• Journal of Korean Society of Water and Wastewater
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• v.26 no.3
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• pp.423-430
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• 2012

This study was conducted to qualify the equality of the flow distribution from open channel between rapid mixing basin and flocculation basins in a domestic S_ water treatment plant, and to suggest a remedy for improving the equality. In order to evaluate the feasibility of the suggested remedy, computational fluid dynamics (CFD) technique are used, and for verifying the CFD simulation results tracer tests were carried out. From the results of CFD simulation and tracer tests, it was investigated that the modification of hydraulic structure in the distribution channel, which is to install the longitudinal orifice baffle in flow direction, could improve the equality of the flow distribution over 75%.

• Journal of Korean Society of Water and Wastewater
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• v.28 no.2
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• pp.217-223
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• 2014

In order to suggest the methodology for improving the equity of flow distribution in open channel with multiple outlet, CFD simulations were carried out for actual scale distribution channel being operated in domestic G_WTP(Water Treatment Plant). Also, before and after installing the longitudinal multi hole(diameter=250 mm, 116 holes) baffle suggested by this research, turbidity measurements data were collected for evaluating the effects of hydraulic modification for inlet flow equity. From the both results, total turbidity of settled water was lowered by 30 % and equity of flow distribution was improved about 60 % compared with before hydraulic structure modification.

• Journal of Korean Society of Environmental Engineers
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• v.35 no.12
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• pp.918-928
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• 2013

The inequitable flow distribution to flocculation basins is an important problem faced in many water treatment plants. This is caused by the structure of a distribution channel, the height differences of outlet weirs etc. But, a modified approach for the structures has no effectiveness to achieve flow equality. The aim of this study is to reduce the inequality by adopting optimized inlet valve opening (%) of the flocculation basins using DOE (Design of Experiments) and RSA (Response Surface Analysis). The inlet valve openings (%) and inflow distributions (%) of 6 paralleled basins were set as factors (X) and characteristics(Y) respectively. 2 level factorial experiments and RSA were conducted for optimization and regression analysis (Y = f(X) + Const.). Adopting the optimized inlet valve opening (%) at field, standard deviation of flow distribution (%) and effluent turbidity was declined from 3.80% to 0.42% and from 0.29 NTU to 0.03 NTU respectively.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.38 no.9
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• pp.789-795
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• 2014

In this study, the distribution characteristics of diffusers with various shapes that are installed in an open-type thermal storage system are numerically investigated. Four diffusers are designed to distribute a working fluid evenly through the holes on bifurcated pipes. Three-dimensional steady simulations of incompressible laminar flow are conducted using commercial software (ANSYS-FLUENT). The simulation results show that both the bidirectional header-type diffuser and the H-type diffuser distribute the working fluid evenly whereas both the unidirectional and the bidirectional diffusers distribute the working fluid unevenly. The results also show that the H-type diffuser requires a higher head of pump than the bidirectional header-type diffuser. Therefore, the bidirectional header-type diffuser is recommended for use because it enables even distribution of the working fluid and requires a low head of pump.

• Proceedings of the Korea Water Resources Association Conference
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• 2006.05a
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• pp.1677-1680
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• 2006

하수처리장의 침전지 구조물은 고형물(SS) 및 현탁물을 침전, 제거하여 하수의 정화를 도모하는 시설로 초기 유입 하수의 생물학적 처리로 인해 발생되는 슬러지와 처리수를 분리함에 그 목적을 두고 있다. 침전지 구조물은 장소의 제약 및 침전지의 효율성 측면에서 많은 공법이 제안되고 있으며, 그중 이층 침전지의 경우 구조물의 시공비용 절감 및 공간 활용측면에서 단층 침전지에 비해 우수성을 인정받고 있다. 하지만 상 하 층에 위치하고 있는 침전지 유입부의 위치적 특성으로 인해 균등한 유량의 분배가 이루어지지 않고 유량이 한곳에 집중되는 현상으로 보일 수 있다. 본 연구에서는 3차원 수치모형인 FLOW-3D를 이용하여 이층 침전지의 유량분배 최적화를 위한 설계인자를 도출 하였다. 특히 상 하층에 위치하고 있는 유입부의 위치적인 특성을 고려하여 유입부의 직경을 상층 $500mm{\sim}600mm$, 하층 $500mm{\sim}700mm$으로 변화시키며 수치모의를 수행하였으며, 유입량의 분배효과를 확인하기 위해 각 동일한 위치에서 유입량을 산정하였다. 각 케이스별 분배효과를 분석한 결과 상 하층의 유입부 직경을 상층 600mm 와 하층 700mm를 적용했을 경우 유입량의 표준편차가 가장 작게 발생하며, 침전지 내부의 흐름이 원활하게 이루어지는 것으로 확인되었다. 본 연구에서는 상용 CFD모형인 FLOW-3D를 계획 중인 H하수처리장의 이층 침전지 설계에 적용하였으며 유입부 직경에 따른 분배효과를 분석하였다.

• Journal of Korean Society of Water and Wastewater
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• v.27 no.2
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• pp.215-222
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• 2013

The fluctuation of inlet flow to a water treatment plant makes a serious problem that it can change the outlet flowrate from each process abruptly. Since it takes very short time for the surface wave occurred from the fluctuation of inlet flow to reach the latter processes, it is impossible for operators to cope with that stably. In order to investigate the characteristics of hydraulic behavior for rectangular sedimentation basin in water treatment plant, CFD(Computational Fluid Dynamics) simulation were employed. From the results of both CFD simulations, it was confirmed that time taken for the follow-up processes by the fluctuation in intake well can be estimated by the propagation velocity of surface waves. Also, it takes very short time for the surface wave occurred from the fluctuation of inlet flow to reach the latter processes. In the case of inlet flowerate being increased sharply, local velocity within sedimentation basin appeared as wave pattern and increased due to convection current. Also, it could be observed that vortex made local velocity in the vicinity of bottom rise.

• Journal of Korean Society of Environmental Engineers
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• v.37 no.11
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• pp.607-618
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• 2015

This study was conducted to suggest hydraulic modification for improving evenness of inlet flow distribution into side stream type low-pressure MF (microfiltration) module using CFD (computational fluid dynamics) simulation and PIV (particle image velocimetry) techniques. From the results of CFD simulation for various typed inlet structure, it was investigated that installing internal orifice baffle in inlet the distribution channel could improve the evenness of inlet flow distribution over about 40%. Also, from the results of PIV measurements which were carried out for verifying the CFD simulation, it was observed that the momentum of the water body coming from the opposite side of the inlet was relatively larger. This momentum would generate strong shear force in the near of inlet side wall. On the other hands, occurrence of dead zone and eddy flow was confirmed in the opposite side.

• Proceedings of the Korea Water Resources Association Conference
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• 2016.05a
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• pp.332-332
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• 2016

수공구조물 설계시 hardware와 software의 발달로 수리계산과 수치해석의 오차율이 감소함에 따라 수치해석을 이용하는 빈도가 높아지고, 신뢰도가 향상되고 있는 추세에 있다. 그러나 댐 설계에 있어 수위별 방유량 관계 검토시 수치해석값은 각 수위에 해당하는 몇 개의 유량값을 대응시켜 경향만 비교하고 수리계산 결과를 설계에 반영해 왔다. 이러한 방법은 여수로 주변에 인접구조물이 없고, 여수로 각 수문별 균등한 유량이 방류될 경우 문제가 되지 않지만, 여수로 직상류 지형에 만곡부나 지형적 특성이 여수로 방류에 영향을 미치거나, 취수탑 등 여수로에 인접한 수리구조물이 설치되어 접근수로에서 복잡한 유동을 형성하는 경우 각 문비마다 방류량의 분배율은 달라질 수밖에 없고, 수리계산 결과를 일괄 반영하기에는 오차가 증가할 수밖에 없다. 이에 본 연구에서는 댐 운영시 중요한 인자 중 하나인 수위-방류량 관계에 대하여 수치모형을 이용한 정밀한 분석을 통하여 댐 여수로 운영시 오차율을 저감시키고, 적용성을 향상시키는 방안을 검토하였다. 첫째, 수위별 방류량 관계 검토시 여수로 상류에서 일정한 시간에 따라 선형적으로 수위가 증가하도록 경계조건을 설정한 후 3차원 수치해석 모형의 Output data를 단위시간에 따라 수위와 방류량이 산정되도록 하고, 기존 검토 방식대로 각 수위별 모형을 steady 상태로 수행하여 비교분석하였다. 수리계산과 기존 방식, 본 연구에서 제시한 방법에 대한 오차율 검토 결과 오차는 3 % 이내로 검토되었다. 둘째, 수치해석을 이용하여 수위별 방류량 산정시 접근유속에 대한 영향을 받게 되므로 수리계산시 에너지 경사를 이용하여 수위값을 반영하지만, 수치해석을 이용하여 수위별 방류량 산정시 경계조건을 부여한 수위값을 반영하거나, 임의의 지점에서의 수위값을 반영하는 경우 등 일괄적이지 않은 수위값을 반영하여 오차율이 증가하는 경향이 있다. 따라서, 본 연구에서는 여수로 지점별 전수두를 측정하여 방류량 값을 산정하여 비교하였다.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.15 no.5
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• pp.3336-3344
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• 2014

The purpose of this study is small scale coagulation module is developed and demonstrated through a lab-scale test. Recent as a sewage treatment rate increases, have heightened the interest in the necessity on the nonpoint source and developing a small processing unit has been increased. Coagulation sedimentation module in this study is additional growth of floc through swirling in the outside zone, reduction of microstructure floc number and the internal settling zone through vertical/level flow complex sedimentation method after the coagulation process precipitation method as an effective high separation efficiency can be divided was also assessed. Coagulation sedimentation module can increase the load factor was 4.4 times compared to conventional clarifier base on the same volume and surface area through vertical/level flow. In this study, this process was selected formation and maintenance of swirling and uniform flow distribution in the internal settling zone as an important design factor, to derive its FLUENT was used to characteristics of the flow model. Through the simulation of swirling, influent velocity, dimensions of external basin, hopper depth of bottom cone was determined and through analysis of velocity distribution, flow distribution detailed specifications are derived like as diameter and number of effluent hole. Lab-scale($120{\ell}/hr$) test results, influent of 300~800 NTU to less than 10 NTU without polymer feeding was able to operate in the 20minutes retention time(surface loading rate $37.3m^3/m^2$-day), and through analysis FLUENT the possibility of using design parameters were derived.