• Water Engineering Research
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• 제4권1호
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• pp.1-17
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• 2003

A mathematical model was developed to simulate the performance of a prototype wind-powered reverse osmosis desalination system. The model consists of two sub-models operated in a series. The first sub-model is the wind-energy conversion sub-model, which has wind energy and feed water as its input and pressurized feed water as its output. The second sub-model is a reverse osmosis (RO) process sub-model, with pressurized feed water as its input and the flow and salinity of the product water or permeate as its output. Model coefficients were determined based on field experiments of a prototype wind powered RO desalination system of the University of Hawaii, from June to December 2001. The mathematical model developed by this study predicts the performance of wind-powered RO desalination systems under different design conditions. The system optimization is achieved using a linear programming approach. Based on the results of system optimization, a design guide is prepared, which can be used by both manufacturer and end-user of the wind-driven reverse osmosis system.

• 멤브레인
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• 제12권3호
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• pp.151-157
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• 2002

본 연구는 하수를 공업용수로 재이용하기 위한 분리막 시스템 적용에 관한 연구이다. 정밀여과와 역삼투시스템으로 구성된 bench scale 실험장치를 이용하여 하수처리장 현장에서 실험을 수행한 결과, 정밀여과 시스템은 이온성분은 제거할 수 없었으나 SS를 70% 이상 처리할 수 있어 처리수는 직접냉각수로 재이용이 가능하였다. 그리고 역삼투 시스템은 SS는 물론 이온성분도 95% 이상 제거할 수 있어 처리수는 간접냉각수 및 제품세척수로 사용이 가능하였다. $100 m^3$/일 용량의 pilot Plant를 제작하기 위해서는 정밀여과 모듈은 20개, 역삼투 모듈은 12개가 필요하였다.

• 한국방재학회:학술대회논문집
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• 한국방재학회 2010년도 정기 학술발표대회
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• pp.101.2-101.2
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• 2010

현재 forward osmosis(FO)에 대한 관심이 증가하고 있다. 하지만 FO에 대한 안정성 평가는 전무한 실정이다. 본 연구는 많은 연구로 안정성을 인정받고 있는 RO와 직접 비교를 통하여 FO의 붕소에 대한 안정성을 평가하였다.

• 한국물환경학회지
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• 제20권4호
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• pp.307-312
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• 2004

This study was focused on experiment for the separation and concentration process of Cu(II), Zn(II) solution with the variation of applied pressure and concentration using reverse osmosis plate and frame modules. Rejection coefficient and degree of concentration for Cu(II) component using single and multi-stage reverse osmosis process were showed 96.3~97.8%, 0.044~0.191(in single-stage), 96.3~98.4%, 0.400~2.264(in multi-stage) within the range of experimental condition, respectively. Those of Zn(II) were 93.3~97.1%, 0.019~0.395(in single-stage), 96.3~98.2%, 0.365~1.454(in multi-stage), respectively. Degree of concentration of multi-stage were higher than those of single-stage. Heavy metal[Cu(II), Zn(II)] separation was very efficient in using reverse osmosis plate and frame type modules. Separation efficiency for a mixed solution Cu(II) and Zn(II) was higher than those of each one of Cu(II) and Zn(II).

• 공업화학
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• 제33권6호
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• pp.551-556
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• 2022

분리막을 활용한 수처리 공정을 통해 얻어진 담수된 물은 전 세계적인 물 부족 문제를 해결해 줄 수 있는 유망한 기술로 많은 주목을 받고 있다. 오늘날 담수화에 가장 널리 활용되고 있는 역삼투압 분리막 기반 공정은 지구상에 풍부한 바닷물을 담수화하는 기술이기 때문에 산업적으로도 그 잠재성이 매우 풍부하다. 이러한 담수 공정 성능을 향상시키기 위해서는 분리막의 역삼투압 메커니즘을 원자/분자 수준에서 이해할 필요가 있다. 본 총설에서는 오늘날 소재 연구에 있어 중요한 역할을 담당하고 있는 분자 전산모사에 대한 소개와 함께 역삼투압 분리막 연구 개발에 있어 원자/분자 수준에서의 전산모사 역할을 소개하고자 한다.

• 한국막학회:학술대회논문집
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• 한국막학회 1991년도 추계 총회 및 학술발표회
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• pp.9-16
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• 1991

The current status of reverse osmosis and ultrafiltration membranes are reviewed with the view for the future. In the case of reverse osmosis (RO) membranes, as examples, new crosslinked aromatic polyamide membranes exhibited the superior separation performance with the sufficient water permeability, the high tolerance for oxidizing agents and chemicals. Ultrafiltration (UF) membrane based on poly(phenylene sulfide sulfone) (PPSS) also exibited the superior separation performance with the high solvent, heat and fouling resistance.

• 한국막학회:학술대회논문집
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• 한국막학회 2004년도 Proceedings of the second conference of aseanian membrane society
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• pp.170-174
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• 2004

Most of thin film composite reverse osmosis membranes include amide linkages, which are susceptible to chlorine attack resulting in N-chloro derivatives. This study examined a new method based on post-treatment of reverse osmosis membrane with various silane derivatives to improve chlorine resistance. The silane derivatives contain one alkyl group and three alkoxy groups such as trifluoromethyltrimethoxysilane, 3-aminopropylmethoxydiethoxysilane and 3, 3, 3-trifluoropropyltrimethoxysilane. Compared to commercial membranes, silane derivatives coated membranes showed significantly enhanced chlorine durability.

• 멤브레인
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• 제10권4호
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• pp.220-229
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• 2000

본 연구는 한외여과 중공사형 모듈과 역삼투 나권형 모듈로 구성된 모듈 set 1∼7을 이용하여 모듈 set에 따른 순수 및 2차 처리수의 투과 flux를 고찰하고, 적용압력과 온도변화에 의한 한외여과 막과 역삼투 막의 분리 특성을 고찰하였다. 탁도와 SS는 한외여과 막에서 효율적으로 제거되며 COD, T-N, TDS 등은 역삼투 막에서 우수한 제거효율을 나타내었다. 적용압력과 온도의 증가에 따른 투과 flux는 선형적으로 증가하는 경향을 보였다. 이로부터 한외여과 및 역삼투 막은 정유공장 방류수의 고도처리 및 재활용을 위해 적합한 것으로 나타났다.

• 한국막학회:학술대회논문집
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• 한국막학회 1995년도 제3회 하계분리막 Workshop (환경과 막분리 공정의 역할)
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• pp.39-50
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• 1995

The membrane processes that are commonly uscd in water and wastewater treatment are reverse osmosis (Ro), ultrafiltration (UF) and microfiltration (MF), which utilize pressure differentials. There is also nano-filtration (NF), or low-pressure reverse osmosis, which is positioned midway between conventional reverse osmosis and ultrafiltration. Reverse osmosis membranes reject dissolved ions, while ultrafiltration can be used to reject relatively larger molecules, such as protein, polysacchalides and so on. Microfiltration is capable of eliminating particles at submicron level. This paper summarizes the characteristics of MSAS process first, as it is the main membrane process applied to wastewater treatment. Two successful examples of the applications, the cases of individual building reuse system and nightsoil treatment, are then shown. The latest trend of new membrane applications, i.e., immersed-type MSAS is also introduced.

• 상하수도학회지
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• 제25권2호
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• pp.171-176
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• 2011

Organic matters that comprise a tiny part of seawater generally occur over 50% of membrane fouling in Reverse Osmosis Process. This study evaluates Foundation efficiency of reverse osmosis membranes under brackish and seawater conditions and resistance of organic fouling. Moreover, analyzing the membrane surface through roughness, contact angle and zeta potential results in roughness and contact angle are proportional to flux decline rate (FDR), yet FDR has high value when zeta potential is low level. Furthermore, with various membrane fouling of different raw water conditions, the flux tends to improve when pH value is high and raw water which is complex with organic and cation pollutes membrane faster than organic separated raw water condition.