• 한국유체기계학회 논문집
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• 제19권4호
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• pp.48-53
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• 2016

The centrifugal separator which uses gravity separation method for oil-water separation, rotating at high-speed, is one of the most commonly used device for controlling the amount of the oil in waste water collected in bilge. The IMO (International Maritime Organization) has set regulations, also known as MARPOL 73/78, for the prevention of marine pollution. In addition, DET NORSKE VERITAS (DNV) has set standards regarding the assignment of Environmental Class Notation, CLEAN or CLEAN DESIGN, of ships. One of the requirements for classification is that in addition to conforming to MARPOL 73/78, more stringent measures must be taken as well. One of these measures is to limit the oil concentration in bilge water to less than 5ppm. So in this study, an Oil-Water Separator (OWS) is used together with multiple separating plates as a filtration system to be used as an oil-water separation device. The OWS operates using centrifugal separation in which the mixture is separated by centrifugal forces. The main purpose of this paper is to present the OWS separation efficiency according to the rotation speed, mass-flow rate, the angle and the number of stacked layers of the laminated plate using Computational Fluid Dynamics (CFD). Improvements to the device will be investigated from these results.

• 상하수도학회지
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• 제19권1호
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• pp.38-46
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• 2005

In this research, we tried to combine the coagulation/sedimentation process as pre-treatment with UF membrane filtration to reduce the membrane fouling and to improve the permeate water quality. We used the Jet Mixed Separator (JMS) as coagulation/sedimentation process. We observed that the HPC and E.Coli can't be removed through the direct UF memebrane filtation of surface water. The removal efficiency of dissolved organic substances, indicated by E260 and DOC, was 40% and 15%, respectively. However, the removal efficiency of it increased two time as a result of combination of JMS process as coagulation/sedimentation pre-treatment. This was resulted from the formation of high molecular humic micro-floc through JMS process. The accumulation amount of irreversible cake layer which was not removed by backwashing was less than direct UF membrane filtration of surface water. Moreover, the loading rate of fouling induced substances, such as humic substances and suspended substances, on membrane surface decreased drastically through JMS process. As a result, the accumulation amount of irreversible cake on membrane surface was decreased.

• 한국항해항만학회:학술대회논문집
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• 한국항해항만학회 2005년도 추계학술대회 논문집
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• pp.175-179
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• 2005

새롭게 적용되는 IMO 규정에 적합한 Bilge Separator를 개발하기 위하여 Bilge 폐수에 함유된 Emulsion의 처리가 매우 중요하다. 에멀젼의 경우 그 안정성으로 인해 육상에서도 처리하기가 매우 까다로운데 본 연구에서는 화학적인 방법을 이용하여 Emulsion의 안정성을 파괴하여 처리하고자 하였다. 파괴된 기름 입자는 서로 응집하여 부상처리 되게 되는데, 선박은 특성상 장치의 설치장소가 협소하기 때문에 Bilge 폐수의 처리에 시간이 충분치 않다. 이러한 문제의 해결과 화학적 처리에 가장 기본이 되는 응집제의 선정과 기본적인 환경요인들을 결정하여 실험을 진행하였다. 실험결과 국내 제품 중의 응집제를 선정하였고 가장 응집효과가 좋은 pH 영역과 응집제의 투여량을 결정하여 이를 바탕으로 에멀젼 함유 Bilge 폐수를 처리한 결과 IMO에서 정한 기준을 만족하는 결과를 얻을 수 있었다.

• 한국해양공학회지
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• 제28권4호
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• pp.280-287
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• 2014

In this paper, the numerical simulation of the gas-liquid flow in a cylinder cyclone separator is performed to investigate the flow characteristics using a commercial software, FLUENT, which solves the Reynolds-averaged Navier-Stokes(RaNS) equations. First, a single-phase flow with water in a gas-liquid cylinder cyclone(GLCC) separator is simulated and compared with the experiments(Farchi, 1990) and numerical simulations(Erdal, 1997). Then, the characteristics of the multi-phase flow for water-air, mud-only, and mud-air cases are discussed in the view point of the feasibilities for a mud handling system.

• 한국물환경학회지
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• 제27권3호
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• pp.342-348
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• 2011

A hydrodynamic separator using natural free energy provided by bridge was operated for the treatment of stormwater runoff. The separator was automatically controlled by using electronic valve which is connected with pressure meter. Normally the separator was opened during dry days, but it was closed after the capture of first flush. The results indicated that the average pressure and the flow rate were directly affected by the rainfall intensity. The pressure was more than 3 meters as the rainfall intensity was above 5 mm/hr. The percent volume of underflow decreased as the pressure and flow rate increased, but the percent volume of overflow showed an opposite behavior. The concentration of total suspended solids (TSS) in underflow increased as a function of increasing pressure while it decreased in overflow. The TSS separation efficiency was evaluated based on mass balance. It ranged from 30% to 90% with the pressure ranging from 2 to 10 meters, and it was proportional to pressure and flow rate. The analysis of water balance indicated that around 13% of total runoff was captured by the separator as a first flush, and this runoff was separated as underflow and overflow with the respective percent volume of 29% and 71%. The pollutants budget was also examined based on mass balance. The results showed that the percent of TSS, $COD_{cr}$, TN and TP in underflow were 73%, 59%, 7.6% and 49%, respectively.

• 수산해양기술연구
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• 제44권2호
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• pp.99-111
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• 2008

The purpose of this study is to develop the jellyfish separator system(JSS) for reducing fishery damage by the increase of jellyfish in the sea area of Korea in summer. First of all, to find the optimum structure of a JSS, six types of JSS in trawl fishery were designed and manufactured, the underwater shape of JSS and the separating process by JSS were observed in the circulating water channel(CWC). And the field experiments were carried out in July and September 2004 in the southern sea of Korea. For the moving path of the jellyfish model in the CWC, in case that the model was larger than the mesh size of the separator net, it was guided toward the lower part of the separator net by the guiding net and discharged through the outlet. In case that the model was smaller than the mesh size of the separator net, some models which passed through the upper part of the guiding net were smaller than the mesh size of the guiding net and discharged through the outlet and most of the model which passed through the lower part of the guiding net moved to the codend passing through the separator net. According to the field experiment result, the optimum tilt angle of separator net was inferred $20^{\circ}$ that the discharge rate of jellyfish was higher than the other tilt angle of separator net and the optimum structure of JSS was inferred GS type(consists of guiding net and separator net) that the discharge rate of jellyfish was higher than S type(consists of separator net). It was demamded to carry out more study for the countermeasure to reduce loss of fish.

• 해양환경안전학회:학술대회논문집
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• 해양환경안전학회 2006년도 춘계학술발표회
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• pp.103-108
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• 2006

새롭게 적용되는 IMO 규정에 적합한 선박의 15ppm Bilge Separator를 개발하기 위하여 Bilge 폐수에 함유된 Emulsion 의 처리가 매우 중요하다. 에멀젼의 경우 그 안정성으로 인해 육상에서도 처리하기가 매우 까다로운데 본 연구에서는 화학적인 방법을 이용하여 Emulsion의 안정성을 파괴하여 처리하고자 하였다 파괴된 기름 입자는 서로 응집하여 부상처리 되는데, 선박은 특성상 장치의 설치장소가 협소하기 때문에 Bilge 폐수의 처리에 시간이 충분치 않다. 이러한 문제의 해결과 화학적 처리에 가장 기본이 되는 응집제의 선정과 기본적인 환경요인들을 결정하여 실험을 진행하였다. 실험결과 국내 제품 중의 응집제를 선정하였고 가장 응집 효과가 좋은 pH 영역과 응집제의 투여량을 결정하였으며 기초 실험을 통해 최적효율을 나타내는 부상방법을 결정하여 이를 바탕으로 Pilot Plant를 제작하여 에멀젼 함유 Bilge 폐수를 처리한 결과 IMO에서 정한 기준을 만족하는 결과를 얻을 수 있었다.

• 한국산업융합학회 논문집
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• 제26권5호
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• pp.803-812
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• 2023

The subsea separator of an offshore plant for offshore oil and gas development performs the process of separating oil and gas from crude oil produced in the subsea. The oil-gas subsea separator can be divided into a gravity type that separates fluids by gravity and an in-line type that separates fluids using centrifugal force of density. In the case of the deep sea, the development of a small in-line type separator is required due to manufacturing cost and safety problems caused by water pressure. Therefore, in this study, the gas-liquid phase separation efficiency of the subsea separator was identified through the study of the multiphase flow characteristics of the in-line type separator. For the optimal design of the in-line type separator, the shape of the internal swirl element(ISE) was selected first, and the separation efficiency results for each section of the in-line type separator were analyzed. This study was conducted in parallel with experiments and numerical analysis, and it is expected that the reliability and efficiency of the in-line type separator will be improved through the results.

• 상하수도학회지
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• 제23권5호
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• pp.557-564
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• 2009

A combined sewer system can quickly drain both storm water and sewage, improve the living environment and resolve flood measures. A combined sewer system is much superior to separate sewer system in reduction of the non-point source pollutant load. However, during rainfall. it is impossible in time, space and economic terms to cope with the entire volume of storm water. A sewage system that exceeds the capacity of the sewer facilities drain into the river mixed with storm-water. In addition, high concentration of CSOs by first-flush increase pollution load and reduce treatment efficiency in sewage treatment plant. The aim of this study was to develope a processing unit for the removal of high CSOs concentrations in relation to water quality during rainfall events in a combined sewer. The most suitable operational design for processing facilities under various conditions was also determined. With a designed discharge of 19.89 m/min, the removal efficiency was good, without excessive overflow, but it was less effective in relation to underflow, and decreased with decreasing particle size and specific gravity. It was necessary to lessen radius of vortex separator for increasing inlet velocity in optimum range for efficient performance, and removal efficiency was considered to high because of rotation increases through enlargement of comparing height of vortex separator in diameter. By distribution of influent particle size, the actual turbulent flow and experimental results was a little different from the theoretical removal efficiency due to turbulent effect in device.

• 대한기계학회논문집B
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• 제41권9호
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• pp.571-577
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• 2017

본 연구는 수치해석 기법을 활용하여 오일샌드 플랜트에 사용되는 다상유동분리기의 다양한 유입구 형상에 따른 효율 분석에 관한 연구이다. 본 연구에 사용된 유수분리기(FWKO, Free-water knockout)는 유량 $15,89m^3/d$(100 bbl/d), SOR(Steam-to-Oil Ratio) 3.5의 값을 가지며 Stokes 이론을 기반으로 설계되었다. 모듈화를 위하여 두 개의 유수분리기를 병렬 연결하였고 이에 따른 유입구 형상 최적화를 수행하였다. 유입구를 통해 유입되는 비투멘 에멀젼은 $150^{\circ}C$, 50 bar이며, API는 17의 값을 갖는다. 유수분리공정의 평균체류시간은 물과 오일이 95% 분리되는 시간으로 정의하였다. 다상유동의 밀도차에 의한 중력분리과정을 모사하기 위하여 유한체적법(VOF, Volume Of Fluid)과 상차분모델(DPM, Discrete Phase Model)을 조합하여 활용하였으며 준과도(Pseudo-transient) 해석기법을 활용하였다.