• Proceedings of the Korea Water Resources Association Conference
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• 2011.05a
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• pp.134-134
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• 2011

3차원 난류 부력젵의 혼합을 큰 와 모의(large-eddy simulation) 기법을 이용하여 수치모의 한다. 개발된 수치모형은 3차원 열동수역학 모형을 이용하여 부력젵의 퍼짐, 자기 보존 그리고 주변류의 연행 등을 포함하는 난류젵의 동적 특성을 분석할 수 있다. 수치해석에서 하부격자규모 (subgrid scale, SGS) 난류 응력은 부력항을 수정한 Smagorinsky 모형을 이용한다. 여과된 엔탈피 수송방정식에서 하부격자규모의 스칼라 플럭스는 상수의 SGS Prandtl 수를 가지는 단순 경사수송 가설에 근거하여 모의한다. 계산된 결과를 실험결과와 비교하며, 결과는 양호하게 일치함을 보여준다. 계산결과에 따르면 부력항의 수정이나 SGS 난류 Prandtl 수는 결과에 큰 영향을 미치지 않지만 SGS 모형 상수인 Cs 값은 부력젵 확산 예측에 중요한 영향을 미치는 것으로 나타났다.

• Journal of Korea Water Resources Association
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• v.30 no.5
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• pp.467-475
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• 1997

In this study, breakwater model which has several outlet pipes to discharge heated water is settled in the experimental open channel and velocity distribution of wall jet is measured. Numerical simulation of velocity structure of wall jet using 3-dimensional computer model. Fluent model, is also carried out. The calculated results are verified with the experimental results and the flow characteristics of wall jet are investigated. The length of zone of flow establishment of wall jet is shorter than that of free jet, and the diminution rate of jet centerline longitudinal velocity is larger than that of free jet. Characteristics of buoyant jet and non-buoyant simple jet simulated by Fluent model are compared. Near the outlet pipe, in the region where x/lQ is over 15, this is reversed. Comparison of vertical distribution of longitudinal velocity shows that positive velocity of non-buoyant jet is bigger than that of buoyant jet in the bottom layer and in the upper layer, negative velocity of non-buoyant jet is bigger too. Flow separation in free surface of the buoyant jet occurs in smaller distances from the outlet than the non-buoyant jet. Buoyant jet expands faster than the non-buoyant jet in vertical direction.

• Journal of Korean Society of Coastal and Ocean Engineers
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• v.6 no.1
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• pp.34-39
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• 1994

The dilution and the shore attachment of buoyant effluent into a crossflow are investigated experimentally. The effluent is produced by discharging warm water through a side channel into an open channel crossflow with the same depth to the side channel flow. Buoyancy causes the effluent to lift off the bottom, spreads across the crossflow and stays as the surface layer. The geometry of the recirculating region and the dilution of the effluent depend mainly on the buoyancy. The condition of the shore attachment can be specified by the ratios of velocities and Froude numbers.