (b) ฮฑ = 0.3; (c) ฮฑ = 0.5; (d) ฮฑ = 0.7.
    Fig. 12. Bed shear stress distribution (a) ฮฑ = 0.1; (b) ฮฑ = 0.3; (c) ฮฑ = 0.5; (d) ฮฑ = 0.7.
    Fig. 12. Bed shear stress distribution (a) ฮฑ = 0.1; (b) ฮฑ = 0.3; (c) ฮฑ = 0.5; (d) ฮฑ = 0.7.
    Fig. 12. (continued).
    Fig. 12. (continued).
    Fig. 13. Variation of the maximum bed shear stress position with time (a) ฮฑ = 0.1; (b) ฮฑ = 0.3; (c) ฮฑ = 0.5; (d) ฮฑ = 0.7.
    Fig. 13. Variation of the maximum bed shear stress position with time (a) ฮฑ = 0.1; (b) ฮฑ = 0.3; (c) ฮฑ = 0.5; (d) ฮฑ = 0.7.
    Fig. 14. Time when the maximum bed shear stress appears at different positions (a) ฮฑ = 0.1; (b) ฮฑ = 0.3; (c) ฮฑ = 0.5; (d) ฮฑ = 0.7.
    Fig. 14. Time when the maximum bed shear stress appears at different positions (a) ฮฑ = 0.1; (b) ฮฑ = 0.3; (c) ฮฑ = 0.5; (d) ฮฑ = 0.7.
    Fig. 15. Movement characteristics of the fluid particles (a) ฮฑ = 0.1; (b) ฮฑ = 0.3; (c) ฮฑ = 0.5; (d) ฮฑ = 0.7.
    Fig. 15. Movement characteristics of the fluid particles (a) ฮฑ = 0.1; (b) ฮฑ = 0.3; (c) ฮฑ = 0.5; (d) ฮฑ = 0.7.
    Fig. 15. (continued).
    Fig. 15. (continued).

    Keywords

    Dam-break flow, Bed slope, Wet bed, Velocity profile, Bed shear stress, Large eddy simulation

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    Figure 3. Comparison of water surface profiles over porous media with 12 mm particle diameter in laboratory measurements (symbols) and numerical results (lines).

    ๋‹ค๊ณต์ธต์— ๋Œ€ํ•œ ๋Œ๋ฐœ ๋Œ ๋ถ•๊ดด์˜ 3์ฐจ์› ์œ ๋™ ์ˆ˜์น˜ํ•ด์„ ์‹œ๋ฎฌ๋ ˆ์ด์…˜

    A. Safarzadeh1*, P. Mohsenzadeh2, S. Abbasi3
    1 Professor of Civil Eng., Water Engineering and Mineral Waters Research Center, Univ. of Mohaghegh Ardabili,Ardabil, Iran
    2 M.Sc., Graduated of Civil-Hydraulic Structures Eng., Faculty of Eng., Univ. of Mohaghegh Ardabili, Ardabil, Iran
    3 M.Sc., Graduated of Civil -Hydraulic Structures Eng., Faculty of Eng., Univ. of Mohaghegh Ardabili, Ardabil, Iran Safarzadeh@uma.ac.ir

    Highlights

    ์œ ์ฒด ์ด๋™์— ์˜ํ•ด ์ƒ์„ฑ๋œ RBF๋Š” Ls-Dyna์—์„œ Fluent, ICFD ALE ๋ฐ SPH ๋ฐฉ๋ฒ•์œผ๋กœ ์‹œ๋ฎฌ๋ ˆ์ด์…˜๋˜์—ˆ์Šต๋‹ˆ๋‹ค.
    RBF์˜ ๊ณผ์˜ˆ์ธก์€ ์œ ์ฒด๊ฐ€ ๋ฉ”์ธ ๋„๋ฉ”์ธ์—์„œ ๊ณ ์†์œผ๋กœ ๋ถ„๋ฆฌ๋  ๋•Œ ๋ฐœ์ƒํ•ฉ๋‹ˆ๋‹ค.
    ์ด ๊ณผ์ž‰ ์˜ˆ์ธก์€ ์š”์†Œ ํฌ๊ธฐ, ์‹œ๊ฐ„ ๋‹จ๊ณ„ ํฌ๊ธฐ ๋ฐ ์œ ์ฒด ๋ชจ๋ธ์— ๋”ฐ๋ผ ๋‹ค๋ฆ…๋‹ˆ๋‹ค.
    ์œ ์ฒด ์„ฑ๋Šฅ์„ ๊ฒ€์ฆํ•˜๋ ค๋ฉด ์ตœ๋Œ€ RBF๋ณด๋‹ค ์ž„ํŽ„์Šค๊ฐ€ ๊ถŒ์žฅ๋ฉ๋‹ˆ๋‹ค.

    Abstract

    Dam break is a very important problem due to its effects on economy, security, human casualties and environmental consequences. In this study, 3D flow due to dam break over the porous substrate is numerically simulated and the effect of porosity, permeability and thickness of the porous bed and the water depth in the porous substrate are investigated. Classic models of dam break over a rigid bed and water infiltration through porous media were studied and results of the numerical simulations are compared with existing laboratory data. Validation of the results is performed by comparing the water surface profiles and wave front position with dam break on rigid and porous bed. Results showed that, due to the effect of dynamic wave in the initial stage of dam break, a local peak occurs in the flood hydrograph. The presence of porous bed reduces the acceleration of the flood wave relative to the flow over the solid bed and it decreases with the increase of the permeability of the bed. By increasing the permeability of the bed, the slope of the ascending limb of the flood hydrograph and the peak discharge drops. Furthermore, if the depth and permeability of the bed is such that the intrusive flow reaches the rigid substrate under the porous bed, saturation of the porous bed, results in a sharp increase in the slope of the flood hydrograph. The maximum values of the peak discharge at the end of the channel with porous bed occurred in saturated porous bed conditions.

    ๋Œ ๋ถ•๊ดด๋Š” ๊ฒฝ์ œ, ๋ณด์•ˆ, ์ธ๋ช… ํ”ผํ•ด ๋ฐ ํ™˜๊ฒฝ์  ์˜ํ–ฅ์œผ๋กœ ์ธํ•ด ๋งค์šฐ ์ค‘์š”ํ•œ ๋ฌธ์ œ์ž…๋‹ˆ๋‹ค. ๋ณธ ์—ฐ๊ตฌ์—์„œ๋Š” ๋‹ค๊ณต์„ฑ ๊ธฐ์žฌ์— ๋Œ€ํ•œ ๋Œ ํŒŒ๊ดด๋กœ ์ธํ•œ 3์ฐจ์› ์œ ๋™์„ ์ˆ˜์น˜์ ์œผ๋กœ ์‹œ๋ฎฌ๋ ˆ์ด์…˜ํ•˜๊ณ  ๋‹ค๊ณต์„ฑ ๊ธฐ์žฌ์˜ ๋‹ค๊ณต์„ฑ, ํˆฌ๊ณผ๋„ ๋ฐ ๋‹ค๊ณต์„ฑ ์ธต์˜ ๋‘๊ป˜ ๋ฐ ์ˆ˜์‹ฌ์˜ ์˜ํ–ฅ์„ ์กฐ์‚ฌํ•ฉ๋‹ˆ๋‹ค. ๋‹จ๋‹จํ•œ ๋ฐ”๋‹ฅ์— ๋Œ€ํ•œ ๋Œ ํŒŒ๊ดด ๋ฐ ๋‹ค๊ณต์„ฑ ๋งค์ฒด๋ฅผ ํ†ตํ•œ ๋ฌผ ์นจํˆฌ์˜ ๊ณ ์ „ ๋ชจ๋ธ์„ ์—ฐ๊ตฌํ•˜๊ณ  ์ˆ˜์น˜ ์‹œ๋ฎฌ๋ ˆ์ด์…˜ ๊ฒฐ๊ณผ๋ฅผ ๊ธฐ์กด ์‹คํ—˜์‹ค ๋ฐ์ดํ„ฐ์™€ ๋น„๊ตํ•ฉ๋‹ˆ๋‹ค. ๊ฒฐ๊ณผ ๊ฒ€์ฆ์€ ๊ฐ•์ฒด ๋ฐ ๋‹ค๊ณต์„ฑ ๋ฒ ๋“œ์—์„œ ๋Œ ํŒŒ๋‹จ๊ณผ ์ˆ˜๋ฉด ํ”„๋กœํŒŒ์ผ ๋ฐ ํŒŒ๋ฉด ์œ„์น˜๋ฅผ ๋น„๊ตํ•˜์—ฌ ์ˆ˜ํ–‰๋ฉ๋‹ˆ๋‹ค. ๊ทธ ๊ฒฐ๊ณผ ๋ŒํŒŒ๊ดด ์ดˆ๊ธฐ์˜ ๋™์ ํŒŒ๋™์˜ ์˜ํ–ฅ์œผ๋กœ ํ™์ˆ˜์ˆ˜๋ฌธ๊ณก์„ ์—์„œ ๊ตญ๋ถ€์ฒจ๋‘๊ฐ€ ๋ฐœ์ƒํ•˜๋Š” ๊ฒƒ์œผ๋กœ ๋‚˜ํƒ€๋‚ฌ๋‹ค. ๋‹ค๊ณต์„ฑ ๋ฒ ๋“œ์˜ ์กด์žฌ๋Š” ๊ณ ์ฒด ๋ฒ ๋“œ ์œ„์˜ ์œ ๋™์— ๋Œ€ํ•œ ํ™์ˆ˜ํŒŒ์˜ ๊ฐ€์†์„ ๊ฐ์†Œ์‹œํ‚ค๊ณ  ๋ฒ ๋“œ์˜ ํˆฌ๊ณผ์„ฑ์ด ์ฆ๊ฐ€ํ•จ์— ๋”ฐ๋ผ ๊ฐ์†Œํ•ฉ๋‹ˆ๋‹ค. ๋ฒ ๋“œ์˜ ํˆฌ์ˆ˜์„ฑ์„ ์ฆ๊ฐ€์‹œ์ผœ ํ™์ˆ˜ ์ˆ˜๋ฌธ๊ณก์„ ์˜ ์˜ค๋ฆ„์ฐจ์ˆœ ๊ฒฝ์‚ฌ์™€ ์ฒจ๋‘๋ฐฉ๋ฅ˜๋Ÿ‰์ด ๊ฐ์†Œํ•œ๋‹ค. ๋”์šฑ์ด, ๋งŒ์•ฝ ์ธต์˜ ๊นŠ์ด์™€ ํˆฌ๊ณผ์„ฑ์ด ๊ด€์ž… ์œ ๋™์ด ๋‹ค๊ณต์„ฑ ์ธต ์•„๋ž˜์˜ ๋‹จ๋‹จํ•œ ๊ธฐ์งˆ์— ๋„๋‹ฌํ•˜๋Š” ์ •๋„๋ผ๋ฉด, ๋‹ค๊ณต์„ฑ ์ธต์˜ ํฌํ™”๋Š” ํ™์ˆ˜ ์ˆ˜๋ฌธ๊ณก์„ ์˜ ๊ธฐ์šธ๊ธฐ์˜ ๊ธ‰๊ฒฉํ•œ ์ฆ๊ฐ€๋ฅผ ์ดˆ๋ž˜ํ•ฉ๋‹ˆ๋‹ค. ๋‹ค๊ณต์ธต์ด ์žˆ๋Š” ์ฑ„๋„์˜ ๋๋‹จ์—์„œ ์ตœ๋Œ€ ๋ฐฉ์ „ ํ”ผํฌ๊ฐ’์€ ํฌํ™” ๋‹ค๊ณต์ธต ์กฐ๊ฑด์—์„œ ๋ฐœ์ƒํ•˜์˜€๋‹ค.

    Keywords

    Keywords: Dams Break, 3D modeling, Porous Bed, Permeability, Flood wave

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    Fig. 6. Experiment of waves passing through a single block of porous medium.

    Generalization of a three-layer model for wave attenuation in n-block submerged porous breakwater

    NadhiraKarimaaIkhaMagdalenaabIndrianaMarcelaaMohammadFaridbaFaculty of Mathematics and Natural Sciences, Bandung Institute of Technology, 40132, IndonesiabCenter for Coastal and Marine Development, Bandung Institute of Technology, Indonesia

    Highlights

    โ€ขA new three-layer model for n-block submerged porous breakwaters is developed.

    โ€ขNew analytical approach in finding the wave transmission coefficient is presented.

    โ€ขA finite volume method successfully simulates the wave attenuation process.

    โ€ขPorous media blocks characteristics and configuration can optimize wave reduction.

    Abstract

    ๋†’์€ ํŒŒ๋„ ์ง„ํญ์€ ํ•ด์•ˆ์„ ์— ์œ„ํ—˜ํ•œ ์˜ํ–ฅ์„ ๋ฏธ์น˜๊ณ  ํ•ด์•ˆ ๋ณต์›๋ ฅ์„ ์•ฝํ™”์‹œํ‚ฌ ์ˆ˜ ์žˆ์Šต๋‹ˆ๋‹ค. ๊ทธ๋Ÿฌ๋‚˜ ๋‹ค์ค‘ ๋‹ค๊ณต์„ฑ ๋งค์ฒด๋Š” ํ•ด์–‘ ์ƒํƒœ๊ณ„์˜ ํ™˜๊ฒฝ ์นœํ™”์ ์ธ ํ•ด์•ˆ ๋ณดํ˜ธ ์—ญํ• ์„ ํ•  ์ˆ˜ ์žˆ์Šต๋‹ˆ๋‹ค.

    ์ด ๋…ผ๋ฌธ์—์„œ ์šฐ๋ฆฌ๋Š” n๊ฐœ์˜ ์ž ๊ธด ๋‹ค๊ณต์„ฑ ๋ฏธ๋””์–ด ๋ธ”๋ก์ด ์žˆ๋Š” ์˜์—ญ์—์„œ ํŒŒ๋™ ์ง„ํญ ๊ฐ์†Œ๋ฅผ ๊ณ„์‚ฐํ•˜๊ธฐ ์œ„ํ•ด 3์ธต ๊นŠ์ด ํ†ตํ•ฉ ๋ฐฉ์ •์‹์„ ์‚ฌ์šฉํ•ฉ๋‹ˆ๋‹ค. ์ˆ˜ํ•™์  ๋ชจ๋ธ์€ ํŒŒ๋™ ์ „๋‹ฌ ๊ณ„์ˆ˜๋ฅผ ์–ป๊ธฐ ์œ„ํ•ด ์—ฌ๋Ÿฌ ํ–‰๋ ฌ ๋ฐฉ์ •์‹์„ ํฌํ•จํ•˜๋Š” ๋ณ€์ˆ˜ ๋ถ„๋ฆฌ ๋ฐฉ๋ฒ•์„ ์‚ฌ์šฉํ•˜์—ฌ ํ•ด์„์ ์œผ๋กœ ํ•ด๊ฒฐ๋ฉ๋‹ˆ๋‹ค.

    ์ด ๊ณ„์ˆ˜๋Š” ์ง„ํญ ๊ฐ์†Œ์˜ ํฌ๊ธฐ์— ๋Œ€ํ•œ ์ •๋ณด๋ฅผ ์ œ๊ณตํ•ฉ๋‹ˆ๋‹ค. ๋˜ํ•œ ๋ชจ๋ธ์„ ์ˆ˜์น˜์ ์œผ๋กœ ํ’€๊ธฐ ์œ„ํ•ด ์ง€๊ทธ์žฌ๊ทธ ์œ ํ•œ ์ฒด์  ๋ฐฉ๋ฒ•์ด ์ ์šฉ๋ฉ๋‹ˆ๋‹ค.

    ์ˆ˜์น˜ ์‹œ๋ฎฌ๋ ˆ์ด์…˜์„ ํ†ตํ•ด ๋‹ค๊ณต์„ฑ ๋งค์งˆ ๋ธ”๋ก์˜ ๊ตฌ์„ฑ๊ณผ ํŠน์„ฑ์ด ํˆฌ๊ณผํŒŒ ์ง„ํญ์„ ์ค„์ด๋Š” ๋ฐ ์ค‘์š”ํ•˜๋‹ค๋Š” ๊ฒฐ๋ก ์„ ๋‚ด๋ ธ์Šต๋‹ˆ๋‹ค.

    High wave amplitudes may cause dangerous effects on the shoreline and weaken coastal resilience. However, multiple porous media can act as environmental friendly coastal protectors of the marine ecosystem. In this paper, we use three-layer depth-integrated equations to calculate wave amplitude reduction in a domain withย nย submerged porous media blocks. The mathematical model is solved analytically using the separation of variables method involving several matrix equations to obtain the wave transmission coefficient. This coefficient provides information about the magnitude of amplitude reduction. Additionally, a staggered finite volume method is applied to solve the model numerically. By conducting numerical simulations, we conclude that porous media blocksโ€™ configuration and characteristics are crucial in reducing transmitted wave amplitude.

    Keywords

    Three-layer equations, Submerged porous media, Wave transmission coefficient, Finite volume method

    Fig. 1. Sketch of the problem configuration.
    Fig. 1. Sketch of the problem configuration.
    Fig. 6. Experiment of waves passing through a single block of porous medium.
    Fig. 6. Experiment of waves passing through a single block of porous medium.

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    Figure 9. Turbulent kinetic energy (TKE) contour map on different sections.

    Numerical Simulation Research on the Diversion
    Characteristics of a Trapezoidal Channel

    Yong Cheng, Yude Song, Chunye Liu, Wene Wang * and Xiaotao Hu
    Key Laboratory of Agricultural Soil and Water Engineering in Arid and Semiarid Areas, Ministry of Education, Northwest A&F University, Yangling 712100, China

    • Correspondence: wangwene@nwsuaf.edu.cn

    Abstract

    ๊ฐœ๋ฐฉ ์ฑ„๋„ ๋ถ„๊ธฐ์ ์€ ๊ด€๊ฐœ ์ง€์—ญ์—์„œ ๊ฐ€์žฅ ์ผ๋ฐ˜์ ์ธ ๋ฌผ ์ „ํ™˜ ๊ตฌ์กฐ์ž…๋‹ˆ๋‹ค. ๊ด€๊ฐœ์šฉ์ˆ˜ ์šด๋ฐ˜์—์„œ๋Š” ๋ฌผ ์šด๋ฐ˜ ํšจ์œจ๊ณผ ์นจ์ „์ด ์ฃผ์š” ๊ด€์‹ฌ์‚ฌ์ž…๋‹ˆ๋‹ค. ๋”ฐ๋ผ์„œ ์ด ์—ฐ๊ตฌ๋Š” ๊ด€๊ฐœ ์ง€์—ญ์˜ ๋ฌผ ๊ณต๊ธ‰์— ๋Œ€ํ•œ ๊ฐœ๋ฐฉ ์ฑ„๋„ ๋ถ„๊ธฐ์ ์˜ ์˜ํ–ฅ์„ ๋ถ„์„ํ•ฉ๋‹ˆ๋‹ค.

    ์—ฌ๊ธฐ์—์„œ FLOW-3D ์†Œํ”„ํŠธ์›จ์–ด๋ฅผ ์‚ฌ์šฉํ•˜๊ณ  15 ์„ธํŠธ์˜ ์ž‘์—… ์กฐ๊ฑด์„ ํฌํ•จํ•˜๋Š” ์ˆ˜์น˜ ์‹œ๋ฎฌ๋ ˆ์ด์…˜์„ ํ†ตํ•ด ๊ฐœ๋ฐฉ ์ฑ„๋„ ๋ถ„๊ธฐ์ ์—์„œ์˜ 3์ฐจ์› ์œ ๋™์„ ์—ฐ๊ตฌํ–ˆ์Šต๋‹ˆ๋‹ค. ๊ฐœ์ˆ˜๋กœ ๋ถ„๊ธฐ์  ๋ถ€๊ทผ์˜ ์žฌ์ˆœํ™˜ ๊ตฌ์—ญ ๋ฐ ์œ ๋™ ๊ตฌ์กฐ์˜ ์ˆ˜๋ฆฌํ•™์  ํŠน์„ฑ์„ ๋ถ„์„ํ•˜์˜€๋‹ค.

    ๊ทธ๋Ÿฐ ๋‹ค์Œ ์‚ฌ๋‹ค๋ฆฌ๊ผด ์ฑ„๋„์—์„œ ํ‘œ๋ฉด ๋ฐ ๋ฐ”๋‹ฅ์ธต์˜ ํ๋ฆ„ ์ „ํ™˜ ํญ์— ๋Œ€ํ•œ ๋ฐฉ์ •์‹์„ ์–ป์—ˆ์Šต๋‹ˆ๋‹ค. ์ˆ˜์‹ฌ์— ๋”ฐ๋ฅธ ํ๋ฆ„ ์ „ํ™˜ ํญ์€ ์‚ฌ๋‹ค๋ฆฌ๊ผด ์ฑ„๋„๊ณผ ์ง์‚ฌ๊ฐํ˜• ์ฑ„๋„์—์„œ ๋‹ค๋ฅธ ๊ฒƒ์œผ๋กœ ๋‚˜ํƒ€๋‚ฌ์Šต๋‹ˆ๋‹ค. ๊ฒฐ๊ณผ๋Š” ๋˜ํ•œ ๊ฐœ๋ฐฉ ์ˆ˜๋กœ ๋ถ„๊ธฐ์ ์ด ์ฃผ ์ˆ˜๋กœ์˜ ์œ ์†์— ์ƒ๋‹นํ•œ ์˜ํ–ฅ์„ ๋ฏธ์นœ๋‹ค๋Š” ๊ฒƒ์„ ๋ณด์—ฌ์ค๋‹ˆ๋‹ค.

    ๊ฐœ๋ฐฉ ์ฑ„๋„ ๋ถ„๊ธฐ์ ์˜ ์žฌ์ˆœํ™˜ ์˜์—ญ์—์„œ์˜ ์œ ์†์€ ์ž‘์•˜์ง€๋งŒ ๋งฅ๋™ ์†๋„์™€ ๋‚œ๋ฅ˜ ์šด๋™ ์—๋„ˆ์ง€๋Š” ์ปธ๋‹ค. ์ด ์ง€์—ญ์—์„œ ์†Œ์‚ฐ๋˜๋Š” ์—๋„ˆ์ง€๋Š” ์ƒ๋Œ€์ ์œผ๋กœ ์ปค์„œ ์ˆ˜๋กœ ๋ฌผ ์ „๋‹ฌ์— ๋„์›€์ด ๋˜์ง€ ์•Š์•˜์Šต๋‹ˆ๋‹ค.

    ์ด ์—ฐ๊ตฌ๋Š” ๊ด€๊ฐœ๊ตฌ์—ญ์˜ ์ˆ˜๋กœ ์ตœ์ ํ™” ๋ฐ ์šด์˜ ๊ด€๋ฆฌ์— ๋Œ€ํ•œ ์ฐธ๊ณ  ์ž๋ฃŒ๋ฅผ ์ œ๊ณตํ•ฉ๋‹ˆ๋‹ค.

    Open-channel bifurcations are the most common water diversion structures in irrigation districts. In irrigation water conveyance, water transport efficiency and sedimentation are primary concerns. This study accordingly analyzes the influence of open-channel bifurcations on water delivery in irrigation areas. Herein, the three-dimensional flow at an open-channel bifurcation was studied via numerical simulations using FLOW-3D software and including 15 sets of working conditions. The hydraulic characteristics of the recirculation zone and flow structures in the vicinity of the open-channel bifurcation were analyzed. Equations for the flow diversion width of the surface and bottom layers in the trapezoidal channel were then obtained. The flow diversion widths along the water depth were found to differ between trapezoidal and rectangular channels. The results also show that open-channel bifurcations considerably influence the flow velocity in the main channel. The flow velocity in the recirculation zone of open-channel bifurcations was small, but the pulsation velocity and the turbulent kinetic energy were large. The energy dissipated in this area was relatively large, which was not conducive to channel water delivery. This study provides a reference for channel optimization and operation management in irrigation districts.

    Keywords

    trapezoidal open channel; numerical simulation; the recirculation zone; flow diversion
    width; turbulence kinetic energy

    Figure 1. Experimental plan and section measurement layout. Note: Red points in the figure represent the measurement point arrangement, and Roman numerals represent measurement section numbers.
    Figure 1. Experimental plan and section measurement layout. Note: Red points in the figure represent the measurement point arrangement, and Roman numerals represent measurement section numbers.
    Figure 5. Froude number (Fr) contour map at different water depths. Note: Q1 = 40 L/s; b = 30 cm. X* and Y* are obtained by dimensionless processing of X-axis and Y-axis coordinates. (a) depth of water below the sill height; (b) depth of water above the sill height.
    Figure 5. Froude number (Fr) contour map at different water depths. Note: Q1 = 40 L/s; b = 30 cm. X* and Y* are obtained by dimensionless processing of X-axis and Y-axis coordinates. (a) depth of water below the sill height; (b) depth of water above the sill height.
    Plunge pool scour and bank erosion: assessment of protection measures for Ilarion dam by physical and numerical modelling

    Plunge pool scour and bank erosion: assessment of protection measures for Ilarion dam by physical and numerical modelling

    Abstract

    130m ๋†’์ด์˜ Ilarion ๋Œ์€ ๊ทธ๋ฆฌ์Šค ๋ถ๋ถ€์˜ Aliakmon ๊ฐ•์— ๊ฑด์„ค๋˜์—ˆ์Šต๋‹ˆ๋‹ค. 2๊ฐœ์˜ ์—ฌ์ˆ˜๋กœ์—๋Š” ํ”Œ๋Ÿฐ์ง€ ํ’€์˜ ์ค‘์‹ฌ์„ ํ–ฅํ•ด ๊ณ ์† ์ œํŠธ๋ฅผ ๋น—๋‚˜๊ฐ€๊ฒŒ ํ•˜๋Š” ์Šคํ‚ค ์ ํ”„๊ฐ€ ์žฅ์ฐฉ๋˜์–ด ์žˆ์Šต๋‹ˆ๋‹ค. ์ตœ๊ทผ ๋ช‡ ๋…„ ๋™์•ˆ ๋‘ ๋ฒˆ์˜ ์ฃผ์š” ํ™์ˆ˜ ๋™์•ˆ ์ˆ˜์˜์žฅ์—์„œ ์ƒ๋‹นํ•œ ์ˆ˜์ค‘ ์ž‘์—…์ด ๋ฐœ์ƒํ–ˆ์Šต๋‹ˆ๋‹ค.

    ์‹ ๋ขฐํ•  ์ˆ˜ ์žˆ๋Š” ๋ณดํ˜ธ ์กฐ์น˜๋ฅผ ์กฐ์‚ฌํ•˜๊ธฐ ์œ„ํ•ด FLOW-3Dยฎ๋ฅผ ์‚ฌ์šฉํ•˜์—ฌ 1:55 ์Šค์ผ€์ผ ๋ฌผ๋ฆฌ์  ๋ชจ๋ธ๊ณผ ์ˆ˜์น˜ ๋ชจ๋ธ์„ ๋งŒ๋“ค์—ˆ์Šต๋‹ˆ๋‹ค. ํ”Œ๋Ÿฐ์ง€ ํ’€๊ณผ ์—ฌ์ˆ˜๋กœ์—์„œ์˜ ์œ ์ฒด์—ญํ•™์  ๊ฑฐ๋™๊ณผ ์ œํŠธ์˜ ๊ถค์ ์„ ๊ฒฐ์ •ํ•  ์ˆ˜ ์žˆ์—ˆ์Šต๋‹ˆ๋‹ค.

    ์ˆ˜์น˜ ๋ชจ๋ธ์€ ํ”Œ๋Ÿฐ์ง€ ํ’€์˜ ํ๋ฆ„์ด ๊ณ ๋„๋กœ ๋น„๋Œ€์นญ์ด๊ณ  ๋‘ ๊ฐœ์˜ ๋ฐฐ์ˆ˜๋กœ ์ค‘ ํ•˜๋‚˜๋งŒ ์žˆ๋Š” ํšŒ์ „ ํ๋ฆ„์ด ์ž‘๋™ํ•œ๋‹ค๋Š” ๊ฒƒ์„ ๋ณด์—ฌ์ฃผ์—ˆ์Šต๋‹ˆ๋‹ค.

    ์ด ํšŒ์ „ ํ๋ฆ„์€ ์—ฌ์ˆ˜๋กœ์˜ ํ๋ฆ„ ์†๋„๋ณด๋‹ค 3๋ฐฐ ๋” ํฐ ๊ตญ๋ถ€์ ์œผ๋กœ ํšจ๊ณผ์ ์ธ ํ๋ฆ„ ์†๋„๋ฅผ ์ดˆ๋ž˜ํ•ฉ๋‹ˆ๋‹ค. ์‹œ๋ฎฌ๋ ˆ์ด์…˜์„ ํ†ตํ•ด ์ด ๋ฌธ์ œ์— ๋Œ€ํ•œ ํ•œ ๊ฐ€์ง€ ํ•ด๊ฒฐ์ฑ…์€ ๋‘ ๋ฐฉ์ˆ˜๋กœ์˜ ๋Œ€์นญ ์ž‘๋™์ž„์„ ํ™•์ธํ–ˆ์Šต๋‹ˆ๋‹ค.

    The 130 m high Ilarion Dam is built on the Aliakmon River in northern Greece. Its two spillways are equipped with ski jumps to deflect high-velocity jets towards the centre of the plunge pool. Significant scouring occurred in the pool during two major floods in recent years. To investigate reliable protection measures, a 1:55 scale physical model and a numerical model with FLOW-3Dยฎ were created. The hydrodynamic behaviour of the flow in the plunge pool and in the spillways as well as the trajectory of the jets could be determined. The numerical model showed, that the flow in the plunge pool is highly asymmetric and a rotational flow forms with only one of the two spillways is operational. This rotational flow results in locally effective flow rates three times greater than the flow rate from the spillway. Simulations confirm, that one solution to this problem is the symmetrical operation of both spillways.

    Details

    TitlePlunge pool scour and bank erosion: assessment of protection measures for Ilarion dam by physical and numerical modelling

    Author(s)Van Mol, Romain Nathan Hippolyte Merlin ; Mรถrtl, Christian ; Amini, Azin ; Siachou, Sofia Schleiss, Anton ; De Cesare, Giovanni

    Published inProceedings of HYDRO 2022 Conference

    Pagination9

    PagesPaper 27.02

    ConferenceHYDRO 2022 Conference, Strasbourg, France, April 25-27, 2022

    Date2022

    Keywords

    scourplunge poolspillwaynumerical modellingFLOW-3D

    Note[1390]

    LaboratoriesLCH
    PL-LCH

    Record Appears inScientific production and competences > ENAC – School of Architecture, Civil and Environmental Engineering > IIC – Civil Engineering Institute > PL-LCH – Hydraulic Constructions Platform
    Scientific production and competences > ENAC – School of Architecture, Civil and Environmental Engineering > IIC – Civil Engineering Institute > LCH – Hydraulic Constructions Laboratory
    Peer-reviewed publications
    Conference Papers
    Work produced at EPFL

    Record creation date2022-09-14

    Figure 1 Mitochondrial Weir Dam

    The Three-dimensional Simulation of Granular
    Mixtures Weir

    Shen Zhen-dong*1, 2, Zhang Yang1, 2
    1Zhejiang Guangchuan Engineering Consultation Co., Ltd., Hangzhou, 310020,
    Zhejiang, China
    2Zhejiang Institute of Hydraulics &Estuary, Hangzhou 310020, Zhejiang, China
    E-mail: zdshen1991@126.com

    Abstract

    ์ตœ๊ทผ ๋ช‡ ๋…„ ๋™์•ˆ ์ƒํƒœํ•™์  ์ˆ˜์ž์› ๋ณด์กด ๊ณตํ•™์˜ ๋ฐœ์ „์œผ๋กœ ๋งŽ์€ ์ƒˆ๋กœ์šด ๋Œ ๋””์ž์ธ์ด ๋“ฑ์žฅํ–ˆ์Šต๋‹ˆ๋‹ค. ๋ณธ ๋…ผ๋ฌธ์—์„œ๋Š” ์ฒด๊ณ„์ ์ธ ์†Œ๋ฉด๋ณด ์—ฐ๊ตฌ์™€ ์กฐ์‚ฌ๋ฅผ ๋ฐ”ํƒ•์œผ๋กœ ์ƒˆ๋กœ์šด ์ข…๋ฅ˜์˜ ์ž…์ƒ ํ˜ผํ•ฉ๋ฌผ ์œ„์–ด๋ฅผ ์ œ์‹œํ•˜์˜€์Šต๋‹ˆ๋‹ค.

    ์ž…์ƒ๋ณด์˜ ์ˆ˜์น˜ํ•ด์„์€ Flow-3D๋ฅผ ์ด์šฉํ•˜์—ฌ ์ˆ˜ํ–‰ํ•˜์˜€์œผ๋ฉฐ, ๊ทธ ๊ฒฐ๊ณผ๋ฅผ ๋ฌผ๋ฆฌ์  ๋ชจ๋ธ ์‹คํ—˜๊ฒฐ๊ณผ์™€ ๋น„๊ตํ•˜์˜€์Šต๋‹ˆ๋‹ค. ์œ ์†, ์œ ์† ๋ถ„ํฌ ๋ฐ ๋‘‘์˜ ํŒŒ์†์— ๋Œ€ํ•œ ์ˆ˜์น˜ ์‹œ๋ฎฌ๋ ˆ์ด์…˜ ๊ฒฐ๊ณผ๋Š” ์‹คํ—˜ ๊ฒฐ๊ณผ์™€ ์ž˜ ์ผ์น˜ํ•˜๋ฉฐ, ์ด๋Š” 3์ฐจ์› ์ˆ˜ํ•™์  ๋ชจ๋ธ์ด ๋ฌผ๋ฆฌ์  ๋ชจ๋ธ ์‹คํ—˜๊ณผ ๊ฒฐํ•ฉ๋˜์–ด ๋ชจ๋“  ์ž…์ƒ ํ˜ผํ•ฉ๋ฌผ ๋‘‘์„ ์‹œ๋ฎฌ๋ ˆ์ด์…˜ํ•  ์ˆ˜ ์žˆ์Œ์„ ๋‚˜ํƒ€๋ƒ…๋‹ˆ๋‹ค.

    ์ด ๋ฐฉ๋ฒ•์„ ์ด์šฉํ•˜์—ฌ ํŠน์„ฑ ๋ฐ ์ˆ˜๋ฆฌํ•™์  ๋งค๊ฐœ๋ณ€์ˆ˜๋ฅผ ๋ถ„์„ํ•˜๋ฉด ์ƒํƒœ๋ณด์˜ ํ›„์† ์—ฐ๊ตฌ๋ฅผ ์œ„ํ•œ ๊ธฐ์ˆ ์  ์ง€์›์„ ์ œ๊ณตํ•  ์ˆ˜ ์žˆ์Šต๋‹ˆ๋‹ค.

    In recent years, with the development of ecological water conservancy engineering,
    many new weir designs have also emerged. This paper has put forward a new kind of granular
    mixtures weir based on the systematic carding weir researches, combined with investigation. The
    numerical simulation of granular weir is carried out by using Flow-3D,and the results are
    compared with the physical model experiment results. The numerical simulation results of the
    flow velocity, flow distribution and the failure of the weir are in good agreement with the
    experimental results, which indicates that the 3-D mathematical model can be combined with
    physical model experiments to simulate the granular mixtures weir in all directions. Using this
    method to analysis the characteristics and hydraulic parameters can provide technical support
    for the follow-up research of ecological weir.

    Figure 1 Mitochondrial Weir Dam
    Figure 1 Mitochondrial Weir Dam
    Table 1 Numerical simulation programme table
    Table 1 Numerical simulation programme table
    Figure 4 Final Damage of Weir in Different Projects
    Figure 4 Final Damage of Weir in Different Projects

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    Fig. 9. Simulated separation regions for surface mounted cylinder

    Investigation on the Local Scour Beneath Piggyback Pipelines Under Clear-Water Conditions

    China Ocean Engineering volume 35, pages422โ€“431 (2021)Cite this article

    Abstract

    ํ”ผ๊ธฐ๋ฐฑ ํŒŒ์ดํ”„๋ผ์ธ์€ 2๊ฐœ์˜ ํŒŒ์ดํ”„๋กœ ๊ตฌ์„ฑ๋˜์–ด 2์ฐจ ๋ผ์ธ์ด 2๊ฐœ์˜ ํŒŒ์ดํ”„ ์‚ฌ์ด์˜ ๊ธธ์ด๊ฐ€ ๊ณ ์ •๋œ ๊ฑฐ๋ฆฌ๋กœ ๋ฉ”์ธ ํŒŒ์ดํ”„์— ํƒ‘์Šนํ•ฉ๋‹ˆ๋‹ค. ์ƒˆ๋กœ์šด ์ „๋žต์€ ๋‹จ์ผ ํ๋ฆ„ ๋ผ์ธ ๋Œ€์‹  ์—ฐ์•ˆ ์ง€์—ญ์—์„œ ํ™œ์šฉ๋ฉ๋‹ˆ๋‹ค.

    ์ด์™€ ๊ด€๋ จํ•˜์—ฌ ์ •์ƒ ์ „๋ฅ˜์—์„œ ํ”ผ๊ธฐ๋ฐฑ ํŒŒ์ดํ”„๋ผ์ธ ์•„๋ž˜์˜ ์„ธ๊ตด ํšจ๊ณผ๋ฅผ ์กฐ์‚ฌํ•˜๋Š” ์‹คํ—˜ ๋ฐ ์ˆ˜์น˜ ์—ฐ๊ตฌ๋Š” ์†Œ์ˆ˜์— ๋ถˆ๊ณผํ•ฉ๋‹ˆ๋‹ค. ๋”ฐ๋ผ์„œ ๋ณธ ์—ฐ๊ตฌ์—์„œ๋Š” ์ˆ˜์น˜๋ชจ์‚ฌ ๋ฐ ์‹คํ—˜์  ์‹คํ—˜์„ ํ†ตํ•ด ๊ด€์ง๊ฒฝ, ๊ด€๊ฐ„๊ฒฉ ๋“ฑ ์ •๋ฅ˜์— ์˜ํ•œ ์„ธ๊ตด์— ์˜ํ–ฅ์„ ๋ฏธ์น˜๋Š” ์š”์ธ์„ ์‚ดํŽด๋ณด๊ณ ์ž ํ•ฉ๋‹ˆ๋‹ค.

    ๋”ฐ๋ผ์„œ ์—ฐ๊ตฌ์˜ ์ฒซ ๋ฒˆ์งธ ๋‹จ๊ณ„์—์„œ ๋‹จ์ผ ํŒŒ์ดํ”„๋ฅผ ์„ค์น˜ํ•˜๊ณ  ์‹คํ—˜์‹์˜ ๊ฒฐ๊ณผ์™€ ๊ฒฐ๊ณผ๋ฅผ ๋น„๊ตํ•˜๊ธฐ ์œ„ํ•ด ์‹คํ—˜์‹ค์—์„œ ํ…Œ์ŠคํŠธํ–ˆ์Šต๋‹ˆ๋‹ค. ์‹คํ—˜์  ๊ฒ€์ฆ์„ ๋งˆ์นœ ํ›„, ํ”ผ๊ธฐ๋ฐฑ ํŒŒ์ดํ”„๋ผ์ธ๋„ ์กฐ๋ฆฝํ•˜์—ฌ ์•ˆ์ •๋œ ์ „๋ฅ˜ ์กฐ๊ฑด์—์„œ ์ •๋ จ์„ ์—ฐ๊ตฌํ–ˆ์Šต๋‹ˆ๋‹ค. ํŒŒ์ดํ”„ ์‚ฌ์ด์˜ ๊ฐ„๊ฒฉ์„ ๋Š˜๋ฆฌ๋ฉด ์ตœ๋Œ€ ์„ธ๊ตด ๊นŠ์ด๊ฐ€ ๊ฐ์†Œํ•œ๋‹ค๋Š” ๊ฒฐ๋ก ์ด ๋‚ด๋ ค์กŒ์Šต๋‹ˆ๋‹ค.

    ๊ทธ๋Ÿฌ๋‚˜ ์ž‘์€ ํŒŒ์ดํ”„์˜ ์ง๊ฒฝ์ด ์ฆ๊ฐ€ํ•˜๋ฉด ์ตœ๋Œ€ ์„ธ๊ตด ๊นŠ์ด๊ฐ€ ์ปค์ง‘๋‹ˆ๋‹ค. ๋‘˜์งธ, ๋ณธ ์—ฐ๊ตฌ์˜ ์ˆ˜์น˜์  ์กฐ์‚ฌ์— ์ ํ•ฉํ•œ ๋„๊ตฌ์ธ FLOW-3D ์†Œํ”„ํŠธ์›จ์–ด๋ฅผ ์‚ฌ์šฉํ•˜์—ฌ ์ˆ˜์น˜ํ•ด์„์„ ์ˆ˜ํ–‰ํ•˜์˜€์Šต๋‹ˆ๋‹ค.

    ๋งˆ์ง€๋ง‰์œผ๋กœ, ์ˆ˜์น˜ ๊ฒฐ๊ณผ๋ฅผ ํ•ด๋‹น ์‹คํ—˜ ๋ฐ์ดํ„ฐ์™€ ๋น„๊ตํ–ˆ์œผ๋ฉฐ, ์ด๋“ค ์‚ฌ์ด์— ๋น„๊ต์  ์ข‹์€ ์ผ์น˜๊ฐ€ ๋‹ฌ์„ฑ๋˜์—ˆ์Šต๋‹ˆ๋‹ค.

    A piggyback pipeline consists of two pipes such that the secondary line rides on the main pipe with a fixed distance between two pipes in length. The novel strategy is utilized in offshore areas instead of a single flow line. In this regard, there are only a handful of experimental and numerical studies investigating the effect of scour below a piggyback pipeline under steady current. Hence, this study focuses on examining the influential factors on scouring due to steady current including the pipe diameter and the gap between pipes through numerical simulations and experimental tests. Accordingly, at the first phase of the research, a single pipe was established and tested in laboratory to compare the results with those of an empirical equation. After finishing experimental verifications, piggyback pipelines were also assembled to study the scouring under steady current conditions. It was concluded that by increasing the gap distance between the pipes, the maximum scour depth decreases; however, an increase in the small pipeโ€™s diameter results in a larger maximum scour depth. Secondly, numerical simulations were carried out using the FLOW-3D software which was found to be a suitable tool for the numerical investigation of this study. Finally, the numerical results have been compared with the corresponding experimental data and a relatively good agreement was achieved between them.

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    Fig. 1.   (a) Arrangement of piggyback pipeline, (b) Plan view of experimental flume.
    Fig. 1. (a) Arrangement of piggyback pipeline, (b) Plan view of experimental flume.
    Fig. 3.   Initial photos of two mounted piggyback pipelines in experimental setup for d/D=0.25.
    Fig. 3. Initial photos of two mounted piggyback pipelines in experimental setup for d/D=0.25.
    Fig. 9.     Simulated  separation  regions  for  surface  mounted  cylinder
    Fig. 9. Simulated separation regions for surface mounted cylinder

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    Flow Field in a Sloped Channel with Damaged and Undamaged Piers: Numerical and Experimental Studies

    Flow Field in a Sloped Channel with Damaged and Undamaged Piers: Numerical and Experimental Studies

    Ehsan Oveici,ย Omid Tayariย &ย Navid Jalalkamali
    KSCE Journal of Civil Engineeringย volumeย 25,ย pages4240โ€“4251 (2021)Cite this article

    Abstract

    ๋ณธ ๋…ผ๋ฌธ์€ ๊ฒฝ์‚ฌ๊ฐ€ ์™„๋งŒํ•œ ์ˆ˜๋กœ์—์„œ ์†์ƒ๋˜๊ฑฐ๋‚˜ ์†์ƒ๋˜์ง€ ์•Š์€ ๊ต๊ฐ ์ฃผ๋ณ€์˜ ์œ ๋™ ํŒจํ„ด์„ ๋ถ„์„ํ–ˆ์Šต๋‹ˆ๋‹ค. ์‹คํ—˜์€ ๊ธธ์ด๊ฐ€ 12m์ด๊ณ  ๊ธฐ์šธ๊ธฐ๊ฐ€ 0.008์ธ ์ง์„  ์ˆ˜๋กœ์—์„œ ์ˆ˜ํ–‰๋˜์—ˆ์Šต๋‹ˆ๋‹ค. Acoustic Doppler Velocimeter(ADV)๋ฅผ ์ด์šฉํ•˜์—ฌ 3์ฐจ์› ์œ ์† ๋ฐ์ดํ„ฐ๋ฅผ ์ˆ˜์ง‘ํ•˜์˜€๊ณ , ๊ทธ ๊ฒฐ๊ณผ๋ฅผ PIV(Particle Image Velocimetry) ๋ฐ์ดํ„ฐ์™€ ๋ถ„์„ํ•˜์—ฌ ๋น„๊ตํ•˜์˜€์Šต๋‹ˆ๋‹ค.

    ๋‹ค์ค‘ ๋ธ”๋ก ์˜ต์…˜์ด ์žˆ๋Š” ์ทจ์ˆ˜๊ตฌ์˜ ํ‡ด์ ๋ฌผ ์‹œ๋ฎฌ๋ ˆ์ด์…˜(SSIIM)์€ ์ด ์—ฐ๊ตฌ์—์„œ ํ๋ฆ„์˜ ์ˆ˜์น˜ ์‹œ๋ฎฌ๋ ˆ์ด์…˜์„ ์œ„ํ•ด ํ†ตํ•ฉ๋˜์—ˆ์Šต๋‹ˆ๋‹ค. ์ผ๋ฐ˜์ ์œผ๋กœ ๋น„๊ต์—์„œ ์–ป์€ ๊ฒฐ๊ณผ๋Š” ์ˆ˜์น˜ ๋ฐ์ดํ„ฐ์™€ ์‹คํ—˜ ๋ฐ์ดํ„ฐ ๊ฐ„์˜ ์ ์ ˆํ•œ ์ผ์น˜๋ฅผ ๋‚˜ํƒ€๋ƒ…๋‹ˆ๋‹ค. ๊ฒฐ๊ณผ๋Š” ๋ชจ๋“  ๊ฒฝ์šฐ์— ์ˆ˜๋กœ ์ž…๊ตฌ์—์„œ 2m ๊ฑฐ๋ฆฌ์—์„œ ๊ธฐ๋ณต์  ์ˆ˜์•• ์ ํ”„๊ฐ€ ๋ฐœ์ƒํ–ˆ์Œ์„ ๋ณด์—ฌ์ฃผ์—ˆ์Šต๋‹ˆ๋‹ค.

    ๊ฒฝ์‚ฌ์ง„ ์ˆ˜๋กœ์˜ ์ตœ๋Œ€ ๋ฒ ๋“œ ์ „๋‹จ์‘๋ ฅ์€ 2๊ฐœ์˜ ์†์ƒ ๋ฐ ์†์ƒ๋˜์ง€ ์•Š์€ ๊ต๊ฐ์„ ์„ค์น˜ํ•˜๊ธฐ ์œ„ํ•œ ์ˆ˜ํ‰ ์ˆ˜๋กœ์˜ 12๋ฐฐ์˜€์Šต๋‹ˆ๋‹ค. ์ด์™€ ๊ฐ™์€ ๊ฒฝ์‚ฌ์ˆ˜๋กœ ๊ต๊ฐ์˜ ์œ„์น˜์— ๋”ฐ๋ผ ์ƒ๋ฅ˜์ธก ์ˆ˜์œ„๋Š” ์ˆ˜ํ‰์ˆ˜๋กœ์˜ ์œ ์‚ฌํ•œ ์กฐ๊ฑด์— ๋น„ํ•ด 72.5% ๊ฐ์†Œํ•œ ๋ฐ˜๋ฉด, ์ด ๊ฐ์†Œ๋Ÿ‰์€ ๊ฒฝ์‚ฌ๋ฉด์—์„œ ๋‹ค๋ฅธ ๊ฒฝ์šฐ์— ๋น„ํ•ด 8.3% ๊ฐ์†Œํ•˜์˜€๋‹ค. ์ฑ„๋„ ๋˜ํ•œ ๋‘ ๊ต๊ฐ์ด ์žˆ๋Š” ๊ฒฝ์šฐ ์ตœ๋Œ€ Froude ์ˆ˜๋Š” ์ˆ˜ํ‰ ์ˆ˜๋กœ์˜ 5.7๋ฐฐ์˜€์Šต๋‹ˆ๋‹ค.

    This paper analyzed the flow pattern around damaged and undamaged bridge piers in a channel with a mild slope. The experiments were carried out on a straight channel with a length of 12 meters and a slope of 0.008. Acoustic Doppler velocimeter (ADV) was employed to collect three-dimensional flow velocity data, and the results were analyzed and compared with particle image velocimetry (PIV) data. Sediment Simulation in Intakes with Multiblock option (SSIIM) was incorporated for the numerical simulation of the flow in this study. Generally, the results obtained from the comparisons referred to the appropriate agreement between the numerical and the experimental data. The results showed that an undular hydraulic jump occurred at a distance of two meters from the channel entrance in every case; the maximum bed shear stress in the sloped channel was 12 times that in a horizontal channel for installing two damaged and undamaged piers. With this position of the piers in the sloped channel, the upstream water level underwent a 72.5% reduction compared to similar conditions in a horizontal channel, while the amount of this water level decrease was equal to 8.3% compared to the other cases in a sloped channel. In addition, with the presence of both piers, the maximum Froude number was 5.7 times that in a horizontal channel.

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    References

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    ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ์˜ํ–ฅ ์ตœ์†Œํ™”๋ฅผ ์œ„ํ•œ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ์ตœ์  ํ™œ์šฉ๋ฐฉ์•ˆ ๊ฒ€ํ† 

    The Optimal Operation on Auxiliary Spillway to Minimize the Flood Damage in Downstream River with Various Outflow Conditions

    ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ์˜ํ–ฅ ์ตœ์†Œํ™”๋ฅผ ์œ„ํ•œ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ์ตœ์  ํ™œ์šฉ๋ฐฉ์•ˆ ๊ฒ€ํ† 

    Hyung Ju Yoo1, Sung Sik Joo2, Beom Jae Kwon3, Seung Oh Lee4*

    ์œ  ํ˜•์ฃผ1, ์ฃผ ์„ฑ์‹2, ๊ถŒ ๋ฒ”์žฌ3, ์ด ์Šน์˜ค4*

    1Ph.D Student, Dept. of Civil & Environmental Engineering, Hongik University
    2Director, Water Resources & Environment Department, HECOREA
    3Director, Water Resources Department, ISAN
    4Professor, Dept. of Civil & Environmental Engineering, Hongik University

    1ํ™์ต๋Œ€ํ•™๊ต ๊ฑด์„คํ™˜๊ฒฝ๊ณตํ•™๊ณผ ๋ฐ•์‚ฌ๊ณผ์ •
    2ใˆœํ—ฅ์ฝ”๋ฆฌ์•„ ์ˆ˜์ž์›ํ™˜๊ฒฝ์‚ฌ์—…๋ถ€ ์ด์‚ฌ
    3ใˆœ์ด์‚ฐ ์ˆ˜์ž์›๋ถ€ ์ด์‚ฌ
    4ํ™์ต๋Œ€ํ•™๊ต ๊ฑด์„คํ™˜๊ฒฝ๊ณตํ•™๊ณผ ๊ต์ˆ˜

    ABSTRACT

    ์ตœ๊ทผ ๊ธฐํ›„๋ณ€ํ™”๋กœ ์ธํ•ด ๊ฐ•์šฐ๊ฐ•๋„ ๋ฐ ๋นˆ๋„์˜ ์ฆ๊ฐ€์— ๋”ฐ๋ฅธ ์ง‘์ค‘ํ˜ธ์šฐ์˜ ์˜ํ–ฅ ๋ฐ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์˜ ๋…ธํ›„ํ™”์— ๋Œ€๋น„ํ•˜์—ฌ ํ™์ˆ˜ ์‹œ ํ•˜๋ฅ˜ ํ•˜์ฒœ์˜ ์˜ํ–ฅ์„ ์ตœ์†Œํ™”ํ•  ์ˆ˜ ์žˆ๋Š” ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ํ™œ์šฉ๋ฐฉ์•ˆ ๊ตฌ์ถ•์ด ํ•„์š”ํ•œ ์‹ค์ •์ด๋‹ค. ์ด๋ฅผ ์œ„ํ•ด, ์ˆ˜๋ฆฌ๋ชจํ˜• ์‹คํ—˜ ๋ฐ ์ˆ˜์น˜๋ชจํ˜• ์‹คํ—˜์„ ํ†ตํ•˜์—ฌ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ์šด์˜์— ๋”ฐ๋ฅธ ํ๋ฆ„ํŠน์„ฑ ๋ณ€ํ™” ๊ฒ€ํ† ์— ๊ด€ํ•œ ์—ฐ๊ตฌ๊ฐ€ ๋งŽ์ด ์ง„ํ–‰๋˜์–ด ์™”๋‹ค. ๊ทธ๋Ÿฌ๋‚˜ ๋Œ€๋ถ€๋ถ„์˜ ์—ฐ๊ตฌ๋Š” ์—ฌ์ˆ˜๋กœ์—์„œ์˜ ํ๋ฆ„ํŠน์„ฑ ๋ฐ ๊ธฐ๋Šฅ์„ฑ์— ๋Œ€ํ•œ ๊ฒ€ํ† ๋ฅผ ์ˆ˜ํ–‰ํ•˜์˜€์„ ๋ฟ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ํ™œ์šฉ๋ฐฉ์•ˆ์— ๋”ฐ๋ฅธ ํ•˜๋ฅ˜ํ•˜์ฒœ ์˜ํ–ฅ ๊ฒ€ํ†  ๋ฐ ํ˜ธ์•ˆ ์•ˆ์ •์„ฑ ๊ฒ€ํ† ์— ๊ด€ํ•œ ์—ฐ๊ตฌ๋Š” ๋ฏธ๋น„ํ•œ ์‹ค์ •์ด๋‹ค. ์ด์— ๋ณธ ์—ฐ๊ตฌ์—์„œ๋Š” ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ ๋ฐ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜ ์กฐ๊ฑด์— ๋”ฐ๋ฅธ ํ•˜๋ฅ˜์˜ํ–ฅ ๋ถ„์„ ๋ฐ ํ˜ธ์•ˆ ์•ˆ์ •์„ฑ ์ธก๋ฉด์—์„œ ์ตœ์  ๋ฐฉ๋ฅ˜ ์‹œ๋‚˜๋ฆฌ์˜ค ๊ฒ€ํ† ๋ฅผ 3์ฐจ์› ์ˆ˜์น˜๋ชจํ˜•์ธ FLOW-3D๋ฅผ ์‚ฌ์šฉํ•˜์—ฌ ๊ฒ€ํ† ํ•˜์˜€๋‹ค. ๋˜ํ•œ FLOW-3D ์ˆ˜์น˜๋ชจ์˜ ์ˆ˜ํ–‰์„ ํ†ตํ•œ ์œ ์†, ์ˆ˜์œ„ ๊ฒฐ๊ณผ์™€ ์†Œ๋ฅ˜๋ ฅ ์‚ฐ์ • ๊ฒฐ๊ณผ๋ฅผ ํ˜ธ์•ˆ ์„ค๊ณ„ํ—ˆ์šฉ ๊ธฐ์ค€๊ณผ ๋น„๊ตํ•˜์˜€๋‹ค. ์ˆ˜๋ฌธ ์™„์ „ ๊ฐœ๋„ ์กฐ๊ฑด์œผ๋กœ ๊ฐ€์ •ํ•˜๊ณ  ๊ณ„ํšํ™์ˆ˜๋Ÿ‰ ์œ ์ž… ์‹œ ๋‹ค์–‘ํ•œ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ํ™œ์šฉ๋ฐฉ์•ˆ์— ๋Œ€ํ•˜์—ฌ ์ˆ˜์น˜๋ชจ์˜๋ฅผ ์ˆ˜ํ–‰ํ•œ ๊ฒฐ๊ณผ, ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ๋‹จ๋… ์šด์˜ ์‹œ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ ๋‹จ๋…์šด์˜์— ๋น„ํ•˜์—ฌ ์ตœ๋Œ€์œ ์† ๋ฐ ์ตœ๋Œ€ ์ˆ˜์œ„์˜ ๊ฐ์†Œํšจ๊ณผ๋ฅผ ํ™•์ธํ•˜์˜€๋‹ค. ๋‹ค๋งŒ ๊ณ„ํšํ™์ˆ˜๋Ÿ‰์˜ 45% ์ดํ•˜ ๋ฐฉ๋ฅ˜ ์กฐ๊ฑด์—์„œ ๋Œ€์•ˆ๋ถ€์˜ ํ˜ธ์•ˆ ์•ˆ์ •์„ฑ์„ ํ™•๋ณดํ•˜์˜€๊ณ  ํ•ด๋‹น ๋ฐฉ๋ฅ˜๋Ÿ‰ ์ดˆ๊ณผ ๊ฒฝ์šฐ์—๋Š” ์ฒ˜์˜ค๋ฆ„ ํ˜„์ƒ์ด ๋ฐœ์ƒํ•˜์—ฌ ์›”๋ฅ˜์— ๋Œ€ํ•œ ์œ„ํ—˜์„ฑ ์ฆ๊ฐ€๋ฅผ ํ™•์ธํ•˜์˜€๋‹ค. ๋”ฐ๋ผ์„œ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€์˜ ๋™์‹œ ์šด์˜ ๋ฐฉ์•ˆ ๋„์ถœ์ด ์ค‘์š”ํ•˜๋‹ค๊ณ  ํŒ๋‹จํ•˜์˜€๋‹ค. ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฐ๋ถ„ ๋น„์œจ ๋ฐ ์ด ํ—ˆ์šฉ ๋ฐฉ๋ฅ˜๋Ÿ‰์— ๋Œ€ํ•˜์—ฌ ๊ฒ€ํ† ํ•œ ๊ฒฐ๊ณผ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฉ๋ฅ˜๋Ÿ‰์ด ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฉ๋ฅ˜๋Ÿ‰๋ณด๋‹ค ํฐ ๊ฒฝ์šฐ ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ํ๋ฆ„์ด ์ค‘์‹ฌ์œผ๋กœ ์ง‘์ค‘๋˜์–ด ๋Œ€์•ˆ๋ถ€์˜ ์œ ์† ์ €๊ฐ ๋ฐ ์ˆ˜์œ„ ๊ฐ์†Œ๋ฅผ ํ™•์ธํ•˜์˜€๊ณ , ๊ณ„ํš ํ™์ˆ˜๋Ÿ‰์˜ 77% ์ดํ•˜์˜ ์กฐ๊ฑด์—์„œ ํ˜ธ์•ˆ์˜ ํ—ˆ์šฉ ์œ ์† ๋ฐ ํ—ˆ์šฉ ์†Œ๋ฅ˜๋ ฅ ์กฐ๊ฑด์„ ๋งŒ์กฑํ•˜์˜€๋‹ค. ์ด๋ฅผ ํ†ตํ•˜์—ฌ ๋ณธ ์—ฐ๊ตฌ์—์„œ ์ œ์•ˆํ•œ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ํ™œ์šฉ๋ฐฉ์•ˆ์œผ๋กœ๋Š” ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€ ๋™์‹œ ์šด์˜ ์‹œ ์ด ๋ฐฉ๋ฅ˜๋Ÿ‰์— ๋Œ€ํ•˜์—ฌ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฐ๋ถ„๋Ÿ‰์ด ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฐ๋ถ„๋Ÿ‰๋ณด๋‹ค ํฌ๊ฒŒ ์„ค์ •ํ•˜๋Š” ๊ฒƒ์ด ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ์˜ํ–ฅ์„ ์ตœ์†Œํ™” ํ•  ์ˆ˜ ์žˆ๋Š” ๊ฒƒ์œผ๋กœ ๋‚˜ํƒ€๋‚ฌ๋‹ค. ๊ทธ๋Ÿฌ๋‚˜ ๋ณธ ์—ฐ๊ตฌ๋Š” ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜์— ๋”ฐ๋ฅธ ๋Œ€์•ˆ๋ถ€์—์„œ์˜ ์˜ํ–ฅ์— ๋Œ€ํ•ด์„œ๋งŒ ๊ฒ€ํ† ํ•˜์˜€๊ณ  ์ˆ˜๋ฌธ ์ „๋ฉด ๊ฐœ๋„ ์กฐ๊ฑด์—์„œ ๊ฒ€ํ† ํ•˜์˜€๋‹ค๋Š” ํ•œ๊ณ„์ ์€ ๋ถ„๋ช…ํžˆ ์žˆ๋‹ค. ์ด์— ํ–ฅํ›„์—๋Š” ๋‹ค์–‘ํ•œ ์ˆ˜๋ฌธ ๊ฐœ๋„ ์กฐ๊ฑด ๋ฐ ๋ฐฉ๋ฅ˜ ์‹œ๋‚˜๋ฆฌ์˜ค๋ฅผ ์ ์šฉ ๋ฐ ๊ฒ€ํ† ํ•œ๋‹ค๋ฉด ๋ณด๋‹ค ํšจ์œจ์ ์ด๊ณ , ํšจ๊ณผ์ ์ธ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ํ™œ์šฉ๋ฐฉ์•ˆ์„ ๋„์ถœ์ด ๊ฐ€๋Šฅํ•  ๊ฒƒ์œผ๋กœ ๊ธฐ๋Œ€ ๋œ๋‹ค.

    ํ‚ค์›Œ๋“œ : ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ, FLOW-3D, ์ˆ˜์น˜๋ชจ์˜, ํ˜ธ์•ˆ ์•ˆ์ •์„ฑ, ์†Œ๋ฅ˜๋ ฅ

    1. ์„œ ๋ก 

    ์ตœ๊ทผ ๊ธฐํ›„๋ณ€ํ™”๋กœ ์ธํ•œ ์ง‘์ค‘ํ˜ธ์šฐ์˜ ์˜ํ–ฅ์œผ๋กœ ํ™์ˆ˜ ์‹œ ๋Œ์œผ๋กœ ์œ ์ž…๋˜๋Š” ํ™์ˆ˜๋Ÿ‰์ด ์„ค๊ณ„ ํ™์ˆ˜๋Ÿ‰๋ณด๋‹ค ์ฆ๊ฐ€ํ•˜์—ฌ ๋Œ ์•ˆ์ •์„ฑ ํ™•๋ณด๊ฐ€ ํ•„์š”ํ•œ ์‹ค์ •์ด๋‹ค(Office for Government Policy Coordination, 2003). MOLIT & K-water(2004)์—์„œ๋Š” ๊ธฐ์กด๋Œ์˜ ์ˆ˜๋ฌธํ•™์  ์•ˆ์ •์„ฑ ๊ฒ€ํ† ๋ฅผ ์ˆ˜ํ–‰ํ•˜์˜€์œผ๋ฉฐ ์ด์ƒํ™์ˆ˜ ๋ฐœ์ƒ ์‹œ 24๊ฐœ ๋Œ์—์„œ ์›”๋ฅ˜ ๋“ฑ์œผ๋กœ ์ธํ•œ ๋ถ•๊ดด์œ„ํ—˜์œผ๋กœ ๋Œ ํ•˜๋ฅ˜์ง€์—ญ์˜ ๊ทน์‹ฌํ•œ ํ”ผํ•ด๋ฅผ ์˜ˆ์ƒํ•˜์—ฌ ๋ณด์กฐ์—ฌ์ˆ˜๋กœ ์‹ ์„ค ๋ฐ ๊ธฐ์กด์—ฌ์ˆ˜๋กœ ํ™•์žฅ ๋“ฑ ์น˜์ˆ˜๋Šฅ๋ ฅ ์ฆ๋Œ€ ๊ธฐ๋ณธ๊ณ„ํš์„ ์ˆ˜๋ฆฝํ•˜์˜€๊ณ  ์ด๋ฅผ ํ†ตํ•˜์—ฌ ๊ทนํ•œํ™์ˆ˜ ๋ฐœ์ƒ ์‹œ ํ™์ˆ˜๋Ÿ‰ ๋ฐฐ์ œ๋Šฅ๋ ฅ์„ ์ฆ๋Œ€ํ•˜์—ฌ ๊ธฐ์กด๋Œ์˜ ์•ˆ์ „์„ฑ ํ™•๋ณด ๋ฐ ํ•˜๋ฅ˜์ง€์—ญ์˜ ํ”ผํ•ด๋ฅผ ๋ฐฉ์ง€ํ•˜๊ณ ์ž ํ•˜์˜€๋‹ค. ์—ฌ๊ธฐ์„œ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ๋Š” ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€ ๋™์‹œ ๋˜๋Š” ๋ณ„๋„ ์šด์˜ํ•˜๋Š” ์—ฌ์ˆ˜๋กœ๋กœ์จ ๋น„์ƒ์ƒํ™ฉ ์‹œ ๋ฐฉ๋ฅ˜ ๊ธฐ๋Šฅ์„ ํฌํ•จํ•˜๊ณ  ์žˆ๊ณ (K-water, 2021), ์ตœ๊ทผ์—๋Š” ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์˜ ๋…ธํ›„ํ™”์— ๋”ฐ๋ผ ๋ณด์กฐ์—ฌ์ˆ˜๋กœ์˜ ํ™œ์šฉ๋ฐฉ์•ˆ์— ๋Œ€ํ•œ ๊ด€์‹ฌ์ด ์ฆ๊ฐ€ํ•˜๊ณ  ์žˆ๋‹ค. ๋”ฐ๋ผ์„œ ๋ณธ ์—ฐ๊ตฌ์—์„œ๋Š” 3์ฐจ์› ์ˆ˜์น˜ํ•ด์„์„ ์ˆ˜ํ–‰ํ•˜์—ฌ ๊ธฐ์กด ๋ฐ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฉ๋ฅ˜๋Ÿ‰ ์กฐํ•ฉ์— ๋”ฐ๋ฅธ ํ•˜๋ฅ˜ ์˜ํ–ฅ์„ ๋ถ„์„ํ•˜๊ณ  ํ•˜๋ฅ˜ ํ˜ธ์•ˆ ์•ˆ์ •์„ฑ ์ธก๋ฉด์—์„œ ์ตœ์  ๋ฐฉ๋ฅ˜ ์‹œ๋‚˜๋ฆฌ์˜ค๋ฅผ ๊ฒ€ํ† ํ•˜๊ณ ์ž ํ•œ๋‹ค.

    ๊ธฐ์กด์˜ ๋Œ ์—ฌ์ˆ˜๋กœ ๊ฒ€ํ† ์— ๊ด€ํ•œ ์—ฐ๊ตฌ๋Š” ์ฃผ๋กœ ์ˆ˜๋ฆฌ์‹คํ—˜์„ ํ†ตํ•˜์—ฌ ๋ฐฉ๋ฅ˜์กฐ๊ฑด ๋ณ„ ํ๋ฆ„ํŠน์„ฑ์„ ๊ฒ€ํ† ํ•˜์˜€์œผ๋‚˜ ์ตœ๊ทผ์—๋Š” ์ˆ˜์น˜๋ชจํ˜• ์‹คํ—˜๊ฒฐ๊ณผ๊ฐ€ ์ˆ˜๋ฆฌ๋ชจํ˜•์‹คํ—˜๊ณผ ๋น„๊ตํ•˜์—ฌ ๊ทผ์‚ฌํ•œ ๊ฒƒ์„ ํ™•์ธํ•˜๋Š” ๋“ฑ ์ ์ฐจ ์ˆ˜์น˜๋ชจํ˜•์‹คํ—˜์„ ์ˆ˜๋ฆฌ๋ชจํ˜•์‹คํ—˜์˜ ๋Œ€์•ˆ์œผ๋กœ ํ™œ์šฉํ•˜๊ณ  ์žˆ๋‹ค(Jeon et al., 2006Kim, 2007Kim et al., 2008). ๊ตญ๋‚ด์˜ ๊ฒฝ์šฐ, Jeon et al.(2006)์€ ์ˆ˜๋ฆฌ๋ชจํ˜• ์‹คํ—˜๊ณผ ์ˆ˜์น˜๋ชจ์˜๋ฅผ ์ด์šฉํ•˜์—ฌ ์ž„ํ•˜๋Œ ๋ฐ”์ƒ์—ฌ์ˆ˜๋กœ์˜ ๊ธฐ๋ณธ์„ค๊ณ„์•ˆ์„ ๋„์ถœํ•˜์˜€๊ณ , Kim et al.(2008)์€ ๊ฐ€๋Šฅ์ตœ๋Œ€ํ™์ˆ˜๋Ÿ‰ ์œ ์ž… ์‹œ ๋น„์ƒ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜์— ๋”ฐ๋ฅธ ์ˆ˜๋ฆฌํ•™์  ์•ˆ์ •์„ฑ๊ณผ ๊ธฐ๋Šฅ์„ฑ์„ 3์ฐจ์› ์ˆ˜์น˜๋ชจํ˜•์ธ FLOW-3D๋ฅผ ํ™œ์šฉํ•˜์—ฌ ๊ฒ€ํ† ํ•˜์˜€๋‹ค. ๋˜ํ•œ Kim and Kim(2013)์€ ์ถฉ์ฃผ๋Œ์˜ ํ™์ˆ˜์กฐ์ ˆ ํšจ๊ณผ ๊ฒ€ํ†  ๋ฐ ๋ฐฉ๋ฅ˜๋Ÿ‰ ๋ณ€ํ™”์— ๋”ฐ๋ฅธ ์ƒยทํ•˜๋ฅ˜์˜ ์ˆ˜์œ„ ๋ณ€ํ™”๋ฅผ ์ˆ˜์น˜๋ชจํ˜•์„ ํ†ตํ•˜์—ฌ ๊ฒ€ํ† ํ•˜์˜€๋‹ค. ๊ตญ์™ธ์˜ ๊ฒฝ์šฐ Zeng et al.(2017)์€ 3์ฐจ์› ์ˆ˜์น˜๋ชจํ˜•์ธ Fluent๋ฅผ ํ™œ์šฉํ•œ ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜์— ๋”ฐ๋ฅธ ํ๋ฆ„ํŠน์„ฑ ๊ฒฐ๊ณผ์™€ ์ธก์ •๊ฒฐ๊ณผ๋ฅผ ๋น„๊ตํ•˜์—ฌ ์ˆ˜์น˜๋ชจํ˜• ๊ฒฐ๊ณผ์˜ ์‹ ๋ขฐ์„ฑ์„ ๊ฒ€ํ† ํ•˜์˜€๋‹ค. Li et al.(2011)์€ ๊ฐ€๋Šฅ ์ตœ๋Œ€ ํ™์ˆ˜๋Ÿ‰(Probable Maximum Flood, PMF)์กฐ๊ฑด์—์„œ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€ ์‹ ๊ทœ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ์œ ์ž…๋ถ€ ์ฃผ๋ณ€์˜ ํ๋ฆ„ํŠน์„ฑ์— ๋Œ€ํ•˜์—ฌ 3์ฐจ์› ์ˆ˜์น˜๋ชจํ˜• Fluent๋ฅผ ํ™œ์šฉํ•˜์—ฌ ๊ฒ€ํ† ํ•˜์˜€๊ณ , Lee et al.(2019)๋Š” ์„œ๋กœ ๊ทผ์ ‘ํ•ด์žˆ๋Š” ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€ ๋ณด์กฐ์—ฌ์ˆ˜๋กœ ๋™์‹œ ์šด์˜ ์‹œ ๋ฐฉ๋ฅ˜๋Šฅ ๊ฒ€ํ† ๋ฅผ ์ˆ˜๋ฆฌ๋ชจํ˜• ์‹คํ—˜ ๋ฐ ์ˆ˜์น˜๋ชจํ˜• ์‹คํ—˜(FLOW-3D)์„ ํ†ตํ•˜์—ฌ ์ˆ˜ํ–‰ํ•˜์˜€์œผ๋ฉฐ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ๋ฅผ ๋™์‹œ์šด์˜ํ•˜๊ฒŒ ๋˜๋ฉด ๋ฐฐ์ˆ˜๋กœ ๊ฐ„์„ญ์œผ๋กœ ์ธํ•˜์—ฌ ์ด ๋ฐฉ๋ฅ˜๋Ÿ‰์ด 7.6%๊นŒ์ง€ ๊ฐ์†Œ๋˜์–ด ๋Œ์˜ ๋ฐฉ๋ฅ˜๋Šฅ๋ ฅ์ด ๊ฐ์†Œํ•˜์˜€์Œ์„ ํ™•์ธํ•˜์˜€๋‹ค.

    ๊ทธ๋Ÿฌ๋‚˜ ๋Œ€๋ถ€๋ถ„์˜ ์—ฌ์ˆ˜๋กœ ๊ฒ€ํ† ์— ๋Œ€ํ•œ ์—ฐ๊ตฌ๋Š” ์—ฌ์ˆ˜๋กœ ๋‚ด์—์„œ์˜ ํ๋ฆ„ํŠน์„ฑ ๋ฐ ๊ธฐ๋Šฅ์„ฑ์— ๋Œ€ํ•œ ๊ฒ€ํ† ๋ฅผ ์ˆ˜ํ–‰ํ•˜์˜€๊ณ . ์ด์— ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜์šด์˜์— ๋”ฐ๋ฅธ ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ํ๋ฆ„ํŠน์„ฑ ๋ณ€ํ™” ๋ฐ ํ˜ธ์•ˆ ์•ˆ์ •์„ฑ ํ‰๊ฐ€์— ๊ด€ํ•œ ์ถ”๊ฐ€์ ์ธ ๊ฒ€ํ† ๊ฐ€ ํ•„์š”ํ•œ ์‹ค์ •์ด๋‹ค. ๋”ฐ๋ผ์„œ ๋ณธ ์—ฐ๊ตฌ์—์„œ๋Š” ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ ๋ฐ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜ ์กฐ๊ฑด์— ๋”ฐ๋ฅธ ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ํ๋ฆ„ํŠน์„ฑ ๋ฐ ํ˜ธ์•ˆ ์•ˆ์ •์„ฑ๋ถ„์„์„ 3์ฐจ์› ์ˆ˜์น˜๋ชจํ˜•์ธ FLOW-3D๋ฅผ ์ด์šฉํ•˜์—ฌ ๊ฒ€ํ† ํ•˜์˜€๋‹ค. ๋˜ํ•œ ๋‹ค์–‘ํ•œ ๋ฐฉ๋ฅ˜ ๋ฐฐ๋ถ„ ๋น„์œจ ๋ฐ ํ—ˆ์šฉ ๋ฐฉ๋ฅ˜๋Ÿ‰ ์กฐ๊ฑด ๋ณ€ํ™”์— ๋”ฐ๋ฅธ ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ํ๋ฆ„ํŠน์„ฑ ๋ฐ ์†Œ๋ฅ˜๋ ฅ ๋ถ„์„๊ฒฐ๊ณผ๋ฅผ ํ˜ธ์•ˆ ์„ค๊ณ„ ํ—ˆ์šฉ์œ ์† ๋ฐ ํ—ˆ์šฉ ์†Œ๋ฅ˜๋ ฅ ๊ธฐ์ค€๊ณผ ๋น„๊ตํ•˜์—ฌ ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ์˜ํ–ฅ์„ ์ตœ์†Œํ™” ํ•  ์ˆ˜ ์žˆ๋Š” ์ตœ์ ์˜ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ํ™œ์šฉ๋ฐฉ์•ˆ์„ ๋„์ถœํ•˜๊ณ ์ž ํ•œ๋‹ค.

    2. ๋ณธ ๋ก 

    2.1 ์ด๋ก ์  ๋ฐฐ๊ฒฝ

    2.1.1 3์ฐจ์› ์ˆ˜์น˜๋ชจํ˜•์˜ ๊ธฐ๋ณธ์ด๋ก 

    FLOW-3D๋Š” ๋ฏธ๊ตญ Flow Science, Inc์—์„œ ๊ฐœ๋ฐœํ•œ ๋ฒ”์šฉ ์œ ์ฒด์—ญํ•™ ํ”„๋กœ๊ทธ๋žจ(CFD, Computational Fluid Dynamics)์œผ๋กœ ์ž์œ  ์ˆ˜๋ฉด์„ ๊ฐ–๋Š” ํ๋ฆ„๋ชจ์˜์— ์‚ฌ์šฉ๋˜๋Š” 3์ฐจ์› ์ˆ˜์น˜ํ•ด์„ ๋ชจํ˜•์ด๋‹ค. ๋‚œ๋ฅ˜๋ชจํ˜•์„ ํ†ตํ•ด ๋‚œ๋ฅ˜ ํ•ด์„์ด ๊ฐ€๋Šฅํ•˜๊ณ , ๋Œ ๋ฐฉ๋ฅ˜์— ๋”ฐ๋ฅธ ํ•˜๋ฅ˜ ํ•˜์ฒœ์˜ ํ๋ฆ„ ํ•ด์„์—๋„ ๋งŽ์ด ์‚ฌ์šฉ๋˜์–ด ์™”๋‹ค(Flow Science, 2011). ๋ณธ ์—ฐ๊ตฌ์—์„œ๋Š” FLOW-3D(version 12.0)์„ ์ด์šฉํ•˜์—ฌ ํ™์ˆ˜ ์‹œ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์˜ ๋…ธํ›„ํ™”์— ๋Œ€๋น„ํ•˜์—ฌ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ํ™œ์šฉ๋ฐฉ์•ˆ์— ๋Œ€ํ•œ ๊ฒ€ํ† ๋ฅผ ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ํ˜ธ์•ˆ ์•ˆ์ •์„ฑ ์ธก๋ฉด์—์„œ ๊ฒ€ํ† ํ•˜์˜€๋‹ค.

    2.1.2 ์œ ๋™ํ•ด์„์˜ ์ง€๋ฐฐ๋ฐฉ์ •์‹

    1) ์—ฐ์† ๋ฐฉ์ •์‹(Continuity Equation)

    FLOW-3D๋Š” ๋น„์••์ถ•์„ฑ ์œ ์ฒด์— ๋Œ€ํ•˜์—ฌ ์—ฐ์†๋ฐฉ์ •์‹์„ ์‚ฌ์šฉํ•˜๋ฉฐ, ๋ฐ€๋„๋Š” ์ƒ์ˆ˜ํ•ญ์œผ๋กœ ์ ์šฉ๋œ๋‹ค. ์—ฐ์† ๋ฐฉ์ •์‹์€ Eqs. (1)(2)์™€ ๊ฐ™๋‹ค.

    (1)

    โˆ‡ยทv=0

    (2)

    โˆ‚โˆ‚x(uAx)+โˆ‚โˆ‚y(vAy)+โˆ‚โˆ‚z(wAz)=RSORฯ

    ์—ฌ๊ธฐ์„œ, ฯ๋Š” ์œ ์ฒด ๋ฐ€๋„(kg/m3), u, v, w๋Š” x, y, z๋ฐฉํ–ฅ์˜ ์œ ์†(m/s), Ax, Ay, Az๋Š” ๊ฐ ๋ฐฉํ–ฅ์˜ ์š”์†Œ๋ฉด์ (m2), RSOR๋Š” ์งˆ๋Ÿ‰ ์ƒ์„ฑ/์†Œ๋ฉธ(mass source/sink)ํ•ญ์„ ์˜๋ฏธํ•œ๋‹ค.

    2) ์šด๋™๋Ÿ‰ ๋ฐฉ์ •์‹(Momentum Equation)

    ๊ฐ ๋ฐฉํ–ฅ ์†๋„์„ฑ๋ถ„ u, v, w์— ๋Œ€ํ•œ ์šด๋™๋ฐฉ์ •์‹์€ Navier-Stokes ๋ฐฉ์ •์‹์œผ๋กœ ๋‹ค์Œ Eqs. (3)(4)(5)์™€ ๊ฐ™๋‹ค.

    (3)

    โˆ‚uโˆ‚t+1VF(uAxโˆ‚uโˆ‚x+vAyโˆ‚vโˆ‚y+wAzโˆ‚wโˆ‚z)=-1ฯโˆ‚pโˆ‚x+Gx+fx-bx-RSORฯVFu

    (4)

    โˆ‚vโˆ‚t+1VF(uAxโˆ‚uโˆ‚x+vAyโˆ‚vโˆ‚y+wAzโˆ‚wโˆ‚z)=-1ฯโˆ‚pโˆ‚y+Gy+fy-by-RSORฯVFv

    (5)

    โˆ‚wโˆ‚t+1VF(uAxโˆ‚uโˆ‚x+vAyโˆ‚vโˆ‚y+wAzโˆ‚wโˆ‚z)=-1ฯโˆ‚pโˆ‚z+Gz+fz-bz-RSORฯVFw

    ์—ฌ๊ธฐ์„œ, Gx, Gy, Gz๋Š” ์ฒด์ ๋ ฅ์— ์˜ํ•œ ๊ฐ€์†ํ•ญ, fx, fy, fz๋Š” ์ ์„ฑ์— ์˜ํ•œ ๊ฐ€์†ํ•ญ, bx, by, bz๋Š” ๋‹ค๊ณต์„ฑ ๋งค์ฒด์—์„œ์˜ ํ๋ฆ„์†์‹ค์„ ์˜๋ฏธํ•œ๋‹ค.

    2.1.3 ์†Œ๋ฅ˜๋ ฅ ์‚ฐ์ •

    ํ˜ธ์•ˆ์„ค๊ณ„ ์‹œ ์ œ๋ฐฉ์‚ฌ๋ฉด ํ˜ธ์•ˆ์˜ ์•ˆ์ •์„ฑ ํ™•๋ณด๋ฅผ ์œ„ํ•ด์„œ๋Š” ํ•˜์ฒœ์˜ ํ๋ฆ„์— ์˜ํ•˜์—ฌ ํ˜ธ์•ˆ์— ์ž‘์šฉํ•˜๋Š” ์†Œ๋ฅ˜๋ ฅ์— ์ €ํ•ญํ•  ์ˆ˜ ์žˆ๋Š” ์žฌ๋ฃŒ ๋ฐ ๊ณต๋ฒ• ์„ ํƒ์ด ํ•„์š”ํ•˜๋‹ค. ๊ตญ๋‚ด์˜ ๊ฒฝ์šฐ ํ•˜์ฒœ๊ณต์‚ฌ์„ค๊ณ„์‹ค๋ฌด์š”๋ น(MOLIT, 2016)์—์„œ ๊ณ„ํšํ™์ˆ˜๋Ÿ‰ ์œ ํ•˜ ์‹œ ์†Œ๋ฅ˜๋ ฅ ์‚ฐ์ • ๋ฐฉ๋ฒ•์„ ์ œ์‹œํ•˜๊ณ  ์žˆ๋‹ค. ์†Œ๋ฅ˜๋ ฅ์€ ํ•˜์ฒœ์˜ ํ‰๊ท ์œ ์†์„ ์ด์šฉํ•˜์—ฌ ์‚ฐ์ •ํ•  ์ˆ˜ ์žˆ์œผ๋ฉฐ, ์†Œ๋ฅ˜๋ ฅ ์‚ฐ์ •์‹์€ Eqs. (6)(7)๊ณผ ๊ฐ™๋‹ค.

    1) Schoklitsch ๊ณต์‹

    Schoklitsch(1934)๋Š” Chezy ์œ ์†๊ณ„์ˆ˜๋ฅผ ์ ์šฉํ•˜์—ฌ ์†Œ๋ฅ˜๋ ฅ์„ ์‚ฐ์ •ํ•˜์˜€๋‹ค.

    (6)

    ฯ„=ฮณRI=ฮณC2V2

    ์—ฌ๊ธฐ์„œ, ฯ„๋Š” ์†Œ๋ฅ˜๋ ฅ(N/m2), R์€ ๋™์ˆ˜๋ฐ˜๊ฒฝ(m), ฮณ๋Š” ๋ฌผ์˜ ๋‹จ์œ„์ค‘๋Ÿ‰(10.0 kN/m3), I๋Š” ์—๋„ˆ์ง€๊ฒฝ์‚ฌ, C๋Š” Chezy ์œ ์†๊ณ„์ˆ˜, V๋Š” ํ‰๊ท ์œ ์†(m/s)์„ ์˜๋ฏธํ•œ๋‹ค.

    2) Manning ์กฐ๋„๊ณ„์ˆ˜๋ฅผ ๊ณ ๋ คํ•œ ๊ณต์‹

    Chezy ์œ ์†๊ณ„์ˆ˜๋ฅผ ๋Œ€์‹ ํ•˜์—ฌ Manning์˜ ์กฐ๋„๊ณ„์ˆ˜๋ฅผ ๊ณ ๋ คํ•˜์—ฌ ์†Œ๋ฅ˜๋ ฅ์„ ์‚ฐ์ •ํ•  ์ˆ˜ ์žˆ๋‹ค.

    (7)

    ฯ„=ฮณn2V2R1/3

    ์—ฌ๊ธฐ์„œ, ฯ„๋Š” ์†Œ๋ฅ˜๋ ฅ(N/m2), R์€ ๋™์ˆ˜๋ฐ˜๊ฒฝ(m), ฮณ๋Š” ๋ฌผ์˜ ๋‹จ์œ„์ค‘๋Ÿ‰(10.0 kN/m3), n์€ Manning์˜ ์กฐ๋„๊ณ„์ˆ˜, V๋Š” ํ‰๊ท ์œ ์†(m/s)์„ ์˜๋ฏธํ•œ๋‹ค.

    FLOW-3D ์ˆ˜์น˜๋ชจ์˜ ์ˆ˜ํ–‰์„ ํ†ตํ•˜์—ฌ ํ•˜์ฒœ์˜ ๋ฐ”๋‹ฅ ์œ ์†์„ ๋„์ถœํ•  ์ˆ˜ ์žˆ์œผ๋ฉฐ, ๋ณธ ์—ฐ๊ตฌ์—์„œ๋Š” Maning ์กฐ๋„๊ณ„์ˆ˜๋กค ๊ณ ๋ คํ•˜์—ฌ ์†Œ๋ฅ˜๋ ฅ์„ ์‚ฐ์ •ํ•˜๊ณ ์ž ํ•œ๋‹ค. ์†Œ๋ฅ˜๋ ฅ์„ ์‚ฐ์ •ํ•˜๊ธฐ ์œ„ํ•ด์„œ ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜์— ๋”ฐ๋ฅธ ๋Œ€์•ˆ๋ถ€์˜ ๋ฐ”๋‹ฅ์œ ์† ๋ณ€ํ™”๋ฅผ ๊ฒ€ํ† ํ•˜์—ฌ ์ตœ๋Œ€ ์œ ์† ๊ฐ’์„ ์ด์šฉํ•˜์˜€๋‹ค. ์ตœ์ข…์ ์œผ๋กœ ์‚ฐ์ •ํ•œ ์†Œ๋ฅ˜๋ ฅ๊ณผ ํ˜ธ์•ˆ์˜ ์žฌ๋ฃŒ ๋ฐ ๊ณต๋ฒ•์— ๋”ฐ๋ฅธ ํ—ˆ์šฉ ์†Œ๋ฅ˜๋ ฅ๊ณผ ๋น„๊ตํ•˜์—ฌ ์ œ๋ฐฉ์‚ฌ๋ฉด ํ˜ธ์•ˆ์˜ ์•ˆ์ •์„ฑ ๊ฒ€ํ† ๋ฅผ ์ˆ˜ํ–‰ํ•˜๊ฒŒ ๋œ๋‹ค.

    2.2 ํ•˜์ฒœํ˜ธ์•ˆ ์„ค๊ณ„๊ธฐ์ค€

    ํ•˜์ฒœ ํ˜ธ์•ˆ์€ ๊ณ„ํšํ™์ˆ˜์œ„ ์ดํ•˜์˜ ์œ ์ˆ˜์ž‘์šฉ์— ๋Œ€ํ•˜์—ฌ ์•ˆ์ •์„ฑ์ด ํ™•๋ณด๋˜๋„๋ก ๊ณ„ํšํ•˜์—ฌ์•ผ ํ•˜๋ฉฐ, ํ˜ธ์•ˆ์˜ ์„ค๊ณ„ ์‹œ์—๋Š” ์‚ฌ์šฉ์žฌ๋ฃŒ์˜ ํ™•๋ณด์šฉ์ด์„ฑ, ์‹œ๊ณต์ƒ์˜ ์šฉ์ด์„ฑ, ์„ธ๊ตด์— ๋Œ€ํ•œ ๊ตด์š”์„ฑ(flexibility) ๋“ฑ์„ ๊ณ ๋ คํ•˜์—ฌ ํ˜ธ์•ˆ์˜ ํ˜•ํƒœ, ์‹œ๊ณต๋ฐฉ๋ฒ• ๋“ฑ์„ ๊ฒฐ์ •ํ•œ๋‹ค(MOLIT, 2019). ๊ตญ๋‚ด์˜ ๊ฒฝ์šฐ, ํ•˜์ฒœ๊ณต์‚ฌ์„ค๊ณ„์‹ค๋ฌด์š”๋ น(MOLIT, 2016)์—์„œ๋Š” ๋‹ค์–‘ํ•œ ํ˜ธ์•ˆ๊ณต๋ฒ•์— ๋Œ€ํ•˜์—ฌ ๋น„ํƒˆ๊ฒฝ์‚ฌ์— ๋”ฐ๋ผ ์„ค๊ณ„ ์œ ์†์„ ๋น„๊ตํ•˜๊ฑฐ๋‚˜, ํ—ˆ์šฉ ์†Œ๋ฅ˜๋ ฅ์„ ๋น„๊ตํ•จ์œผ๋กœ์จ ํ˜ธ์•ˆ์˜ ์•ˆ์ •์„ฑ์„ ํ‰๊ฐ€ํ•œ๋‹ค. ํ˜ธ์•ˆ์— ๋Œ€ํ•œ ๊ตญ์™ธ์˜ ์„ค๊ณ„๊ธฐ์ค€์œผ๋กœ ๋ฏธ๊ตญ์˜ ๊ฒฝ์šฐ, ASTM(๋ฏธ๊ตญ์žฌ๋ฃŒ์‹œํ—˜ํ•™ํšŒ)์—์„œ ํ˜ธ์•ˆ๋ธ”๋ก ๋ฐ ์‹์ƒ๋งคํŠธ ์‹œํ—˜๋ฐฉ๋ฒ•์„ ์ œ์‹œํ•˜์˜€๊ณ  ์ œํ’ˆ๋ณ„๋กœ ASTM ์‹œํ—˜์— ์˜ํ•œ ํ—ˆ์šฉ์œ ์† ๋ฐ ํ—ˆ์šฉ ์†Œ๋ฅ˜๋ ฅ์„ ์ œ์‹œํ•˜์˜€๋‹ค. ์ผ๋ณธ์˜ ๊ฒฝ์šฐ, ํ˜ธ์•ˆ ๋ธ”๋ก์— ๋Œ€ํ•œ ์ถ•์†Œ์‹คํ—˜์„ ํ†ตํ•˜์—ฌ ํ•ญ๋ ฅ์„ ์ธก์ •ํ•˜๊ณ  ์ด๋ฅผ ํ†ตํ•ด์„œ ํ˜ธ์•ˆ ๋ธ”๋ก์— ๋Œ€ํ•œ ํ•ญ๋ ฅ๊ณ„์ˆ˜๋ฅผ ์ œ์‹œํ•˜๊ณ  ์žˆ๋‹ค. ์„ค๊ณ„ ์‹œ์—๋Š” ํ•ญ๋ ฅ๊ณ„์ˆ˜์— ์˜ํ•œ ๋ธ”๋ก์˜ ์•ˆ์ •์„ฑ์„ ํ‰๊ฐ€ํ•˜๊ณ  ์žˆ์œผ๋‚˜, ์ตœ๊ทผ์—๋Š” ์„ธ๊ตด์˜ ์˜ํ–ฅ์„ ๊ณ ๋ คํ•  ์ˆ˜ ์žˆ๋Š” ํ˜ธ์•ˆ ์•ˆ์ •์„ฑ ํ‰๊ฐ€์˜ ํ•„์š”์„ฑ์„ ์ œ๊ธฐํ•˜๊ณ  ์žˆ๋‹ค(MOLIT, 2019). ๊ด€๋ จ๋œ ๊ตญ๋‚ดยท์™ธ์˜ ํ•˜์ฒœํ˜ธ์•ˆ ์„ค๊ณ„๊ธฐ์ค€์€ Table 1์— ์ •๋ฆฌํ•˜์—ฌ ์ œ์‹œํ•˜์˜€๊ณ , ๋ณธ ์—ฐ๊ตฌ์—์„œ ํ•˜์ฒœ ํ˜ธ์•ˆ ์•ˆ์ •์„ฑ ํ‰๊ฐ€ ์‹œ ํ•˜์ฒœ๊ณต์‚ฌ์„ค๊ณ„์‹ค๋ฌด์š”๋ น(MOLIT, 2016)๊ณผ ASTM ์‹œํ—˜์—์„œ ์ œ์‹œํ•œ ํ—ˆ์šฉ์†Œ๋ฅ˜๋ ฅ ๋ฐ ํ—ˆ์šฉ์œ ์† ๊ธฐ์ค€์„ ๋น„๊ตํ•˜์—ฌ ๊ฐ๊ฐ 0.28 kN/m2, 5.0 m/s ๋ฏธ๋งŒ์ผ ๊ฒฝ์šฐ ํ˜ธ์•ˆ ์•ˆ์ •์„ฑ์„ ํ™•๋ณดํ•˜์˜€๋‹ค๊ณ  ํŒ๋‹จํ•˜์˜€๋‹ค.

    Table 1.

    Standard of Permissible Velocity and Shear on Revetment

    Country (Reference)MaterialPermissible velocity (Vp, m/s)Permissible Shear (ฯ„p, kN/m2)
    KoreaRiver Construction Design Practice Guidelines
    (MOLIT, 2016)
    Vegetated5.00.50
    Stone5.00.80
    USAASTM D’6460Vegetated6.10.81
    Unvegetated5.00.28
    JAPANDynamic Design Method of Revetment5.0

    2.3. ๋ณด์กฐ์—ฌ์ˆ˜๋กœ ์šด์˜์— ๋”ฐ๋ฅธ ํ•˜๋ฅ˜ํ•˜์ฒœ ์˜ํ–ฅ ๋ถ„์„

    2.3.1 ๋ชจํ˜•์˜ ๊ตฌ์ถ• ๋ฐ ๊ฒฝ๊ณ„์กฐ๊ฑด

    ๋ณธ ์—ฐ๊ตฌ์—์„œ๋Š” ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์˜ ๋…ธํ›„ํ™”์— ๋Œ€๋น„ํ•˜์—ฌ ํ™์ˆ˜ ์‹œ ๋ณด์กฐ์—ฌ์ˆ˜๋กœ์˜ ํ™œ์šฉ๋ฐฉ์•ˆ์— ๋”ฐ๋ฅธ ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ํ๋ฆ„ํŠน์„ฑ ๋ฐ ํ˜ธ์•ˆ์•ˆ์ •์„ฑ ํ‰๊ฐ€๋ฅผ ์ˆ˜ํ–‰ํ•˜๊ธฐ ์œ„ํ•ด FLOW-3D ๋ชจํ˜•์„ ์ด์šฉํ•˜์˜€๋‹ค. ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ ๋ฐ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ๋Š” ์น˜์ˆ˜๋Šฅ๋ ฅ ์ฆ๋Œ€์‚ฌ์—…(MOLIT & K-water, 2004)์„ ํ†ตํ•˜์—ฌ ์™„๊ณต๋œ โ—‹โ—‹๋Œ์˜ ์ œ์›์„ ์ด์šฉํ•˜์—ฌ ๊ตฌ์ถ•ํ•˜์˜€๋‹ค. โ—‹โ—‹๋Œ์€ ์„ค๊ณ„๋นˆ๋„(100๋…„) ๋ฐ 200๋…„๋นˆ๋„ ๊นŒ์ง€๋Š” ๊ณ„ํšํ™์ˆ˜์œ„ ์ด๋‚ด๋กœ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ๋ฅผ ํ†ตํ•˜์—ฌ ์šด์˜์ด ๊ฐ€๋Šฅํ•˜๋‚˜ ๊ทธ ์ด์ƒ ํ™์ˆ˜์กฐ์ ˆ์€ ๋ณด์กฐ์—ฌ์ˆ˜๋กœ๋ฅผ ํ†ตํ•˜์—ฌ ์กฐ์ ˆํ•ด์•ผ ํ•˜๋ฉฐ, ๋˜ํ•œ 2011๋…„ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ ์ •๋ฐ€์•ˆ์ „์ง„๋‹จ ๊ฒฐ๊ณผ ์‚ฌ๋ฉด์˜ ํ‘œ์ธต ์œ ์‹ค ๋ฐ ์˜น๋ฒฝ ๋ฐ€๋ฆผํ˜„์ƒ ๋“ฑ์ด ํ™•์ธ๋˜์–ด ๋…ธํ›„ํ™”์— ๋”ฐ๋ฅธ ๋ณด์ˆ˜ยท๋ณด๊ฐ•์ด ํ•„์š”ํ•œ ์ƒํƒœ์ด๋‹ค. ์ด์— ๋ณด์กฐ์—ฌ์ˆ˜๋กœ์˜ ํ™œ์šฉ๋ฐฉ์•ˆ ๊ฒ€ํ† ๊ฐ€ ํ•„์š”ํ•œ ๊ฒƒ์œผ๋กœ ํŒ๋‹จํ•˜์—ฌ ๋ณธ ์—ฐ๊ตฌ์˜ ๋Œ€์ƒ๋Œ์œผ๋กœ ์„ ์ •ํ•˜์˜€๋‹ค. ํ•˜๋ฅ˜ ํ•˜์ฒœ์˜ ํ๋ฆ„ํŠน์„ฑ์„ ์˜ˆ์ธกํ•˜๊ธฐ ์œ„ํ•˜์—ฌ ๊ฒฉ์ž๊ฐ„๊ฒฉ์„ 0.99 ~ 8.16 m์˜ ํฌ๊ธฐ๋กœ ํ•˜์—ฌ ์ด ๊ฒฉ์ž์ˆ˜๋Š” 49,102,500๊ฐœ๋กœ ๊ตฌ์„ฑํ•˜์˜€์œผ๋ฉฐ, ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜์— ๋”ฐ๋ฅธ ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ํ๋ฆ„ํ•ด์„์„ ์œ„ํ•œ ๊ฒฝ๊ณ„์กฐ๊ฑด์œผ๋กœ ์ƒ๋ฅ˜๋Š” ์œ ์ž…์œ ๋Ÿ‰(inflow), ๋ฐ”๋‹ฅ์€ ๋ฒฝ๋ฉด(wall), ํ•˜๋ฅ˜๋Š” ์ˆ˜์œ„(water surface elevation)์กฐ๊ฑด์œผ๋กœ ์ ์šฉํ•˜๋„๋ก ํ•˜์˜€๋‹ค(Table 2Fig. 1 ์ฐธ์กฐ). FLOW-3D ๋‚œ๋ฅ˜๋ชจํ˜•์—๋Š” ํ˜ผํ•ฉ๊ธธ์ด ๋ชจํ˜•, ๋‚œ๋ฅ˜์—๋„ˆ์ง€ ๋ชจํ˜•, k-ฯต๋ชจํ˜•, RNG(Renormalized Group Theory) k-ฯต๋ชจํ˜•, LES ๋ชจํ˜• ๋“ฑ์ด ์žˆ์œผ๋ฉฐ, ๋ณธ ์—ฐ๊ตฌ์—์„œ๋Š” ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜์— ๋”ฐ๋ฅธ ๋ณต์žกํ•œ ๋‚œ๋ฅ˜ ํ๋ฆ„ ๋ฐ ๋†’์€ ์ „๋‹จํ๋ฆ„์„ ์ •ํ™•ํ•˜๊ฒŒ ๋ชจ์˜(Flow Science, 2011)ํ•  ์ˆ˜ ์žˆ๋Š” RNG k-ฯต๋ชจํ˜•์„ ์‚ฌ์šฉํ•˜์˜€๊ณ , ํ•˜๋ฅ˜ํ•˜์ฒœ ํ˜ธ์•ˆ์˜ ์•ˆ์ •์„ฑ ์ธก๋ฉด์—์„œ ๋ณด์กฐ์—ฌ์ˆ˜๋กœ์˜ ํ™œ์šฉ๋ฐฉ์•ˆ์„ ๊ฒ€ํ† ํ•˜๊ธฐ ์œ„ํ•˜์—ฌ ๋ฐฉ๋ฅ˜์‹œ๋‚˜๋ฆฌ์˜ค๋Š” Table 3์— ์ œ์‹œ๋œ ๊ฒƒ ๊ฐ™์ด ์„ค์ •ํ•˜์˜€๋‹ค. Case 1 ๋ฐ Case 2๋ฅผ ํ†ตํ•˜์—ฌ ๊ณ„ํšํ™์ˆ˜๋Ÿ‰์— ๋Œ€ํ•˜์—ฌ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋‹จ๋… ์šด์˜์ด ํ•˜๋ฅ˜ํ•˜์ฒœ์— ๋ฏธ์น˜๋Š” ์˜ํ–ฅ์„ ํ™•์ธํ•˜์˜€๊ณ  ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฉ๋ฅ˜๋Ÿ‰ ์กฐ์ ˆ์„ ํ†ตํ•˜์—ฌ ํ˜ธ์•ˆ ์•ˆ์ •์„ฑ ์ธก๋ฉด์—์„œ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜๋Šฅ ๊ฒ€ํ† ๋ฅผ ์ˆ˜ํ–‰ํ•˜์˜€๋‹ค(Case 3 ~ Case 6). ๋˜ํ•œ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฉ๋ฅ˜๋Ÿ‰ ๋ฐฐ๋ถ„์— ๋”ฐ๋ฅธ ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ์˜ํ–ฅ ๊ฒ€ํ† (Case 7 ~ Case 10) ๋ฐ ๋ฐฉ๋ฅ˜ ๋ฐฐ๋ถ„์— ๋”ฐ๋ฅธ ํ—ˆ์šฉ ๋ฐฉ๋ฅ˜๋Ÿ‰์„ ํ˜ธ์•ˆ ์•ˆ์ •์„ฑ ์ธก๋ฉด์—์„œ ๊ฒ€ํ† ๋ฅผ ์ˆ˜ํ–‰ํ•˜์˜€๋‹ค(Case 11 ~ Case 14).

    ์ˆ˜๋ฌธ์€ ์™„์ „๊ฐœ๋„ ์กฐ๊ฑด์œผ๋กœ ๊ฐ€์ •ํ•˜์˜€์œผ๋ฉฐ ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ๊ณ„ํšํ™์ˆ˜๋Ÿ‰์— ๋Œ€ํ•œ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€ ๋ณด์กฐ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฐ๋ถ„๋Ÿ‰์„ ์กฐ์ ˆํ•˜์—ฌ ๋ชจ์˜๋ฅผ ์ˆ˜ํ–‰ํ•˜์˜€๋‹ค. ์—ฌ์ˆ˜๋กœ๋Š” ์ฝ˜ํฌ๋ฆฌํŠธ์˜ ์กฐ๋„๊ณ„์ˆ˜ ๊ฐ’(Chow, 1959)์„ ์ฑ„ํƒํ•˜์˜€๊ณ , ๋Œ ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ์กฐ๋„๊ณ„์ˆ˜๋Š” ํ•˜์ฒœ๊ธฐ๋ณธ๊ณ„ํš(Busan Construction and Management Administration, 2009) ์ œ์‹œ๋œ ์กฐ๋„๊ณ„์ˆ˜ ๊ฐ’์„ ์ฑ„ํƒํ•˜์˜€์œผ๋ฉฐ FLOW-3D์˜ ์ ์šฉ์„ ์œ„ํ•˜์—ฌ Manning-Strickler ๊ณต์‹(Vanoni, 2006)์„ ์ด์šฉํ•˜์—ฌ ์กฐ๋„๊ณ„์ˆ˜๋ฅผ ์กฐ๊ณ ๊ฐ’์œผ๋กœ ๋ณ€ํ™˜ํ•˜์—ฌ ์‚ฌ์šฉํ•˜์˜€๋‹ค. Manning-Strickler ๊ณต์‹์€ Eq. (8)๊ณผ ๊ฐ™์œผ๋ฉฐ, FLOW-3D์— ์ ์šฉํ•œ ์กฐ๋„๊ณ„์ˆ˜ ๋ฐ ์กฐ๊ณ ๋Š” Table 4์™€ ๊ฐ™๋‹ค.

    (8)

    n=ks1/68.1g1/2

    ์—ฌ๊ธฐ์„œ, kS๋Š” ์กฐ๊ณ  (m), n์€ Manning์˜ ์กฐ๋„๊ณ„์ˆ˜, g๋Š” ์ค‘๋ ฅ๊ฐ€์†๋„(m/s2)๋ฅผ ์˜๋ฏธํ•œ๋‹ค.

    ์‹œ๊ฐ„์— ๋”ฐ๋ผ ๋™์ผํ•œ ์œ ๋Ÿ‰์ด ์ผ์ •ํ•˜๊ฒŒ ์œ ์ž…๋˜๋„๋ก ๋ชจ์˜๋ฅผ ์ˆ˜ํ–‰ํ•˜์˜€์œผ๋ฉฐ, ์‹œ๊ฐ„๊ฐ„๊ฒฉ(Time Step)์€ 0.0001์ดˆ๋กœ ์„ค์ •(CFL number < 1.0) ํ•˜์˜€๋‹ค. ๋˜ํ•œ ์—ฌ์ˆ˜๋กœ ์ˆ˜๋ฌธ์„ ํ†ตํ•œ ์œ ๋Ÿ‰์˜ ๋ณ€๋™ ๊ฐ’์ด 1.0%์ด๋‚ด์ผ ๊ฒฝ์šฐ๋Š” ์—ฐ์†๋ฐฉ์ •์‹์„ ๋งŒ์กฑํ•˜๊ณ  ์žˆ๋‹ค๊ณ  ๊ฐ€์ •ํ•˜์˜€๋‹ค. ์ด๋Š”, ์œ ๋Ÿ‰์˜ ๋ณ€๋™ ๊ฐ’์ด 1.0%์ด๋‚ด์ผ ๊ฒฝ์šฐ ์œ ์†์˜ ๋ณ€๋™ ๊ฐ’ ์—ญ์‹œ 1.0%์ด๋‚ด์ด๋ฉฐ, ์ˆ˜์น˜๋ชจ์˜ ๊ฒฐ๊ณผ 1.0%์˜ ์œ ์†๋ณ€๋™์€ ํ˜ธ์•ˆ์˜ ์œ ์†์„ค๊ณ„๊ธฐ์ค€์— ํฌ๊ฒŒ ์˜ํ–ฅ์„ ๋ฏธ์น˜์ง€ ์•Š๋Š”๋‹ค๊ณ  ํŒ๋‹จํ•˜์˜€๋‹ค. ๊ทธ ๊ฒฐ๊ณผ ๋ชจ๋“  ์ˆ˜์น˜๋ชจ์˜ Case์—์„œ 2400์ดˆ ์ด๋‚ด์— ๊ฒฐ๊ณผ ๊ฐ’์ด ์ˆ˜๋ ดํ•˜๋Š” ๊ฒƒ์„ ํ™•์ธํ•˜์˜€๋‹ค.

    Table 2.

    Mesh sizes and numerical conditions

    MeshNumbers49,102,500 EA
    Increment (m)DirectionExisting SpillwayAuxiliary Spillway
    โˆ†X0.99 ~ 4.301.00 ~ 4.30
    โˆ†Y0.99 ~ 8.161.00 ~ 5.90
    โˆ†Z0.50 ~ 1.220.50 ~ 2.00
    Boundary ConditionsXmin / YmaxInflow / Water Surface Elevation
    Xmax, Ymin, Zmin / ZmaxWall / Symmetry
    Turbulence ModelRNG model
    Table 3.

    Case of numerical simulation (Qp : Design flood discharge)

    CaseExisting Spillway (Qe, m3/s)Auxiliary Spillway (Qa, m3/s)Remarks
    1Qp0Reference case
    20Qp
    300.58QpReview of discharge capacity on
    auxiliary spillway
    400.48Qp
    500.45Qp
    600.32Qp
    70.50Qp0.50QpDetermination of optimal division
    ratio on Spillways
    80.61Qp0.39Qp
    90.39Qp0.61Qp
    100.42Qp0.58Qp
    110.32Qp0.45QpDetermination of permissible
    division on Spillways
    120.35Qp0.48Qp
    130.38Qp0.53Qp
    140.41Qp0.56Qp
    Table 4.

    Roughness coefficient and roughness height

    CriteriaRoughness coefficient (n)Roughness height (ks, m)
    Structure (Concrete)0.0140.00061
    River0.0330.10496
    /media/sites/ksds/2021-014-02/N0240140207/images/ksds_14_02_07_F1.jpg
    Fig. 1

    Layout of spillway and river in this study

    2.3.2 ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฉ๋ฅ˜๋Šฅ ๊ฒ€ํ† 

    ๋ณธ ์—ฐ๊ตฌ์—์„œ๋Š” ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฉ๋ฅ˜๋Ÿ‰ ๋ฐฐ๋ถ„์— ๋”ฐ๋ฅธ ํ•˜๋ฅ˜ํ•˜์ฒœ ๋Œ€์•ˆ๋ถ€์˜ ์œ ์†๋ถ„ํฌ ๋ฐ ์ˆ˜์œ„๋ถ„ํฌ๋ฅผ ๊ฒ€ํ† ํ•˜๊ธฐ ์œ„ํ•ด ์ˆ˜์น˜๋ชจ์˜ Case ๋ณ„ ๋‹ค์Œ๊ณผ ๊ฐ™์ด ๊ด€์‹ฌ๊ตฌ์—ญ์„ ์„ค์ •ํ•˜์˜€๋‹ค(Fig. 2 ์ฐธ์กฐ). ๊ด€์‹ฌ๊ตฌ์—ญ(๋Œ€์•ˆ๋ถ€)์˜ ๊ธธ์ด(L)๋Š” ์ด 1.3 km๋กœ 10 m ๋“ฑ ๊ฐ„๊ฒฉ์œผ๋กœ ๋‚˜๋ˆ„์–ด ๊ฒ€ํ† ํ•˜์˜€์œผ๋ฉฐ, Section 1(0 < X/L < 0.27)์€ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜์— ๋”ฐ๋ฅธ ์˜ํ–ฅ์ด ์ง€๋ฐฐ์ ์ธ ๊ตฌ๊ฐ„, Section 2(0.27 < X/L < 1.00)๋Š” ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜์— ๋”ฐ๋ฅธ ์˜ํ–ฅ์ด ์ง€๋ฐฐ์ ์ธ ๊ตฌ๊ฐ„์œผ๋กœ ๊ฐ ๊ตฌ๊ฐ„์—์„œ์˜ ์ˆ˜์œ„, ์œ ์†, ์ˆ˜์‹ฌ๊ฒฐ๊ณผ๋ฅผ ํ™•์ธํ•˜์˜€๋‹ค. ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์˜ ๋…ธํ›„ํ™”์— ๋”ฐ๋ฅธ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฉ๋ฅ˜๋Šฅ ๊ฒ€ํ† ๋ฅผ ์œ„ํ•˜์—ฌ Case 1 – Case 6๊นŒ์ง€์˜ ๊ฒฐ๊ณผ๋ฅผ ๋น„๊ตํ•˜์˜€๋‹ค.

    ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋‹จ๋… ์šด์˜ ์‹œ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ ์šด์˜ ์‹œ ๋ณด๋‹ค ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ๋Œ€์•ˆ๋ถ€์˜ ์ตœ๋Œ€ ์œ ์†(Vmax)์€ ์•ฝ 3% ๊ฐ์†Œํ•˜์˜€์œผ๋ฉฐ, ์ด๋Š” ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ํ•˜์ฒœ ์œ ์ž…๊ฐ์ด ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ ๋ณด๋‹ค 7ยฐ์ž‘์œผ๋ฉฐ ์œ ์ž…ํ•˜์ฒœ์˜ ํญ์ด ์ฆ๊ฐ€ํ•˜์—ฌ ์œ ์†์ด ๊ฐ์†Œํ•œ ๊ฒƒ์œผ๋กœ ํŒ๋‹จ๋œ๋‹ค. ๋Œ€์•ˆ๋ถ€์˜ ์ตœ๋Œ€ ์œ ์† ๋ฐœ์ƒ์œ„์น˜๋Š” ํ•˜๋ฅ˜ ์ชฝ์œผ๋กœ ์ด๋™ํ•˜์˜€์œผ๋ฉฐ ๊ต๋Ÿ‰์œผ๋กœ ์ธํ•œ ๋‹จ๋ฉด์˜ ์ถ•์†Œ๋กœ ์ตœ๋Œ€์œ ์†์ด ๋ฐœ์ƒํ•˜๋Š” ๊ฒƒ์œผ๋กœ ํŒ๋‹จ๋œ๋‹ค. ๋˜ํ•œ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฐ๋ถ„๋Ÿ‰(Qa)์ด ์ฆ๊ฐ€ํ•จ์— ๋”ฐ๋ผ ํ•˜๋ฅ˜ํ•˜์ฒœ ๋Œ€์•ˆ๋ถ€์˜ ์ตœ๋Œ€ ์œ ์†์ด ์ฆ๊ฐ€ํ•˜์˜€๋‹ค. ํ•˜์ฒœํ˜ธ์•ˆ ์„ค๊ณ„๊ธฐ์ค€์—์„œ ์ œ์‹œํ•˜๊ณ  ์žˆ๋Š” ํ—ˆ์šฉ์œ ์†(Vp)๊ณผ ๋น„๊ตํ•œ ๊ฒฐ๊ณผ, ๊ณ„ํšํ™์ˆ˜๋Ÿ‰(Qp)์˜ 45% ์ดํ•˜(Case 5 & 6)๋ฅผ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์—์„œ ๋ฐฉ๋ฅ˜ํ•˜๊ฒŒ ๋˜๋ฉด ํ—ˆ์šฉ ์œ ์†(5.0 m/s)์กฐ๊ฑด์„ ๋งŒ์กฑํ•˜์—ฌ ํ˜ธ์•ˆ์•ˆ์ •์„ฑ์„ ํ™•๋ณดํ•˜์˜€๋‹ค(Fig. 3 ์ฐธ์กฐ). ํ—ˆ์šฉ์œ ์† ์™ธ์—๋„ ๋Œ€์•ˆ๋ถ€์—์„œ์˜ ์†Œ๋ฅ˜๋ ฅ์„ ์‚ฐ์ •ํ•˜์—ฌ ํ•˜์ฒœํ˜ธ์•ˆ ์„ค๊ณ„๊ธฐ์ค€์—์„œ ์ œ์‹œํ•œ ํ—ˆ์šฉ ์†Œ๋ฅ˜๋ ฅ(ฯ„p)๊ณผ ๋น„๊ตํ•œ ๊ฒฐ๊ณผ, ์œ ์†๊ณผ ๋™์ผํ•˜๊ฒŒ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฉ๋ฅ˜๋Ÿ‰์ด ๊ณ„ํšํ™์ˆ˜๋Ÿ‰์˜ 45% ์ดํ•˜์ผ ๊ฒฝ์šฐ ํ—ˆ์šฉ์†Œ๋ฅ˜๋ ฅ(0.28 kN/m2) ์กฐ๊ฑด์„ ๋งŒ์กฑํ•˜์˜€๋‹ค(Fig. 4 ์ฐธ์กฐ). ๊ฐ Case ๋ณ„ ํ˜ธ์•ˆ์„ค๊ณ„์กฐ๊ฑด๊ณผ ๋น„๊ตํ•œ ๊ฒฐ๊ณผ๋Š” Table 5์— ์ œ์‹œํ•˜์˜€๋‹ค.

    ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ์ˆ˜์œ„๋„ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ ์šด์˜ ์‹œ ๋ณด๋‹ค ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ๋‹จ๋… ์šด์˜ ์‹œ ์ตœ๋Œ€ ์ˆ˜์œ„(ฮทmax)๊ฐ€ ์•ฝ 2% ๊ฐ์†Œํ•˜๋Š” ํšจ๊ณผ๋ฅผ ๋ณด์˜€์œผ๋ฉฐ ์ตœ๋Œ€ ์ˆ˜์œ„ ๋ฐœ์ƒ์œ„์น˜๋Š” ์ˆ˜์ถฉ๋ถ€๋กœ ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜์‹œ ์ฒ˜์˜ค๋ฆ„์— ์˜ํ•œ ์ˆ˜์œ„ ์ƒ์Šน์œผ๋กœ ํŒ๋‹จ๋œ๋‹ค. ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์˜ ๋‹จ๋…์šด์˜(Case 1)์˜ ์ˆ˜์œ„(ฮทref)๋ฅผ ๊ธฐ์ค€์œผ๋กœ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฉ๋ฅ˜๋Ÿ‰์ด ์ฆ๊ฐ€ํ•จ์— ๋”ฐ๋ผ ์ˆ˜์œ„๋Š” ์ฆ๊ฐ€ํ•˜์˜€์œผ๋‚˜ ๊ณ„ํšํ™์ˆ˜๋Ÿ‰์˜ 58%๊นŒ์ง€ ๋ฐฉ๋ฅ˜ํ•  ๊ฒฝ์šฐ ์›”๋ฅ˜์— ๋Œ€ํ•œ ์•ˆ์ •์„ฑ(ฮทmax/ฮทref<0.97(=๊ธฐ์„ค์ œ๋ฐฉ๊ณ ))์€ ํ™•๋ณด๋˜์—ˆ๋‹ค(Fig. 5 ์ฐธ์กฐ). ๊ทธ๋Ÿฌ๋‚˜ ๊ณ„ํšํ™์ˆ˜๋Ÿ‰ ์กฐ๊ฑด์—์„œ๋Š” ์›”๋ฅ˜์— ๋Œ€ํ•œ ์œ„ํ—˜์„ฑ์ด ์กด์žฌํ•˜๊ธฐ ๋•Œ๋ฌธ์— ๊ธฐ์กด์—ฌ์ˆ˜๋กœ์™€ ๋ณด์กฐ์—ฌ์ˆ˜๋กœ์˜ ์ ์ ˆํ•œ ๋ฐฉ๋ฅ˜๋Ÿ‰ ๋ฐฐ๋ถ„ ์กฐํ•ฉ์„ ๋„์ถœํ•˜๋Š” ๊ฒƒ์ด ์ค‘์š”ํ•˜๋‹ค๊ณ  ํŒ๋‹จ๋˜์–ด ์ง„๋‹ค.

    /media/sites/ksds/2021-014-02/N0240140207/images/ksds_14_02_07_F2.jpg
    Fig. 2

    Region of interest in this study

    /media/sites/ksds/2021-014-02/N0240140207/images/ksds_14_02_07_F3.jpg
    Fig. 3

    Maximum velocity and location of Vmax according to Qa

    /media/sites/ksds/2021-014-02/N0240140207/images/ksds_14_02_07_F4.jpg
    Fig. 4

    Maximum shear according to Qa

    /media/sites/ksds/2021-014-02/N0240140207/images/ksds_14_02_07_F5.jpg
    Fig. 5

    Maximum water surface elevation and location of ฮทmax according to Qa

    Table 5.

    Numerical results for each cases (Case 1 ~ Case 6)

    CaseMaximum Velocity
    (Vmax, m/s)
    Maximum Shear
    (ฯ„max, kN/m2)
    Evaluation
    in terms of Vp
    Evaluation
    in terms of ฯ„p
    1
    (Qa = 0)
    9.150.54No GoodNo Good
    2
    (Qa = Qp)
    8.870.56No GoodNo Good
    3
    (Qa = 0.58Qp)
    6.530.40No GoodNo Good
    4
    (Qa = 0.48Qp)
    6.220.36No GoodNo Good
    5
    (Qa = 0.45Qp)
    4.220.12AccpetAccpet
    6
    (Qa = 0.32Qp)
    4.040.14AccpetAccpet

    2.3.3 ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜๋Ÿ‰ ๋ฐฐ๋ถ„ ๊ฒ€ํ† 

    ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ ๋ฐ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ๋‹จ๋…์šด์˜์— ๋”ฐ๋ฅธ ํ•˜๋ฅ˜ํ•˜์ฒœ ๋ฐ ํ˜ธ์•ˆ์˜ ์•ˆ์ •์„ฑ ํ‰๊ฐ€๋ฅผ ์ˆ˜ํ–‰ํ•œ ๊ฒฐ๊ณผ ๊ณ„ํšํ™์ˆ˜๋Ÿ‰ ๋ฐฉ๋ฅ˜ ์‹œ ํ•˜๋ฅ˜ํ•˜์ฒœ ๋Œ€์•ˆ๋ถ€์—์„œ ํ˜ธ์•ˆ ์„ค๊ณ„ ์กฐ๊ฑด(ํ—ˆ์šฉ์œ ์† ๋ฐ ํ—ˆ์šฉ ์†Œ๋ฅ˜๋ ฅ)์„ ์ดˆ๊ณผํ•˜์˜€์œผ๋ฉฐ, ์ฒ˜์˜ค๋ฆ„์— ์˜ํ•œ ์ˆ˜์œ„ ์ƒ์Šน์œผ๋กœ ์›”๋ฅ˜์— ๋Œ€ํ•œ ์œ„ํ—˜์„ฑ ์ฆ๊ฐ€๋ฅผ ํ™•์ธํ•˜์˜€๋‹ค. ๋”ฐ๋ผ์„œ ๊ณ„ํš ํ™์ˆ˜๋Ÿ‰ ์กฐ๊ฑด์—์„œ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฉ๋ฅ˜๋Ÿ‰ ๋ฐฐ๋ถ„์„ ํ†ตํ•˜์—ฌ ํ˜ธ์•ˆ ์•ˆ์ •์„ฑ์„ ํ™•๋ณดํ•˜๊ณ  ํ•˜๋ฅ˜ํ•˜์ฒœ์— ๋ฐฉ๋ฅ˜๋กœ ์ธํ•œ ํ”ผํ•ด๋ฅผ ์ตœ์†Œํ™”ํ•  ์ˆ˜ ์žˆ๋Š” ๋ฐฐ๋ถ„์กฐํ•ฉ(Case 7 ~ Case 10)์„ ๊ฒ€ํ† ํ•˜์˜€๋‹ค. Case 7์€ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€ ๋ณด์กฐ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฐ๋ถ„ ๋น„์œจ์„ ๊ท ๋“ฑํ•˜๊ฒŒ ์ ์šฉํ•œ ๊ฒฝ์šฐ์ด๊ณ , Case 8์€ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฐ๋ถ„๋Ÿ‰์ด ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์— ๋น„ํ•˜์—ฌ ๋งŽ์€ ๊ฒฝ์šฐ, Case 9๋Š” ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฐ๋ถ„๋Ÿ‰์ด ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์— ๋น„ํ•˜์—ฌ ๋งŽ์€ ๊ฒฝ์šฐ๋ฅผ ์˜๋ฏธํ•œ๋‹ค. ์ตœ๋Œ€์œ ์†์„ ๋น„๊ตํ•œ ๊ฒฐ๊ณผ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฐ๋ถ„ ๋น„์œจ์ด ํฐ ๊ฒฝ์šฐ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฐ๋ถ„๋Ÿ‰์— ์˜ํ•˜์—ฌ ํ๋ฆ„์ด ํ•˜์ฒœ ์ค‘์‹ฌ์— ์ง‘์ค‘๋˜์–ด ๋Œ€์•ˆ๋ถ€์˜ ์œ ์†์„ ์ €๊ฐํ•˜๋Š” ํšจ๊ณผ๋ฅผ ํ™•์ธํ•˜์˜€๋‹ค. ๋ณด์กฐ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฉ๋ฅ˜๋Ÿ‰ ๋ฐฐ๋ถ„ ๋น„์œจ์ด ์ฆ๊ฐ€ํ• ์ˆ˜๋ก ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ ๋Œ€์•ˆ๋ถ€ ์ธก(0.00<X/L<0.27, Section 1) ์œ ์† ๋ถ„ํฌ๋Š” ๊ฐ์†Œํ•˜์˜€์œผ๋‚˜, ์‹ ๊ทœ์—ฌ์ˆ˜๋กœ ๋Œ€์•ˆ๋ถ€ ์ธก(0.27<X/L<1.00, Section 2) ์œ ์†์€ ์ฆ๊ฐ€ํ•˜๋Š” ๊ฒƒ์„ ํ™•์ธํ•˜์˜€๋‹ค(Fig. 6 ์ฐธ์กฐ). ๊ทธ๋Ÿฌ๋‚˜ ์œ ์† ์ €๊ฐ ํšจ๊ณผ์—๋„ ๋Œ€์•ˆ๋ถ€ ์ „๊ตฌ๊ฐ„์—์„œ ์„ค๊ณ„ ํ—ˆ์šฉ์œ ์† ์กฐ๊ฑด์„ ์ดˆ๊ณผํ•˜์—ฌ ์ œ๋ฐฉ์˜ ์•ˆ์ •์„ฑ์„ ํ™•๋ณดํ•˜์ง€๋Š” ๋ชปํ•˜์˜€๋‹ค. ์†Œ๋ฅ˜๋ ฅ ์‚ฐ์ • ๊ฒฐ๊ณผ ์œ ์†๊ณผ ๋™์ผํ•˜๊ฒŒ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฉ๋ฅ˜๋Ÿ‰์ด ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฉ๋ฅ˜๋Ÿ‰ ๋ณด๋‹ค ํฌ๋ฉด ๊ฐ์†Œํ•˜๋Š” ๊ฒƒ์„ ํ™•์ธํ•˜์˜€๊ณ  ์ผ๋ถ€ ๊ตฌ๊ฐ„์—์„œ๋Š” ํ—ˆ์šฉ ์†Œ๋ฅ˜๋ ฅ ์กฐ๊ฑด์„ ๋งŒ์กฑํ•˜๋Š” ๊ฒƒ์„ ํ™•์ธํ•˜์˜€๋‹ค(Fig. 7 ์ฐธ์กฐ).

    ๋”ฐ๋ผ์„œ ์œ ์† ์ €๊ฐํšจ๊ณผ๊ฐ€ ์žˆ๋Š” ๋ฐฐ๋ถ„ ๋น„์œจ ์กฐ๊ฑด(Qa>Qe)์—์„œ Section 2์— ์œ ์† ์ €๊ฐ์— ์˜ํ–ฅ์„ ๋ฏธ์น˜๋Š” ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜๋Ÿ‰ ๋ฐฐ๋ถ„ ๋น„์œจ์„ ์ฆ๊ฐ€์‹œ์ผœ ์ถ”๊ฐ€ ๊ฒ€ํ† (Case 10)๋ฅผ ์ˆ˜ํ–‰ํ•˜์˜€๋‹ค. ๋‹จ๋…์šด์˜๊ณผ ๋น„๊ต ์‹œ ํ•˜๋ฅ˜ํ•˜์ฒœ์— ์œ ์ž…๋˜๋Š” ์œ ๋Ÿ‰์€ ์ฆ๊ฐ€ํ•˜์˜€์Œ์—๋„ ๋ถˆ๊ตฌํ•˜๊ณ  ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜๋Ÿ‰์— ์˜ํ•ด ํ๋ฆ„์ด ํ•˜์ฒœ ์ค‘์‹ฌ์œผ๋กœ ์ง‘์ค‘๋˜๋Š” ํ˜„์ƒ์— ๋”ฐ๋ผ ๋Œ€์•ˆ๋ถ€์˜ ์œ ์†์€ ๋‹จ๋… ์šด์˜์— ๋น„ํ•˜์—ฌ ๊ฐ์†Œํ•˜๋Š” ๊ฒƒ์„ ํ™•์ธํ•˜์˜€๊ณ (Fig. 8 ์ฐธ์กฐ), ํ˜ธ์•ˆ ์„ค๊ณ„ ํ—ˆ์šฉ์œ ์† ๋ฐ ํ—ˆ์šฉ ์†Œ๋ฅ˜๋ ฅ ์กฐ๊ฑด์„ ๋งŒ์กฑํ•˜๋Š” ๊ตฌ๊ฐ„์ด ๋ฐœ์ƒํ•˜์—ฌ ํ˜ธ์•ˆ ์•ˆ์ •์„ฑ๋„ ํ™•๋ณดํ•œ ๊ฒƒ์œผ๋กœ ํŒ๋‹จ๋˜์—ˆ๋‹ค. ์ตœ์ข…์ ์œผ๋กœ ๊ฐ Case ๋ณ„ ์ˆ˜์œ„ ๊ฒฐ๊ณผ์˜ ๊ฒฝ์šฐ ์—ฌ์ˆ˜๋กœ ๋™์‹œ ์šด์˜์„ ์ˆ˜ํ–‰ํ•˜๊ฒŒ ๋˜๋ฉด ๋Œ€์•ˆ๋ถ€ ์ „ ๊ตฌ๊ฐ„์—์„œ ์›”๋ฅ˜์— ๋Œ€ํ•œ ์•ˆ์ •์„ฑ(ฮทmax/ฮทref<0.97(=๊ธฐ์„ค์ œ๋ฐฉ๊ณ ))์€ ํ™•๋ณดํ•˜์˜€๋‹ค(Fig. 9 ์ฐธ์กฐ). ๊ฐ Case ๋ณ„ ๋Œ€์•ˆ๋ถ€์—์„œ ์ตœ๋Œ€ ์œ ์†๊ฒฐ๊ณผ ๋ฐ ์‚ฐ์ •ํ•œ ์†Œ๋ฅ˜๋ ฅ์€ Table 6์— ์ œ์‹œํ•˜์˜€๋‹ค.

    /media/sites/ksds/2021-014-02/N0240140207/images/ksds_14_02_07_F6.jpg
    Fig. 6

    Maximum velocity on section 1 & 2 according to Qa

    /media/sites/ksds/2021-014-02/N0240140207/images/ksds_14_02_07_F7.jpg
    Fig. 7

    Maximum shear on section 1 & 2 according to Qa

    /media/sites/ksds/2021-014-02/N0240140207/images/ksds_14_02_07_F8.jpg
    Fig. 8

    Velocity results of FLOW-3D (a: auxiliary spillway operation only , b : simultaneous operation of spillways)

    /media/sites/ksds/2021-014-02/N0240140207/images/ksds_14_02_07_F9.jpg
    Fig. 9

    Maximum water surface elevation on section 1 & 2 according to Qa

    Table 6.

    Numerical results for each cases (Case 7 ~ Case 10)

    Case (Qe &amp; Qa)Maximum Velocity (Vmax, m/s)Maximum Shear
    (ฯ„max, kN/m2)
    Evaluation in terms of VpEvaluation in terms of ฯ„p
    Section 1Section 2Section 1Section 2Section 1Section 2Section 1Section 2
    7
    Qe : 0.50QpQa : 0.50Qp
    8.106.230.640.30No GoodNo GoodNo GoodNo Good
    8
    Qe : 0.61QpQa : 0.39Qp
    8.886.410.610.34No GoodNo GoodNo GoodNo Good
    9
    Qe : 0.39QpQa : 0.61Qp
    6.227.330.240.35No GoodNo GoodAcceptNo Good
    10
    Qe : 0.42QpQa : 0.58Qp
    6.394.790.300.19No GoodAcceptNo GoodAccept

    2.3.4 ๋ฐฉ๋ฅ˜๋Ÿ‰ ๋ฐฐ๋ถ„ ๋น„์œจ์˜ ํ—ˆ์šฉ ๋ฐฉ๋ฅ˜๋Ÿ‰ ๊ฒ€ํ† 

    ๊ณ„ํš ํ™์ˆ˜๋Ÿ‰ ๋ฐฉ๋ฅ˜ ์‹œ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฐ๋ถ„ ๋น„์œจ ๊ฒ€ํ†  ๊ฒฐ๊ณผ Case 10(Qe = 0.42Qp, Qa = 0.58Qp)์—์„œ ๋ฐฉ๋ฅ˜์— ๋”ฐ๋ฅธ ํ•˜๋ฅ˜ ํ•˜์ฒœ์˜ ํ”ผํ•ด๋ฅผ ์ตœ์†Œํ™”์‹œํ‚ฌ ์ˆ˜ ์žˆ๋Š” ๊ฒƒ์„ ํ™•์ธํ•˜์˜€๋‹ค. ๊ทธ๋Ÿฌ๋‚˜ ๋Œ€์•ˆ๋ถ€ ์ „ ๊ตฌ๊ฐ„์— ๋Œ€ํ•˜์—ฌ ํ˜ธ์•ˆ ์„ค๊ณ„์กฐ๊ฑด์„ ๋งŒ์กฑํ•˜์ง€ ๋ชปํ•˜์˜€๋‹ค. ๋”ฐ๋ผ์„œ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฉ๋ฅ˜ ๋ฐฐ๋ถ„ ๋น„์œจ์„ ๊ณ ์ •์‹œํ‚จ ํ›„ ์ด ๋ฐฉ๋ฅ˜๋Ÿ‰์„ ์กฐ์ ˆํ•˜์—ฌ ํ—ˆ์šฉ ๋ฐฉ๋ฅ˜๋Ÿ‰์„ ๊ฒ€ํ† ํ•˜์˜€๋‹ค(Case 11 ~ Case 14).

    ํ˜ธ์•ˆ ์•ˆ์ •์„ฑ ์ธก๋ฉด์—์„œ ๊ฒ€ํ† ํ•œ ๊ฒฐ๊ณผ ๊ณ„ํšํ™์ˆ˜๋Ÿ‰ ๋Œ€๋น„ ์ด ๋ฐฉ๋ฅ˜๋Ÿ‰์ด ๊ฐ์†Œํ•˜๋ฉด ์ตœ๋Œ€ ์œ ์† ๋ฐ ์ตœ๋Œ€ ์†Œ๋ฅ˜๋ ฅ์ด ๊ฐ์†Œํ•˜๊ณ  ์ตœ์ข…์ ์œผ๋กœ ๊ณ„ํš ํ™์ˆ˜๋Ÿ‰์˜ 77%๋ฅผ ๋ฐฉ๋ฅ˜ํ•  ๊ฒฝ์šฐ ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ๋Œ€์•ˆ๋ถ€์—์„œ ํ˜ธ์•ˆ ์„ค๊ณ„์กฐ๊ฑด์„ ๋ชจ๋‘ ๋งŒ์กฑํ•˜๋Š” ๊ฒƒ์„ ํ™•์ธํ•˜์˜€๋‹ค(Fig. 10Fig. 11 ์ฐธ์กฐ). ๊ฐ Case ๋ณ„ ๋Œ€์•ˆ๋ถ€์—์„œ ์ตœ๋Œ€ ์œ ์†๊ฒฐ๊ณผ ๋ฐ ์‚ฐ์ •ํ•œ ์†Œ๋ฅ˜๋ ฅ์€ Table 7์— ์ œ์‹œํ•˜์˜€๋‹ค. ๋˜ํ•œ Case ๋ณ„ ์ˆ˜์œ„ ๊ฒ€ํ†  ๊ฒฐ๊ณผ ์ฒ˜์˜ค๋ฆ„์œผ๋กœ ์ธํ•œ ๋Œ€์•ˆ๋ถ€ ์ „ ๊ตฌ๊ฐ„์—์„œ ์›”๋ฅ˜์— ๋Œ€ํ•œ ์•ˆ์ •์„ฑ(ฮทmax/ฮทref<0.97(=๊ธฐ์„ค์ œ๋ฐฉ๊ณ ))์€ ํ™•๋ณดํ•˜์˜€๋‹ค(Fig. 12 ์ฐธ์กฐ).

    Table 7.

    Numerical results for each cases (Case 11 ~ Case 14)

    Case (Qe &amp; Qa)Maximum Velocity
    (Vmax, m/s)
    Maximum Shear
    (ฯ„max, kN/m2)
    Evaluation in terms of VpEvaluation in terms of ฯ„p
    Section 1Section 2Section 1Section 2Section 1Section 2Section 1Section 2
    11
    Qe : 0.32QpQa : 0.45Qp
    3.634.530.090.26AcceptAcceptAcceptAccept
    12
    Qe : 0.35QpQa : 0.48Qp
    5.745.180.230.22No GoodNo GoodAcceptAccept
    13
    Qe : 0.38QpQa : 0.53Qp
    6.704.210.280.11No GoodAcceptAcceptAccept
    14
    Qe : 0.41QpQa : 0.56Qp
    6.545.240.280.24No GoodNo GoodAcceptAccept
    /media/sites/ksds/2021-014-02/N0240140207/images/ksds_14_02_07_F10.jpg
    Fig. 10

    Maximum velocity on section 1 & 2 according to total outflow

    /media/sites/ksds/2021-014-02/N0240140207/images/ksds_14_02_07_F11.jpg
    Fig. 11

    Maximum shear on section 1 & 2 according to total outflow

    /media/sites/ksds/2021-014-02/N0240140207/images/ksds_14_02_07_F12.jpg
    Fig. 12

    Maximum water surface elevation on section 1 & 2 according to total outflow

    3. ๊ฒฐ ๋ก 

    ๋ณธ ์—ฐ๊ตฌ์—์„œ๋Š” ํ™์ˆ˜ ์‹œ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์˜ ๋…ธํ›„ํ™”๋กœ ์ธํ•œ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ํ™œ์šฉ๋ฐฉ์•ˆ์— ๋Œ€ํ•˜์—ฌ ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ํ˜ธ์•ˆ ์•ˆ์ •์„ฑ ์ธก๋ฉด์—์„œ ๊ฒ€ํ† ํ•˜์˜€๋‹ค. ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜๋กœ ์ธํ•œ ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ํ๋ฆ„ํŠน์„ฑ์„ ๊ฒ€ํ† ํ•˜๊ธฐ ์œ„ํ•˜์—ฌ 3์ฐจ์› ์ˆ˜์น˜๋ชจํ˜•์ธ FLOW-3D๋ฅผ ํ™œ์šฉํ•˜์˜€๊ณ , ์—ฌ์ˆ˜๋กœ ์ง€ํ˜•์€ ์น˜์ˆ˜๋Šฅ๋ ฅ ์ฆ๋Œ€์‚ฌ์—…์„ ํ†ตํ•˜์—ฌ ์™„๊ณต๋œ โ—‹โ—‹๋Œ์˜ ์ œ์›์„ ์ด์šฉํ•˜์˜€๋‹ค. ํ•˜๋ฅ˜ํ•˜์ฒœ ์กฐ๋„ ๊ณ„์ˆ˜ ๋ฐ ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜๋Ÿ‰์€ ํ•˜์ฒœ๊ธฐ๋ณธ๊ณ„ํš์„ ์ฐธ๊ณ ํ•˜์—ฌ ์ ์šฉํ•˜์˜€๋‹ค. ์ตœ์ข…์ ์œผ๋กœ ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜๋กœ ์ธํ•œ ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ํ”ผํ•ด๋ฅผ ์ตœ์†Œํ™” ์‹œํ‚ฌ ์ˆ˜ ์žˆ๋Š” ์ ์ ˆํ•œ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ํ™œ์šฉ๋ฐฉ์•ˆ์„ ๋„์ถœํ•˜๊ธฐ ์œ„ํ•˜์—ฌ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ๋‹จ๋… ์šด์˜๊ณผ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€์˜ ๋™์‹œ ์šด์˜์— ๋”ฐ๋ฅธ ํ•˜๋ฅ˜ ํ•˜์ฒœ์˜ ํ๋ฆ„ํŠน์„ฑ ๋ฐ ์†Œ๋ฅ˜๋ ฅ์˜ ๋ณ€ํ™”๋ฅผ ๊ฒ€ํ† ํ•˜์˜€๋‹ค.

    ์ˆ˜๋ฌธ์€ ์™„์ „ ๊ฐœ๋„ ์ƒํƒœ์—์„œ ๋ฐฉ๋ฅ˜ํ•œ๋‹ค๋Š” ๊ฐ€์ •์œผ๋กœ ๊ณ„ํš ํ™์ˆ˜๋Ÿ‰ ์กฐ๊ฑด์—์„œ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ๋‹จ๋… ์šด์˜ ์‹œ ํ•˜๋ฅ˜ํ•˜์ฒœ ๋Œ€์•ˆ๋ถ€์˜ ์œ ์† ๋ฐ ์ˆ˜์œ„๋ฅผ ๊ฒ€ํ† ํ•œ ๊ฒฐ๊ณผ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ ๋‹จ๋…์šด์˜์— ๋น„ํ•˜์—ฌ ์ตœ๋Œ€ ์œ ์† ๋ฐ ์ตœ๋Œ€ ์ˆ˜์œ„๊ฐ€ ๊ฐ์†Œํ•˜๋Š” ๊ฒƒ์„ ํ™•์ธํ•  ์ˆ˜ ์žˆ์—ˆ์œผ๋ฉฐ, ์ด๋Š” ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ๋‹จ๋… ์šด์˜ ์‹œ ํ•˜๋ฅ˜ํ•˜์ฒœ์œผ๋กœ ์œ ์ž…๊ฐ๋„๊ฐ€ ์ž‘์•„์ง€๊ณ , ์œ ์ž…๋˜๋Š” ํ•˜์ฒœ์˜ ํญ์ด ์ฆ๊ฐ€๋˜๊ธฐ ๋•Œ๋ฌธ์ด๋‹ค. ๊ทธ๋Ÿฌ๋‚˜ ๊ณ„ํš ํ™์ˆ˜๋Ÿ‰ ์กฐ๊ฑด์—์„œ ํ•˜์ฒœํ˜ธ์•ˆ ์„ค๊ณ„๊ธฐ์ค€์—์„œ ์ œ์‹œํ•œ ํ—ˆ์šฉ ์œ ์†(5.0 m/s)๊ณผ ํ—ˆ์šฉ ์†Œ๋ฅ˜๋ ฅ(0.28 kN/m2)๊ณผ ๋น„๊ตํ•˜์˜€์„ ๋•Œ ํ˜ธ์•ˆ ์•ˆ์ •์„ฑ์„ ํ™•๋ณดํ•˜์ง€ ๋ชปํ•˜์˜€์œผ๋ฉฐ, ๊ณ„ํšํ™์ˆ˜๋Ÿ‰์˜ 45% ์ดํ•˜ ๋ฐฉ๋ฅ˜ ์‹œ์— ๋Œ€์•ˆ๋ถ€์˜ ํ˜ธ์•ˆ ์•ˆ์ •์„ฑ์„ ํ™•๋ณดํ•˜์˜€๋‹ค. ์ˆ˜์œ„์˜ ๊ฒฝ์šฐ ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜์— ๋”ฐ๋ฅธ ๋Œ€์•ˆ๋ถ€์—์„œ ์ฒ˜์˜ค๋ฆ„ ํ˜„์ƒ์ด ๋ฐœ์ƒํ•˜์—ฌ ์›”๋ฅ˜์— ๋Œ€ํ•œ ์œ„ํ—˜์„ฑ์„ ํ™•์ธํ•˜์˜€๊ณ  ์ด๋ฅผ ํ†ตํ•˜์—ฌ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€์˜ ๋™์‹œ ์šด์˜ ๋ฐฉ์•ˆ์„ ๋„์ถœํ•˜๋Š” ๊ฒƒ์ด ์ค‘์š”ํ•˜๋‹ค๊ณ  ํŒ๋‹จ๋œ๋‹ค. ๋”ฐ๋ผ์„œ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€์˜ ๋™์‹œ ์šด์˜ ์ธก๋ฉด์—์„œ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฐ๋ถ„ ๋น„์œจ ๋ฐ ์ด ๋ฐฉ๋ฅ˜๋Ÿ‰์„ ๋ณ€ํ™”์‹œ์ผœ๊ฐ€๋ฉฐ ํ•˜๋ฅ˜ ํ•˜์ฒœ์˜ ํ๋ฆ„ํŠน์„ฑ ๋ฐ ์†Œ๋ฅ˜๋ ฅ์˜ ๋ณ€ํ™”๋ฅผ ๊ฒ€ํ† ํ•˜์˜€๋‹ค. ๋ฐฐ๋ถ„ ๋น„์œจ์˜ ๊ฒฝ์šฐ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๊ท ๋“ฑ ๋ฐฐ๋ถ„(Case 7) ๋ฐ ํŽธ์ค‘ ๋ฐฐ๋ถ„(Case 8 & Case 9)์„ ๊ฒ€ํ† ํ•˜์—ฌ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฉ๋ฅ˜๋Ÿ‰์ด ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฉ๋ฅ˜๋Ÿ‰๋ณด๋‹ค ํฐ ๊ฒฝ์šฐ ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ์ค‘์‹ฌ๋ถ€๋กœ ์ง‘์ค‘๋˜์–ด ๋Œ€์•ˆ๋ถ€์˜ ์ตœ๋Œ€์œ ์†, ์ตœ๋Œ€์†Œ๋ฅ˜๋ ฅ ๋ฐ ์ตœ๋Œ€์ˆ˜์œ„๊ฐ€ ๊ฐ์†Œํ•˜๋Š” ๊ฒƒ์„ ํ™•์ธํ•˜์˜€๋‹ค. ์ด๋ฅผ ๊ทผ๊ฑฐ๋กœ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฉ๋ฅ˜ ๋น„์œจ์„ ์ฆ๊ฐ€(Qe=0.42Qp, Qa=0.58Qp)์‹œ์ผœ ๊ฒ€ํ† ํ•œ ๊ฒฐ๊ณผ ๋Œ€์•ˆ๋ถ€ ์ผ๋ถ€ ๊ตฌ๊ฐ„์—์„œ ํ—ˆ์šฉ ์œ ์† ๋ฐ ํ—ˆ์šฉ์†Œ๋ฅ˜๋ ฅ ์กฐ๊ฑด์„ ๋งŒ์กฑํ•˜๋Š” ๊ฒƒ์„ ํ™•์ธํ•˜์˜€๋‹ค. ์ด๋ฅผ ํ†ตํ•˜์—ฌ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋™์‹œ ์šด์˜์„ ํ†ตํ•˜์—ฌ ์ ์ ˆํ•œ ๋ฐฉ๋ฅ˜๋Ÿ‰ ๋ฐฐ๋ถ„ ๋น„์œจ์„ ๋„์ถœํ•˜๋Š” ๊ฒƒ์ด ๋ฐฉ๋ฅ˜๋กœ ์ธํ•œ ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ํ”ผํ•ด๋ฅผ ์ €๊ฐํ•˜๋Š”๋ฐ ํšจ๊ณผ์ ์ธ ๊ฒƒ์œผ๋กœ ํŒ๋‹จ๋œ๋‹ค. ๊ทธ๋Ÿฌ๋‚˜ ์„ค๊ณ„ํ™์ˆ˜๋Ÿ‰ ๋ฐฉ๋ฅ˜ ์‹œ ์ „ ๊ตฌ๊ฐ„์—์„œ ํ—ˆ์šฉ ์œ ์† ๋ฐ ์†Œ๋ฅ˜๋ ฅ ์กฐ๊ฑด์„ ๋งŒ์กฑํ•˜์ง€ ๋ชปํ•˜์˜€๋‹ค. ์ตœ์ข…์ ์œผ๋กœ ์ „์ฒด ๋ฐฉ๋ฅ˜๋Ÿ‰์—์„œ ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฉ๋ฅ˜ ๋น„์œจ์„ 42%, ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ๋ฐฉ๋ฅ˜ ๋น„์œจ์„ 58%๋กœ ์„ค์ •ํ•˜์—ฌ ํ—ˆ์šฉ๋ฐฉ๋ฅ˜๋Ÿ‰์„ ๊ฒ€ํ† ํ•œ ๊ฒฐ๊ณผ, ๊ณ„ํšํ™์ˆ˜๋Ÿ‰์˜ 77%์ดํ•˜๋กœ ๋ฐฉ๋ฅ˜ ์‹œ ๋Œ€์•ˆ๋ถ€์˜ ์ตœ๋Œ€์œ ์†์€ ๊ธฐ์กด์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜์˜ ์ง€๋ฐฐ์˜ํ–ฅ๊ตฌ๊ฐ„(section 1)์—์„œ 3.63 m/s, ๊ธฐ์กด ์—ฌ์ˆ˜๋กœ์™€ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜์˜ ์˜ํ–ฅ๊ตฌ๊ฐ„(section 2)์—์„œ 4.53 m/s๋กœ ํ—ˆ์šฉ์œ ์† ์กฐ๊ฑด์„ ๋งŒ์กฑํ•˜์˜€๊ณ , ์‚ฐ์ •ํ•œ ์†Œ๋ฅ˜๋ ฅ๋„ ๊ฐ๊ฐ 0.09 kN/m2 ๋ฐ 0.26 kN/m2๋กœ ํ—ˆ์šฉ ์†Œ๋ฅ˜๋ ฅ ์กฐ๊ฑด์„ ๋งŒ์กฑํ•˜์—ฌ ๋Œ€์•ˆ๋ถ€ ํ˜ธ์•ˆ์˜ ์•ˆ์ •์„ฑ์„ ํ™•๋ณดํ•˜์˜€๋‹ค๊ณ  ํŒ๋‹จ๋œ๋‹ค.

    ๋ณธ ์—ฐ๊ตฌ ๊ฒฐ๊ณผ๋Š” ๊ธฐํ›„๋ณ€ํ™” ๋ฐ ๊ธฐ์กด์—ฌ์ˆ˜๋กœ์˜ ๋…ธํ›„ํ™”๋กœ ์ธํ•˜์—ฌ ํ™์ˆ˜ ์‹œ ๊ธฐ์กด์—ฌ์ˆ˜๋กœ์˜ ๋‹จ๋…์šด์˜์œผ๋กœ ํ•˜๋ฅ˜ํ•˜์ฒœ์˜ ํ”ผํ•ด๊ฐ€ ๋ฐœ์ƒํ•  ์ˆ˜ ์žˆ๋Š” ํ˜„์‹œ์ ์—์„œ ์น˜์ˆ˜์ฆ๋Œ€ ์‚ฌ์—…์œผ๋กœ ์™„๊ณต๋œ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ์˜ ํ™œ์šฉ๋ฐฉ์•ˆ์— ๋Œ€ํ•œ ๊ธฐ์ดˆ์ž๋ฃŒ๋กœ ํ™œ์šฉ๋  ์ˆ˜ ์žˆ๊ณ , ํ–ฅํ›„ ๊ณ„ํš ํ™์ˆ˜๋Ÿ‰ ์œ ์ž… ์‹œ ์ตœ์ ์˜ ๋ฐฐ๋ถ„ ๋น„์œจ ๋ฐ ํ—ˆ์šฉ ๋ฐฉ๋ฅ˜๋Ÿ‰ ๋„์ถœ์— ์ด์šฉํ•  ์ˆ˜ ์žˆ๋‹ค. ๋‹ค๋งŒ ๋ณธ ์—ฐ๊ตฌ๋Š” ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜์— ๋”ฐ๋ฅธ ์ œ๋ฐฉ์— ์ž‘์šฉํ•˜๋Š” ์ˆ˜์ถฉ๋ ฅ์€ ๊ฒ€ํ† ํ•˜์ง€ ๋ชปํ•˜๊ณ , ํ—ˆ์šฉ ์œ ์† ๋ฐ ํ—ˆ์šฉ์†Œ๋ฅ˜๋ ฅ์€ ์ œ๋ฐฉ๊ณผ ์œ ์ˆ˜์˜ ๋ฐฉํ–ฅ์ด ์ผ์ •ํ•œ ๊ตฌ๊ฐ„์— ๋Œ€ํ•˜์—ฌ ๊ฒ€ํ† ํ•˜์˜€๋‹ค. ๋˜ํ•œ ์—ฌ์ˆ˜๋กœ ๋ฐฉ๋ฅ˜์— ๋”ฐ๋ฅธ ๋Œ€์•ˆ๋ถ€์—์„œ์˜ ์˜ํ–ฅ์— ๋Œ€ํ•ด์„œ๋งŒ ๊ฒ€ํ† ํ•˜์˜€๊ณ  ์ˆ˜๋ฌธ ์ „๋ฉด ๊ฐœ๋„ ์กฐ๊ฑด์—์„œ ๊ฒ€ํ† ํ•˜์˜€๋‹ค๋Š” ํ•œ๊ณ„์ ์€ ๋ถ„๋ช…ํžˆ ์žˆ๋‹ค. ์ด์— ํ–ฅํ›„์—๋Š” ๋‹ค์–‘ํ•œ ์ˆ˜๋ฌธ ๊ฐœ๋„ ์กฐ๊ฑด ๋ฐ ๋ฐฉ๋ฅ˜ ์‹œ๋‚˜๋ฆฌ์˜ค๋ฅผ ์ ์šฉ ๋ฐ ๊ฒ€ํ† ํ•˜์—ฌ ๋ณด๋‹ค ํšจ์œจ์ ์ด๊ณ , ํšจ๊ณผ์ ์ธ ๋ณด์กฐ ์—ฌ์ˆ˜๋กœ ํ™œ์šฉ๋ฐฉ์•ˆ์„ ๋„์ถœํ•˜๊ณ ์ž ํ•œ๋‹ค.

    Acknowledgements

    ๋ณธ ๊ฒฐ๊ณผ๋ฌผ์€ K-water์—์„œ ์ˆ˜ํ–‰ํ•œ ๊ธฐ์กด ๋ฐ ์‹ ๊ทœ ์—ฌ์ˆ˜๋กœ ํšจ์œจ์  ์—ฐ๊ณ„์šด์˜ ๋ฐฉ์•ˆ ๋งˆ๋ จ(2021-WR-GP-76-149)์˜ ์ง€์›์„ ๋ฐ›์•„ ์—ฐ๊ตฌ๋˜์—ˆ์Šต๋‹ˆ๋‹ค.

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    1 ๊ฑด์„ค๊ตํ†ต๋ถ€ยทํ•œ๊ตญ์ˆ˜์ž์›๊ณต์‚ฌ (2004). ๋Œ์˜ ์ˆ˜๋ฌธํ•™์  ์•ˆ์ •์„ฑ ๊ฒ€ํ†  ๋ฐ ์น˜์ˆ˜๋Šฅ๋ ฅ์ฆ๋Œ€๋ฐฉ์•ˆ ๊ธฐ๋ณธ๊ณ„ํš ์ˆ˜๋ฆฝ ๋ณด๊ณ ์„œ. ์„ธ์ข…: ๊ตญํ† ๊ตํ†ต๋ถ€.

    2 ๊ตญ๋ฌด์ด๋ฆฌ์‹ค ์ˆ˜ํ•ด๋ฐฉ์ง€๋Œ€์ฑ…๋‹จ (2003). ์ˆ˜ํ•ด๋ฐฉ์ง€๋Œ€์ฑ… ๋ฐฑ์„œ. ์„ธ์ข…: ๊ตญ๋ฌด์ด๋ฆฌ์‹ค.

    3 ๊ตญํ† ๊ตํ†ต๋ถ€ (2016). ํ•˜์ฒœ๊ณต์‚ฌ ์„ค๊ณ„์‹ค๋ฌด์š”๋ น. ์„ธ์ข…: ๊ตญํ† ๊ตํ†ต๋ถ€.

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    5 ๊น€๋Œ€๊ทผ, ๋ฐ•์„ ์ค‘, ์ด์˜์‹, ํ™ฉ์ข…ํ›ˆ (2008). ์ˆ˜์น˜๋ชจํ˜•์‹คํ—˜์„ ์ด์šฉํ•œ ์—ฌ์ˆ˜๋กœ ์„ค๊ณ„ – ์•ˆ๋™๋‹ค๋ชฉ์ ๋Œ. ํ•œ๊ตญ์ˆ˜์ž์›ํ•™ํšŒ ํ•™์ˆ ๋ฐœํ‘œํšŒ. 1604-1608.

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    10 ํ•œ๊ตญ์ˆ˜์ž์›๊ณต์‚ฌ (2021). ๋Œ๊ด€๋ฆฌ ๊ทœ์ •. ๋Œ€์ „: ํ•œ๊ตญ์ˆ˜์ž์›๊ณต์‚ฌ.

    Fig. 1- Schematic of the general pattern of flow and aeration process in the aerators

    2์ƒ ์œ ๋™ ํ•ด์„์„ ํ†ตํ•œ ์ŠˆํŠธ ํญ๊ธฐ ์‹œ์Šคํ…œ ํšจ์œจ์— ๋Œ€ํ•œ ๋žจํ”„ ๊ฐ๋„์˜ ์˜ํ–ฅ ์กฐ์‚ฌ

    Investigation of the Effect of Ramp Angle on Chute Aeration System Efficiency by Two-Phase Flow Analysis

    Authors

    1 Associate Professor, Civil Engineering Department, Jundi-Shapur University of Technology, Dezful, Iran

    2 Instructor in Civil Engineering Department Jundi-Shapur University of Technology, Dezful,Iran.

     10.22055/JISE.2021.37743.1980

    Abstract

    Flow aeration in chute spillway is one of the most effective and economic ways to prevent cavitation damage. Surface damage is significantly reduced when very small values of air are scattered in a water prism. A structure known as an aerator may be used for this purpose. Besides, ramp angle is one of the factors influencing aerator efficiency. In this research, the value of air entraining the flow through the Jarreh Damโ€™s spillway at the ramp angles of 6, 8 and 10 degrees, as three different scenarios, was simulated using the Flow-3D software. In order to validate the results of the inlet air into the flowing fluid at a ramp angle of 6 degrees, the observational results of the dam spillway physical model from the laboratory of TAMAB Company in Iran were used. According to the results, raising the ramp angle increases the inlet air to the water jet nappe, and a ten-degree ramp angle provides the best aeration efficiency. The Flow-3D model can also simulate the two-phase water-air flow on spillways, according to the results.

    ์ŠˆํŠธ ์—ฌ์ˆ˜๋กœ์˜ ํ๋ฆ„ ํญ๊ธฐ๋Š” ์บ๋น„ํ…Œ์ด์…˜ ์†์ƒ์„ ๋ฐฉ์ง€ํ•˜๋Š” ๊ฐ€์žฅ ํšจ๊ณผ์ ์ด๊ณ  ๊ฒฝ์ œ์ ์ธ ๋ฐฉ๋ฒ• ์ค‘ ํ•˜๋‚˜์ž…๋‹ˆ๋‹ค. ์ˆ˜์ค‘ ํ”„๋ฆฌ์ฆ˜์— ์•„์ฃผ ์ž‘์€ ์–‘์˜ ๊ณต๊ธฐ๊ฐ€ ํฉ์–ด์ง€๋ฉด ํ‘œ๋ฉด ์†์ƒ์ด ํฌ๊ฒŒ ์ค„์–ด๋“ญ๋‹ˆ๋‹ค. ์ด๋ฅผ ์œ„ํ•ด ํญ๊ธฐ ์žฅ์น˜๋กœ ์•Œ๋ ค์ง„ ๊ตฌ์กฐ๋ฅผ ์‚ฌ์šฉํ•  ์ˆ˜ ์žˆ์Šต๋‹ˆ๋‹ค. ๋˜ํ•œ, ๋žจํ”„ ๊ฐ๋„๋Š” ํญ๊ธฐ ํšจ์œจ์— ์˜ํ–ฅ์„ ๋ฏธ์น˜๋Š” ์š”์ธ ์ค‘ ํ•˜๋‚˜์ž…๋‹ˆ๋‹ค. ์ด ์—ฐ๊ตฌ์—์„œ๋Š” FLOW-3D ์†Œํ”„ํŠธ์›จ์–ด๋ฅผ ์‚ฌ์šฉํ•˜์—ฌ 3๊ฐ€์ง€ ๋‹ค๋ฅธ ์‹œ๋‚˜๋ฆฌ์˜ค์ธ 6, 8 ๋ฐ 10๋„์˜ ๋žจํ”„ ๊ฐ๋„์—์„œ Jarreh ๋Œ์˜ ๋ฐฉ์ˆ˜๋กœ๋ฅผ ํ†ตํ•ด ํ๋ฆ„์„ ๋™๋ฐ˜ํ•˜๋Š” ๊ณต๊ธฐ์˜ ๊ฐ’์„ ์‹œ๋ฎฌ๋ ˆ์ด์…˜ํ–ˆ์Šต๋‹ˆ๋‹ค. 6๋„์˜ ๊ฒฝ์‚ฌ๊ฐ์—์„œ ์œ ๋™ ์œ ์ฒด๋กœ ์œ ์ž…๋˜๋Š” ๊ณต๊ธฐ์˜ ๊ฒฐ๊ณผ๋ฅผ ๊ฒ€์ฆํ•˜๊ธฐ ์œ„ํ•ด์ด๋ž€ TAMAB Company์˜ ์‹คํ—˜์‹ค์—์„œ ๋Œ ๋ฐฉ์ˆ˜๋กœ ๋ฌผ๋ฆฌ์  ๋ชจ๋ธ์˜ ๊ด€์ฐฐ ๊ฒฐ๊ณผ๋ฅผ ์‚ฌ์šฉํ–ˆ์Šต๋‹ˆ๋‹ค. ๊ฒฐ๊ณผ์— ๋”ฐ๋ฅด๋ฉด ๋žจํ”„ ๊ฐ๋„๋ฅผ ๋†’์ด๋ฉด ์›Œํ„ฐ์ œํŠธ ๊ธฐ์ €๊ท€๋กœ ์œ ์ž…๋˜๋Š” ๊ณต๊ธฐ๊ฐ€ ์ฆ๊ฐ€ํ•˜๊ณ  10๋„ ๋žจํ”„ ๊ฐ๋„๋Š” ์ตœ๊ณ ์˜ ํญ๊ธฐ ํšจ์œจ์„ ์ œ๊ณตํ•ฉ๋‹ˆ๋‹ค. Flow-3D ๋ชจ๋ธ์€ ๊ฒฐ๊ณผ์— ๋”ฐ๋ผ ์—ฌ์ˆ˜๋กœ์˜ 2๋‹จ๊ณ„ ๋ฌผ-๊ณต๊ธฐ ํ๋ฆ„์„ ์‹œ๋ฎฌ๋ ˆ์ด์…˜ํ•  ์ˆ˜๋„ ์žˆ์Šต๋‹ˆ๋‹ค.

    Keywords

    Fig. 1- Schematic of the general pattern of flow and aeration process in the aerators
    Fig. 1- Schematic of the general pattern of flow and aeration process in the aerators
    (a) The full-scale map of the Jarreh spillwayโ€™s plan and profile.
    (a) The full-scale map of the Jarreh spillwayโ€™s plan and profile.
    Fig. 2- Experimental setup (Shamloo et al., 2012)
    Fig. 2- Experimental setup (Shamloo et al., 2012)

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    Figure 2. Schematic diagram for pilot-scale cooling-water circulation system (a) along with a real picture of the system (b).

    Application of Computational Fluid Dynamics in Chlorine-Dynamics Modeling of In-Situ Chlorination Systems for Cooling Systems

    Jongchan Yi 1, Jonghun Lee 1, Mohd Amiruddin Fikri 2,3, Byoung-In Sang 4 and Hyunook Kim 1,*

    Abstract

    ์—ผ์†Œํ™”๋Š” ์ƒ๋Œ€์ ์ธ ํšจ์œจ์„ฑ๊ณผ ์ €๋ ดํ•œ ๋น„์šฉ์œผ๋กœ ์ธํ•ด ๋ฐœ์ „์†Œ ๋ƒ‰๊ฐ ์‹œ์Šคํ…œ์—์„œ ์ƒ๋ฌผํ•™์  ์˜ค์—ผ์„ ์ œ์–ดํ•˜๋Š”โ€‹โ€‹๋ฐ ์„ ํ˜ธ๋˜๋Š” ๋ฐฉ๋ฒ•์ž…๋‹ˆ๋‹ค. ํ•ด์•ˆ ์ง€์—ญ์— ๋ฐœ์ „์†Œ๊ฐ€ ์žˆ๋Š” ๊ฒฝ์šฐ ๋ฐ”๋‹ท๋ฌผ์„ ์‚ฌ์šฉํ•˜์—ฌ ํ˜„์žฅ์—์„œ ์—ผ์†Œ๋ฅผ ์ „๊ธฐํ™”ํ•™์ ์œผ๋กœ ์ƒ์„ฑํ•  ์ˆ˜ ์žˆ์Šต๋‹ˆ๋‹ค. ์ด๋ฅผ ํ˜„์žฅ ์ „๊ธฐ์—ผ์†Œํ™”๋ผ๊ณ  ํ•ฉ๋‹ˆ๋‹ค. ์ด ์ ‘๊ทผ ๋ฐฉ์‹์€ ์œ ํ•ดํ•œ ์—ผ์†Œํ™” ๋ถ€์‚ฐ๋ฌผ์ด ์ ๊ณ  ์—ผ์†Œ๋ฅผ ์ €์žฅํ•  ํ•„์š”๊ฐ€ ์—†๋‹ค๋Š” ์ ์„ ํฌํ•จํ•˜์—ฌ ๋ช‡ ๊ฐ€์ง€ ์žฅ์ ์ด ์žˆ์Šต๋‹ˆ๋‹ค. ๊ทธ๋Ÿผ์—๋„ ๋ถˆ๊ตฌํ•˜๊ณ , ์ด ์ „๊ธฐํ™”ํ•™์  ๊ณต์ •์€ ์‹ค์ œ๋กœ๋Š” ์•„์ง ์ดˆ๊ธฐ ๋‹จ๊ณ„์— ์žˆ์Šต๋‹ˆ๋‹ค. ์ด ์—ฐ๊ตฌ์—์„œ๋Š” ํŒŒ์ผ๋Ÿฟ ๊ทœ๋ชจ ๋ƒ‰๊ฐ ์‹œ์Šคํ…œ์—์„œ ์—ผ์†Œ ๋ถ•๊ดด๋ฅผ ์‹œ๋ฎฌ๋ ˆ์ด์…˜ํ•˜๊ธฐ ์œ„ํ•ด ๋ณ‘๋ ฌ 1์ฐจ ๋™์—ญํ•™์„ ์ ์šฉํ–ˆ์Šต๋‹ˆ๋‹ค. ๋ถ•๊ดด๊ฐ€ ์ทจ์ˆ˜๊ด€์„ ๋”ฐ๋ผ ๋ฐœ์ƒํ•˜๊ธฐ ๋•Œ๋ฌธ์— ๋™์—ญํ•™์€ ์ „์‚ฐ์œ ์ฒด์—ญํ•™(CFD) ์ฝ”๋“œ์— ํ†ตํ•ฉ๋˜์—ˆ์œผ๋ฉฐ, ์ดํ›„์— ํŒŒ์ดํ”„์˜ ์—ผ์†Œ ๊ฑฐ๋™์„ ์‹œ๋ฎฌ๋ ˆ์ด์…˜ํ•˜๋Š”๋ฐ ์ ์šฉ๋˜์—ˆ์Šต๋‹ˆ๋‹ค. ์‹คํ—˜๊ณผ ์‹œ๋ฎฌ๋ ˆ์ด์…˜ ๋ฐ์ดํ„ฐ๋Š” ๊ฐ•ํ•œ ๋‚œ๋ฅ˜๊ฐ€ ํ˜•์„ฑ๋˜๋Š” ์กฐ๊ฑดํ•˜์—์„œ๋„ ํŒŒ์ดํ”„ ๋ฒฝ์„ ๋”ฐ๋ผ ์—ผ์†Œ ๋†๋„๊ฐ€ ์ ์ง„์ ์ธ ๊ฒƒ์œผ๋กœ ๋‚˜ํƒ€๋‚ฌ์Šต๋‹ˆ๋‹ค. ์—ผ์†Œ๊ฐ€ ์ค‘๊ฐ„๋ณด๋‹ค ํŒŒ์ดํ”„ ํ‘œ๋ฉด์„ ๋”ฐ๋ผ ํ›จ์”ฌ ๋” ์ง‘์ค‘์ ์œผ๋กœ ๋‚จ์•„ ์žˆ๋‹ค๋Š” ์‚ฌ์‹ค์€ ์ „๊ธฐ ์—ผ์†Œํ™”๋ฅผ ๊ธฐ๋ฐ˜์œผ๋กœ ํ•˜๋Š” ์‹œ์Šคํ…œ์˜ ์ „์ฒด ์—ผ์†Œ ์š”๊ตฌ๋Ÿ‰์„ ๊ฐ์†Œ์‹œํ‚ฌ ์ˆ˜ ์žˆ์—ˆ์Šต๋‹ˆ๋‹ค. ํ˜„์žฅ ์ „๊ธฐ ์—ผ์†Œํ™” ๋ฐฉ์‹์˜ ๋ƒ‰๊ฐ ์‹œ์Šคํ…œ์€ ์ง์ ‘ ์ฃผ์ž… ๋ฐฉ์‹์— ํ•„์š”ํ•œ ์—ผ์†Œ ์‚ฌ์šฉ๋Ÿ‰์˜ 1/3๋งŒ ์†Œ๋น„ํ–ˆ์Šต๋‹ˆ๋‹ค. ๋”ฐ๋ผ์„œ ํ˜„์žฅ ์ „๊ธฐ์—ผ์†Œํ™”๋Š” ํ•ด์•ˆ ์ง€์—ญ์˜ ๋ฐœ์ „์†Œ์—์„œ ๋ฐ”์ด์˜คํŒŒ์šธ๋ง ์ œ์–ด๋ฅผ ์œ„ํ•œ ๋น„์šฉ ํšจ์œจ์ ์ด๊ณ  ํ™˜๊ฒฝ ์นœํ™”์ ์ธ ์ ‘๊ทผ ๋ฐฉ์‹์œผ๋กœ ์‚ฌ์šฉ๋  ์ˆ˜ ์žˆ๋‹ค๊ณ  ๊ฒฐ๋ก ์ง€์—ˆ์Šต๋‹ˆ๋‹ค.

    Chlorination is the preferred method to control biofouling in a power plant cooling system due to its comparative effectiveness and low cost. If a power plant is located in a coastal area, chlorine can be electrochemically generated in-situ using seawater, which is called in-situ electrochlorination; this approach has several advantages including fewer harmful chlorination byproducts and no need for chlorine storage. Nonetheless, this electrochemical process is still in its infancy in practice. In this study, a parallel first-order kinetics was applied to simulate chlorine decay in a pilot-scale cooling system. Since the decay occurs along the water-intake pipe, the kinetics was incorporated into computational fluid dynamics (CFD) codes, which were subsequently applied to simulate chlorine behavior in the pipe. The experiment and the simulation data indicated that chlorine concentrations along the pipe wall were incremental, even under the condition where a strong turbulent flow was formed. The fact that chlorine remained much more concentrated along the pipe surface than in the middle allowed for the reduction of the overall chlorine demand of the system based on the electro-chlorination. The cooling system, with an in-situ electro-chlorination, consumed only 1/3 of the chlorine dose demanded by the direct injection method. Therefore, it was concluded that in-situ electro-chlorination could serve as a cost-effective and environmentally friendly approach for biofouling control at power plants on coastal areas.

    Keywords

    computational fluid dynamics; power plant; cooling system; electro-chlorination; insitu chlorination

    Figure 1. Electrodes and batch experiment set-up. (a) Two cylindrical electrodes used in this study. (b) Batch experiment set-up for kinetic tests.
    Figure 1. Electrodes and batch experiment set-up. (a) Two cylindrical electrodes used in this study. (b) Batch experiment set-up for kinetic tests.
    Figure 2. Schematic diagram for pilot-scale cooling-water circulation system (a) along with a real picture of the system (b).
    Figure 2. Schematic diagram for pilot-scale cooling-water circulation system (a) along with a real picture of the system (b).
    Figure 3. Free chlorine decay curves in seawater with different TOC and initial chlorine concentration. Each line represents the predicted concentration of chlorine under a given condition. (a) Artificial seawater solution with 1 mg Lโˆ’1 of TOC; (b) artificial seawater solution with 2 mg Lโˆ’1 of TOC; (c) artificial seawater solution with 3 mg Lโˆ’1 of TOC; (d) West Sea water (1.3 mg Lโˆ’1 of TOC).
    Figure 3. Free chlorine decay curves in seawater with different TOC and initial chlorine concentration. Each line represents the predicted concentration of chlorine under a given condition. (a) Artificial seawater solution with 1 mg Lโˆ’1 of TOC; (b) artificial seawater solution with 2 mg Lโˆ’1 of TOC; (c) artificial seawater solution with 3 mg Lโˆ’1 of TOC; (d) West Sea water (1.3 mg Lโˆ’1 of TOC).
    Figure 4. Correlation between model and experimental data in the chlorine kinetics using seawater.
    Figure 4. Correlation between model and experimental data in the chlorine kinetics using seawater.
    Figure 5. Free chlorine concentrations in West Sea water under different current conditions in an insitu electro-chlorination system.
    Figure 5. Free chlorine concentrations in West Sea water under different current conditions in an insitu electro-chlorination system.
    Figure 6. Free chlorine distribution along the sampling ports under different flow rates. Each dot represents experimental data, and each point on the black line is the expected chlorine concentration obtained from computational fluid dynamics (CFD) simulation with a parallel first-order decay model. The red-dotted line is the desirable concentration at the given flow rate: (a) 600 L minโˆ’1 of flow rate, (b) 700 L minโˆ’1 of flow rate, (c) 800 L minโˆ’1 of flow rate, (d) 900 L minโˆ’1 of flow rate.
    Figure 6. Free chlorine distribution along the sampling ports under different flow rates. Each dot represents experimental data, and each point on the black line is the expected chlorine concentration obtained from computational fluid dynamics (CFD) simulation with a parallel first-order decay model. The red-dotted line is the desirable concentration at the given flow rate: (a) 600 L minโˆ’1 of flow rate, (b) 700 L minโˆ’1 of flow rate, (c) 800 L minโˆ’1 of flow rate, (d) 900 L minโˆ’1 of flow rate.
    Figure 7. Fluid contour images from CFD simulation of the electro-chlorination experiment. Inlet flow rate is 800 L minโˆ’1. Outlet pressure was set to 10.8 kPa. (a) Chlorine concentration; (b) expanded view of electrode side in image (a); (c) velocity magnitude; (d) pressure.
    Figure 7. Fluid contour images from CFD simulation of the electro-chlorination experiment. Inlet flow rate is 800 L minโˆ’1. Outlet pressure was set to 10.8 kPa. (a) Chlorine concentration; (b) expanded view of electrode side in image (a); (c) velocity magnitude; (d) pressure.
    Figure 8. Chlorine concentration contour in the simulation of full-scale in-situ electro-chlorination with different cathode positions. The pipe diameter is 2 m and the flow rate is 14 m3 sโˆ’1. The figure shows 10 m of the pipeline. (a) The simulation result when the cathode is placed on the surface of the pipe wall. (b) The simulation result when the cathode is placed on the inside of the pipe with 100 mm of distance from the pipe wall.
    Figure 8. Chlorine concentration contour in the simulation of full-scale in-situ electro-chlorination with different cathode positions. The pipe diameter is 2 m and the flow rate is 14 m3 sโˆ’1. The figure shows 10 m of the pipeline. (a) The simulation result when the cathode is placed on the surface of the pipe wall. (b) The simulation result when the cathode is placed on the inside of the pipe with 100 mm of distance from the pipe wall.
    Figure 9. Comparison of in-situ electro-chlorination and direct chlorine injection in full-scale applications. (a) Estimated chlorine concentrations along the pipe surface. (b) Relative chlorine demands.
    Figure 9. Comparison of in-situ electro-chlorination and direct chlorine injection in full-scale applications. (a) Estimated chlorine concentrations along the pipe surface. (b) Relative chlorine demands.

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