• Proceedings of the Membrane Society of Korea Conference
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• 2000.04a
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• pp.27-29
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• 2000

• Membrane Journal
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• v.18 no.2
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• pp.168-175
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• 2008

This study was carried out for the plate and frame membrane modules equipped with and without plastic protuberances on the support frame in order to determine the effect of eddy flow induced by the protuberances on permeate flux. The initial time for rapidly declined permeate flux on the module with protuberances was delayed twice or more than that on the module without protuberances when kaolin solution was permeated at the operating pressures from 0.4 to 1.6 bar. Also decreasing ratio of the kaolin solution to pure water flux for module with protuberances was 1 to 5% lower than that for module without protuberances. The flux improvement due to protuberances at laminar flow corresponding Reynolds number 1,750 was about double as compared with that in the transition flow region. In general, the kaolin fouling reduction for the plate module with protuberances during initial filtration process was very effective, even though the permeate flux after 60 minutes filtration did not increase significantly.

• Membrane Journal
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• v.11 no.4
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• pp.152-160
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• 2001

The pretreatment for COD removal of acrylic wastewater and separation characteristics of ultrafiltration hollow fiber type module and reverse osmosis spiral wound type module with the variation of applied pressure and temperature were discussed. Thc optimum washing time of membranes was decided with long team operation and the degree of fouling was discussed with operating time. Permeate flux was decreased rapidly at 14 hrs and that of reverse osmosis membrane was indicated similarly. CaO find sand filter for the first step, neutralization process with treated acrylic wastewater as the second step, UF/RO processes were used as final strep. It was shown treat COD and TDS were below allowable discharge value with the result.

• Membrane Journal
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• v.25 no.3
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• pp.268-275
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• 2015

Effects of aeration intensity on local fouling were investigated in submerged membrane modules. Higher liquid velocities were observed at the section with the lower fiber packing density. The liquid velocity is increased with increasing the gas-liquid injection factor. The high shear stress coincided with the high liquid velocity. The shear stress increases with the increasing of gas-liquid injection factor and the liquid velocity improves with the increasing of gas-liquid injection factor. Irreversible fouling resistance ($R_{ir}$) of the fiber position is significant in a local region of high suction pressure near the suction point of the fiber (position 1). The ratio of $R_{ir}/R_m$ and $R_{ir}/R_r$ of position 1 was highest compared to the position 2 and 3. Irreversible fouling resistances results confirmed the preferential deposition of foulants near the suction part of the fiber where the local suction pressure is the highest and correspondingly, more particles are accumulated to the membrane surface. The effects of local fouling along the fiber length are significant factors to optimize the design of submerged modules.

• Proceedings of the Membrane Society of Korea Conference
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• 1997.10a
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• pp.111-113
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• 1997

1. 서론 : "Engaged type"의 2축 RDM은 housing의 부피에 대한 막면적을 극대화시키고 회전방향을 엇갈리게 함으로서 유체의 겉보기속도를 증가시키고 막표면에서 난류와 2차흐름을(secondary flow)를 형성시켜 농도분극층이 감소하여 막오염을 최소화할 수 있다. 본 연구에서는 2축 RDM으로 실제 열간 압연유 폐수를 적용하여 농축실험을 하였으며 투과 특성과 농축수의 열간 압연유 입자 분포의 변화를 조사하였다.변화를 조사하였다.

• Proceedings of the Membrane Society of Korea Conference
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• 1997.10a
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• pp.118-119
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• 1997

1. 서론 : 현대는 인구증가로 인한 생활하수 산업발달에 따른 폐수의 증가 및 오염물질의 다양화로 인하여 상수원이 점점 오염되어 가소 있는 반면, 국민소득 증가와 생활수준의 향상에 따라 맑고 깨끗한 물을 선호하는 계층의 욕구가 증대하고 몇 차례의 수질오염 사고로 인하여 수돗물에 대한 불신이 고조되고 있다. 이런 시점에서 환경부가 먹는 물의 수질을 검사한 결과, 몇몇 항목에서 기준을 초과하였다. 본 실험에서는 전국 먹는 물 수질을 분석하여 환경기준을 초과하는 주 항목을 선택한 뒤, 시판되는 몇몇 Module을 이용하여 과연 환경기준에 적합한 수질을 만들어 낼 수 있는가를 검토함으로써 각 지역별로 막 선택을 차별화하였다.

• Proceedings of the Membrane Society of Korea Conference
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• 1994.04a
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• pp.49-50
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• 1994

상호 불용성인 용매에 녹아있는 반응물들 간의 반응은 각 물질이 상 경계면을 뛰어 넘기가 어려워 매우 느린 속도로 진행된다. 그러나 상호 불용성인 비균질계에 상이동 촉매라는 제 3의 물질을 첨가하면 반응은 급격히 향상된다[1, 2]. 따라서 본 연구에서는 클로로벤젠 상의 브로모 옥탄이 TBABr(Tetra Butyl Ammonium Bromide) 이온 촉매의 존재 하에 수용액상의 요오드 이온과 반응하는 평판형 막반응기를 대상으로 수치모사를 수행하여 그 결과를 Stanley와 Quinn[3]의 실험값 및 수치모사치와 비교하였으며, 막 반응기의 모듈 선택, 설계 및 운영, scale-up시 고려되어야 할 사항들을 탐색연구하여 보았다.

• Proceedings of the Membrane Society of Korea Conference
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• 1995.10a
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• pp.51-51
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• 1995

혐기성 미생물의 특징은 성장 속도가 느리고 침강성이 좋지 않다는 점이다. 이 문제의 한 해결책인 막결합형 혐기성 소화는 고액분리를 완전하게 수행함으로써 미생물의 유출을 방지하여 반응조 내부에 미생물을 고농도로 유지할 수 있을 뿐만 아니라 에너지의 회수와 설비 면적의 축소 등 많은 장점이 있다. 이 막결합형 혐기성 소화의 경제성은 사용된 분리막의 투과 속도에 의해 크게 좌우된다. 분리막의 투과 속도에 영향을 미치는 인자로는 미생물 및 유입수를 비롯한 반응조 내부의 상태, 막모듈 압력 온도 막면유속 등의 운전 조건이 있다. 또한 사용되는 분리막 자체의 재질도 투과 유속에 큰 영향을 미친다. 본 연구의 목적은 관형의 지르코니아 스킨층과 탄소 소재 지지층으로 이루어진 복합 재료 분리막과 폴리프로필렌 분리막을 이용하여 막재질에 따른 막오염 특성을 비교 분석하고 효과적인 투과율 회복 방법을 확립하는 것이다.

• Membrane Journal
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• v.15 no.4
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• pp.310-319
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• 2005

This paper describes the preliminary study on the development of multi-stage membrane demonstration plant for removal of carbon dioxide from flue gas stream being emitted from LNG boiler in thermal power generation plant. The prerequisite requirement is to design and develop the membrane process producing a $99\%\;CO_2$ with $90\%$ recovery from LNG flue gas of 1,000 $Nm^3$/day. Asymmetric polyethersulfone hollow fiber membranes and membrane modules developed in this laboratory[1] were used in this study. Using the permeation data for the hollow fiber membranes, modelling on the membrane module and multi-stage membrane process was done to meet the requirement condition of the process design. The effects of the operating pressure of feed and permeate side and feed concentration on $CO_2$ purity and recovery were investigated experimentally with the developed hollow fiber modules. These experimental results matched well with theoretical modelling results.

• Membrane Journal
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• v.25 no.4
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• pp.352-357
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• 2015

To determine the pervaporation separation characteristics of 1-butanol/water mixtures, PEI/PDMS hollow fiber membrane module commercialized by Airrane Co. was subjected to both lab and pilot tests. The 1% 1-butanol of 1-butanol/water feed mixture was used. The flux of $133g/m^2hr$ and separation factor of 23.4 at $30^{\circ}C$ were obtained whereas the $505g/m^2hr$ and 5.1 were measured at $50^{\circ}C$. When compared with the performance of the hollow fiber PDMS membrane by Nagasep Co., the higher flux of $10{\sim}20g/m^2hr$ was obtained by the module of Airrane Co. In order to realized the durability of Airrane Co. module, the long-term test of 35 days has been conducted and as a result, the flux $510{\sim}520g/m^2hr$ and separation factor 20~25 were maintained with the initial values.