• 멤브레인
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• 제21권1호
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• pp.13-21
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• 2011

본 연구는 폴리에틸렌 정밀여과 막을 이용한 $Al_2O_3$ 콜로이드 현탁액의 운전압력 순환변화에 따른 투과거동을 검토하였다. 운전압력의 순환은 0.49에서 1.96 bar까지 증가시키는 증압운전 후 다시 0.49 bar로 감소시키는 감압운전으로 행하였다. 연속적으로 운전압력을 순환변화 시킨 결과, 증압운전과 감압운전의 투과유속이 서로 다른 이력(hysteresis)을 나타냈다. 현탁액의 투과저항은 감압운전의 경우가 증압운전의 경우보다 컸으며, 투과저항 증가율도 컸다. 막오염 형태는 증압운전과 감압운전 모두 운전초기에 케익오염이 강하게 나타났으며, 막오염의 크기는 감압운전의 오염이 증압운전의 오염보다 컸다.

• 한국막학회:학술대회논문집
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• 한국막학회 2003년도 춘계 총회 및 학술발표회
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• pp.75-78
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• 2003

• 한국막학회:학술대회논문집
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• 한국막학회 2001년도 추계 총회 및 학술발표회(한국막학회)
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• pp.146-148
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• 2001

• 한국막학회:학술대회논문집
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• 한국막학회 2003년도 추계 총회 및 학술발표회
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• pp.142-142
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• 2003

• 한국막학회:학술대회논문집
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• 한국막학회 1999년도 춘계 총회 및 학술발표회
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• pp.91-93
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• 1999

• 상하수도학회지
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• 제10권3호
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• pp.92-99
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• 1996

The effects of membrane fouling on the water permeability were examined using the hollow fiber microfiltration (HMF)membrane. A membrane module with a pore size of 0.1 micron was submerged in the permeation tank and water bath. The applied pressure was 12.4 kPa for direct solid-liquid separation of activated sludge. As the concentration of MLSS(880~2180mg/l) of the feed solution increased, the decreasing rates of the water flux increased and the membrane was clogged more rapidly. The water flux through the membrane did not increase effectively even with the increase in the applied pressure(40.0~93.3kPa). When the membrane was cleaned with water, the recovery rate of water flux were larger for lower applied pressure. The results indicated that the process of direct solid-liquid separation using HMF membrane was effective at lower pressure.

• 멤브레인
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• 제15권2호
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• pp.85-104
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• 2005

Recently, membrane can be prepared by two methods, phase inversion and electrospinning techniques. Phase inversion technique is a conventional but commercially preparation membrane. The most versatile of preparation in this technique is immersion of the cast film into nonsolvent bath, causing dense top layer with a finger-like pattern in the sub layer membrane. The membrane pore size getting from phase inversion is in the range of micro or submicrometer. As a result, it can be used as microfiltration and ultrafiltration applications. A new technique, electrospinning, is introduced for membrane preparation. Nonwoven nanofibrous mat or nanofibrous membrane is obtained. In this technique, electrostatic charge is introduced to the solution jet, causing a thin fiber with high surface area; hence it can be used in the applications where high surface area-to-volume or length-to-diameter ratios are required. Moreover, the pore size can be controlled by controlling the time of electrospinning. Hence, it can be used as a filter for filtering microparticles as well as nanoparticles.

• 상하수도학회지
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• 제20권4호
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• pp.535-543
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• 2006

The Ozone oxidation process was applied to increase the efficiency of reuse process when treating the secondary effluent by the membrane system. This paper focus on decreasing efficiency of membrane fouling, because of membrane fouling reduction by ozone and evaluation of application of the ozone oxidation. The feed water was secondary effluent from BNR process. The result shows that the ozone pretreatment can reduce membrane fouling effectively. Also, the improvement of treated water quality was obvious. The reduction of the membrane fouling led decrease of following pollutant and increase of lnner adsorptive ability of hydrophilic organic matter and decrease of molecular weight. MF membrane process alone can meet the domestic reuse water standards. And ozone pretreatment process also can increase the removal rates of turbidity, COD, nitrogen, and color.

• 환경위생공학
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• 제23권4호
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• pp.13-21
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• 2008

With the rise in membrane applications, residuals management has become a growing challenge for membrane system. The primary residuals of MF/UF (microfiltration/ultrafiltration) system results from the wastes generated during backwashing. Many regulatory agencies, utilities, and water process engineers are unfamiliar with the characteristics and methods for treatment and disposal of membrane residuals. Therefore, this study was performed to investigate the backwash residuals water quality from the pressurized system with and without pre-coagulation, and to suggest approaches for the backwash residuals treatment. Pressurized MF system was installed at Guui water intake pumping station and operated with raw water taken from the Han River. We compared performances with and without the recycling backwash residuals at flux conditions, 50 LMH and 90 LMH with and without pre-treatment (coagulation). Based on the results, recycling of backwash residuals in pressurized system with pre-coagulation showed applicability of backwash residuals managements. Moreover, the recovery rate also increased up to over 99%.

• 멤브레인
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• 제23권3호
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• pp.211-219
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• 2013

탄소 한외여과 및 광촉매 코팅 폴리프로필렌(PP) 구의 혼성수처리 공정에서 물 역세척 주기(FT)의 영향을 알아보고, 탄소 정밀여과막 또는 알루미나 한외여과막 및 정밀여과막을 사용한 기존 결과들과 비교하여 분리막의 영향을 고찰하였다. FT 6분일 때 초기 60분까지 최소 막오염 저항을 보이고 최대 총여과부피를 얻어서, FT 6분이 초기 막오염의 억제에 가장 효과적이고 최적 조건이다. 탁도의 처리효율은 98.6% 이상이며 FT 변화의 영향이 보이지 않았는데, 탄소 또는 알루미나 정밀여과막을 사용한 기존 연구와 일치하는 것이다. 유기물의 처리효율은 FT 6분에서 98.2%로 최대값을 보였는데, 알루미나 정밀여과막의 결과와 유사하다. 반면에 탄소 정밀여과막에서는 유기물의 처리효율이 비역세척(NBF)에서 최소이고 FT가 감소할수록 증가하였으나, 알루미나 한외여과막에서는 NBF에서 최대이고 FT가 감소할수록 역시 증가하였다. 따라서 유기물 처리효율에 대한 물 역세척 주기의 영향은 동일한 재질의 분리막이라도 기공 크기에 따라 다른 기작을 보인다는 것을 알 수 있었다.