• Membrane Journal
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• v.2 no.1
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• pp.1-20
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• 1992

Classical membrane processes like microfiltration (MF), ultrafiltration (UF) and reverse osmosis (RO) are being applied in the last years more frequently in environmental and effluent process problems. Newer technologies and developments like pervaporation (PV) and gas sepaxation (GS) recently found commercial applications in the treatment of waste waters and gas streams. The incentive here is either the clean-up from organic components to comply with federal emission regulations or the recovery of the organics for economical reasons. Processes still in their development stage are combinations of chemical reactions with membrane processes to separate and treat $SO_x$ and $NO_x$ laden waste gas streams in the clean-up of stack-gases. In this paper we will first give a short overview of the more recent developments in MF, UF and RO. This is followed by a closer look on newer technologies applied in environmental problems. The applications looked at are the recovery of organic components from solvent laden gas streams and the separation of organic volatiles from aqueous waste waters via pervaporation. Technical solutions, the advantages and disadvantages of the processes and. where possible, cost estimations will be presented.

• Proceedings of the Membrane Society of Korea Conference
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• 2003.07a
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• pp.95-97
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• 2003

The main purpose of this work is to investigate the performance of membranes for treatment of dyeing wastewater. The microfiltration (MF) membranes (titania-blended polysulfone & alumina) were prepared. The nanofiltration (NF) and reverse osmosis (RO) membranes were kindly supplied by the Sae-Han. In order to reuse the wastewater for dyeing, the effluents were treated by the high flux RO and the fouling resistant RO (FRM) membranes. Also, the NF membrane was used for water reuse in rinsing.

• Proceedings of the Membrane Society of Korea Conference
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• 1994.06a
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• pp.33-43
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• 1994

It is the purpose of this paper to review the recent developments and future trends in various membrane processes, which will result in energy savings. Historically, there was a long period of academic curiosity in membrane research covering from gas separation to reverse osmosis. With advent of asymmetric membrane technology, many membrane processes proved to be energy efficient than the conventional separation methods. Thus, membrane technology has gained wide acceptance from many sectors of industry. The commercial sale of membranes is still modest compared to the major technologies, but it is one of the fastest growing industries. Recently the U.S.Department of Energy conducted a study (1) to evaluate and prioritize research needs in the membrane separation industry in order to foster and better support the deveolpment of energy-efficient new technologies. The National Science Foundation (U.S.A.) did also do a similar investigation. Both agencies have arrived neary at the same conclusion, that is, membrane separations can offer many new and alternative methods of separations that are more energy efficient than existing processes. This paper is largely based on these findings.

• Proceedings of the Membrane Society of Korea Conference
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• 1998.10a
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• pp.156-158
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• 1998

원자력 발전소에서 사용하는 1차 냉각수에 대해 살펴보면, 일차냉각수의 pH는 5~8 범위이며, 수질기준은 염소이온과 불소이온이 0.15 ppm, 현탁고형물 이 0.2 ppm이나 실제 농도는 기준치보다 훨씬 낮은 매우 순수한 상태로 유지된다. 다만, 핵분열 반응도를 제어하기 위해 주입되는 붕소가 수백 ppm정도, pH를 조절하기 위해 부가되는 리튬의 1 ppm정도 포함되며, 그밖에 1ppm 정도의 실리카가 포함될 수 있다. 붕산으로 포화 운전되는 이온교환 수지탑 내에서는 붕산보다 이온선택도가 낮은 실리카는 이온교환수지에 흡착되지 않기 때문에 발전소의 가동년수의 증가에 ㄷ아라 원자로 냉각제의 실리카 농도는 점차 증가하게 되었다.

• Membrane Journal
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• v.12 no.1
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• pp.1-7
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• 2002

Currently, the commercialized cation exchange membranes have the excellent performance and stability, however their costs are very expensive and they are not still optimized for the several application areas. A number of membranenologists are focused to solve the problems on the development of novel membrane to be applicable to each membrane field. The present will deal with the introduction of the existing membrane materials and their performances.

• Proceedings of the Membrane Society of Korea Conference
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• 1998.10a
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• pp.143-145
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• 1998

식품공업 분야에서 특정 성분의 분리, 정제, 농축은 매우 중요한 단위공정으로써 추출(Extraction), 여과(Filtration), 증류(Distillation), 증발(Evaporation)등의 조작을 통하여 실시되고 있다. 최근 들어 화학공업, 기계공업, 식품공업의 지속적인 발전에 힘입어 단위조작을 효율적으로 실시할 수 있는 기술로써 국내의 산업화되고 있는 것이 분리막 기술이다. 현재 식품공업 분야에서 활용되고 있는 분리막공정의 종류는 정밀여과(Microfiltration), 한외여과(Ultrafiltration), 초정밀여과(Nanofiltration), 역삼투(Reverse Osmosis) 시스템으로 유제품, 조미료, 음료공업, 장유산업, 기능성 인자의 분리 등에 공업적으로 점차 그 도입 가능성이 증가하고 있다.

• Membrane and Water Treatment
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• v.10 no.5
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• pp.381-385
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• 2019

Surface modification is very efficient and scalable approach to achieve improved membrane performance. We treated Reverse Osmosis Thin Film Composite (TFC RO) membrane with various concentrations of Polyethylene Glycol (PEG), a hydrophilic polymer after activation with sodium hypochlorite. This treatment resulted in an increment of the water flux by 43% and the salt rejection by 2.36% for the 3000 mg/l PEG-treated membrane. Further, these PEG-treated membranes were exposed to a mixture of 3000 mg/l PEG and 1000 mg/l sodium hypochlorite for 1 hour. Further modification of this membrane by PEG and sodium hypochlorite mixture increased the water permeance up to 133% when compared with the virgin TFC RO membrane. We characterized the treated membranes to understand the changes in wettability by contact angle analysis, changes in surface morphology and roughness by scanning electron microscope (SEM) and atomic force microscope (AFM) analysis.

• Proceedings of the Membrane Society of Korea Conference
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• 1997.06a
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• pp.143-158
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• 1997

Electrochemical deionization (EDI) offers continuous demineralization at higher water recovery rates (>90%), compared with mixed bed ion exchange, and without the use of chemical regenerants and the associated production of saline waste water. Although EDI technology has been used in some power generation applications, its wider application requires the satisfactory resolution of outstanding capital cost and performance issues. This paper reports on the field evaluation of a new cost-effective EDI technology in a power generation application. The E-Cell System$^{TM}$, which became commercially available in the fourth quarter of 1996, consists of a rugged, modular system, based on a new high-performance EDI stack. Starting in May 1996, a 100 gpm modular EDI pilot system, rated for operation at 100 psi, was evaluated at the TVA Brown's Ferry Nuclear Plant. The feed consisted of Reverse Osmosis (RO) permeate with a conductivity of 4-7 $\mu$S/cm. The pilot system reliably produced 17.8-18.0 M$\Omega$.cm water under design operating conditions, independent. Silica levels were reduced from ca. 50 ppb to 4 ppb, while TOC levels were reduced from ca. 120 ppb to 30 ppb.

• Proceedings of the Membrane Society of Korea Conference
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• 1996.09a
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• pp.39-64
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• 1996

Probably over most of recorded time, the quality of drinking water has been praised for good health and blamed for bad health. Certainly it is true, considering pathogenic organism that cause typhoid fever, giardiasis, etc., or considering chemical contaminants suspected of causing cancer. Drinking "natural" waters with a high mineral content is generally accepted to be healthy. Water containing very low levels of total dissolved solids (TDS), such as distilled water, is believed by some to help "cure" arthritis by "washing out" calcium from deposits in joints. Along with this reasoning, many believe that drinking very tow TDS water, treated by distillation, reverse osmosis (RO) or deionization (DD, "leaches" minerals from the body and causes mineral deficiencies with subsequent ill health effects.cies with subsequent ill health effects.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.39 no.6
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• pp.513-518
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• 2015

Salinity gradient power (SGP) has attracted significant attention because of its high potential. In this study, we evaluate reverse electrodialysis (RED) with various compositions of available resources. The polarization curve (I-V characteristics) shows linear behavior, and therefore the power density curve has a parabolic shape. We measure the power density with varying compartment thicknesses and inlet flow rates. The gross power density increases with decreasing compartment thickness and increasing flow rate. The net power density, which is the gross power density minus the pumping power, has a maximum value at a compartment thickness of 0.2 mm and an inlet flow rate of 22.5 mL/min. The power density in RED is also evaluated with compositions of desalination brines, seawater, river water, wastewater, and brackish water. A maximum power density of $1.75W/m^2$ is obtained when brine discharged from forward osmosis (FO) and river water are used as the concentrated and the diluted solutions, respectively.