• Journal of Plant Biotechnology
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• 제31권3호
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• pp.209-217
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• 2004

기내 배양환경을 조절하여 건전한 유식물체를 획득하기 위해 도라지를 무균발아시켜 shoot부분을 NAA 0.1 mg/L가 첨가된 MS 기본배지에 치상한 후 membrane filter 부착 유무와 sucrose 농도를 달리 처리하여 생장반응을 조사하였다. Membrane filter 미부착구에서는 배양용기 내의 $CO_2$와 $C_2$H$_4$ 농도가 membrane filter 부착구에 비해 높았으며 membrane filter가 부착되지 않았을 때 $CO_2$ 농도는 배양기간이 경과될수록 증가하였으나 $C_2$H$_4$ 농도는 감소하는 경향이었다. 식물체 생장은 membrane filter 부착구가 미부착구에 비해 양호하였고, 미부착구에서는 sucrose 농도가 증가할수록 생육이 양호하게 나타났다. 생체중과 건물중은 membrane filter를 부착하지 않은 sucrose 4.5% 처리구에 비해 membrane filter를 부착한 sucrose 무첨가구에서 비슷하거나 높았다. 엽록소 함량은 membrane filter 부착구에서 미부착구에 비해 높았으며 당 함량도 비슷한 경향이었는데 두 처리간 차이는 더 컸다. 기공은 membrane filter 부착구에서 미부착구에 비해 닫혀 있었으며 엽육조직은 membrane filter를 부착하거나 sucrose 농도가 높을수록 잘 발달하였다. 또한 상토에 이식한 후 13일째 생존율은 sucrose 처리 농도에 관계없이 membrane filter 미부착구는 0%인데 비해 부착구는 100%로 나타났다.

• Journal of Advanced Marine Engineering and Technology
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• 제37권5호
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• pp.541-547
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• 2013

물 부족 국가인 우리나라는 정수를 위한 설비시설을 확보하는 것이 무엇보다 중요하다. 그럼에도 불구하고 잦은 수질오염사고와 최근의 구제역으로 인한 가축 매몰지의 침출수 문제 등은 엄격한 수질관리의 필요성을 다시 한 번 깨닫는 계기가 되었다. 현재 가정용 정수기는 4단계 또는 5단계 정수처리 시스템을 적용하고 있으며 각 단계는 Sediment filter, Pre-carbon filter, UF/RO membrane filter, Post-carbon filter로 구성되어 있고 5단계는 Ceramics filter를 마지막 단계에 추가하여 구성하고 있다. 본 연구는 국내 가정용 정수기 필터의 물리적 특성을 파악하는 것이며 6개 사의 시제품을 통하여 분석하였다. 필터의 표면과 형상의 관찰은 SEM 분석을 통하여 이루어졌으며 Sediment filter, UF membrane filter, RO membrane filter의 기공의 크기는 30~47 ${\mu}m$, 0.005~0.5 ${\mu}m$, 0.025~0.25 ${\mu}m$의 분포를 보였고 활성탄의 비표면적은 622 ~ 1,308 $m^2/g$의 분포를 보였다.

• 한국산업보건학회지
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• 제3권1호
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• pp.37-53
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• 1993

The polynuclear hydrocarbons (PAHs) emitted from coke oven standpipe were sampled using three sampling systems, including glass fiber filter+silver membrane filter, glass fiber filter+silver membrane filter+XAD-2 adsorbent tube, PTFE membrane filter+XAD-2 adsorbent tube, extracted by methylene chloride and analysed by gas chromathography using flame ionization detector. The results of this study were as follows. 1. Because the amounts of coke oven emissions(COE) were large, the analyses of PAHs were simple and possible without evaporation and concentration. Although the generation of COE was high during early stage of coking, the airborne concentration of PAHs was low and increased during late coking. 2. The contents of PAHs in COE were 1.35-2.81%. 3. The index components of PAHs were fluoranthene and pyrene. Their correlation coefficient to total PAHs were 0.96, 0.95, respectively. 4. The particulate PAHs were sampled by filter and gaseous PAHs by adsorbent tube. The collection efficiency of glass fiber filter+silver membrane filter was 20% of total amount sampled by filters+adsorbent and PTFE membrane filter 50%. Adsorbent tube must be attached to the filter to collect light and small PAH components. 5. The generation of acenaphthene and indeno (1,2,3-cd) pyrene were low and concentrations of fluorene and anthracene were $20-40ug/m^3$ throughout coking time. Other PAH eoncentrations were sometimes high. The generation of PAHs was low at 4-6 hours of coking time. The gaseous PAHs were generated earlier than particulate PAHs.

• Archives of Pharmacal Research
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• 제20권1호
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• pp.68-71
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• 1997

Penicillin sensor was prepared by immobilizing penicillinase (Pcase) on $H^{+}$-selective carboxylated poly (vinyl chloride) (PVC-COOH) membrane or cellulose filter membrane. The immobilization techniques are as follows. Pcase was immobilized with GTH on $H^{+}$-selective PVC-COOH membrane or some amount of BSA was dropped on that membrane. Another method to make immobilization is to mix type I Pcase with GTH and drop on a cellulose filter membrane. According to immobilization techniques, there were some differences in response properties of enzyme electrodes, however, all electrodes responded to Pcase-resistant penicillin derivatives. Pcase immobilized on cellulose filter membrane with $H^{+}$-selective PVC membrane eletrode was more stable and more sensitive to penicillinase-resistant penicillin derivatives than any other immobilization techniques.

• 한국물환경학회지
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• 제25권2호
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• pp.205-211
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• 2009

In this study, the membrane filter method was compared to the MPN method for the analysis of total coliforms from raw water using raw test waters and controls including 6 standard strains of coliforms, and the various factors were analyzed on the detection of general and fecal origin coliforms. The range of error rate for the detection of 5 standard strains using the membrane filter and the MPN methods was 0 to 6% and 45 to 133%, respectively. The error rate of the membrane filter method was lower than that of the MPN method. The membrane filter method (m-Endo) showed 10% (11 out of 111) of difference for the detection sensitivity of coliforms isolated from raw water compared to the MPN method (BGLB). The membrane filter method was less affected by the factors including temperature, turbidity, charcoals of powder form, contamination, and reverse pressure. In conclusion, the membrane filter method is a better method for the analysis of total coliforms from raw water than the MPN method, considering the accuracy of detection and the tolerance to various experimental factors.

• 한국막학회:학술대회논문집
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• 한국막학회 1993년도 제1회 하계분리막 Workshop
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• pp.83-95
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• 1993

현재 존재하는 다양한 filtration 테크놀러지는 feed stream으로부터 제거되는 파티클의 사이즈에 근거하여 그 범주를 정할 수 있다. 부유 고체물의 재래식 macrofiltration 은 feed solution이 수직 방향으로 filter media을 통하여 흐르게끔 하는 것이다. 전체 용액은 메디아를 통하여 지나가는데 단지 한개의 stream만 만든다. 그런 여과 장채의 보기를 들면, cartridge, filter, bag filter, sand filter, multimedia filter들이 있다. Macrofiltration separation은 1 미크론 이상가는 비용해성 파티클에 국한된다.

• 대한기계학회논문집A
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• 제32권8호
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• pp.617-623
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• 2008

The membrane filter adhered with nanostructured porous layer was made by heat treatment after deposition of nanoparticle-agglomerates sintered in aerosol phase onto a conventional micron-fibrous metal filter as a substrate filter. The Sintered-Nanoparticle-Agglomerates-coated NanoStructured porous layer Membrane Filter (SNA-NSMF), whose the filtration performance was improved compared with the conventional metal membrane filters, was developed by adhesion of nanoparticle-agglomerates of dendrite structure sintered onto the micron-fibrous metal filter. The size of nanoparticle-agglomerates of dendrite structure decreased with increasing the sintering temperature because nanoparticle-agglomerates shrank. When shrinking nanoparticle-agglomerates were deposited and treated with heat onto the conventional micron-fibrous metal filter, pore size of nanostructured porous layer decreased. Therefore, pressure drops of SNA-NSMFs increased from 0.3 to 0.516 kPa and filtration efficiencies remarkably increased from 95.612 to 99.9993%.

• Korean Chemical Engineering Research
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• 제45권6호
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• pp.591-595
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• 2007

기존 마이크론 금속섬유 필터를 지지체로 그 표면 위에 나노입자 증착 후, 열처리를 하여 나노구조 기공층이 표면에 부착 형성된 멤브레인 필터를 제작하였다. 가지상 구조의 나노입자 응집체를 마이크론 금속섬유 필터상에 부착함으로써 기존 금속 멤브레인 필터에 비하여 여과성능이 향상된 나노구조 기공층 멤브레인 필터를 개발하였다. 증착한 나노구조 기공층을 지지체 필터 표면상에 부착시키기 위한 열처리 온도가 증가함에 따라 나노입자 응집체의 수축 현상으로 인하여 나노구조 기공층 멤브레인 필터의 차압은 감소하였지만, 여과효율의 감소는 미미하였다.

• 환경위생공학
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• 제23권2호
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• pp.55-63
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• 2008

All over the world, the existing process of water purification needs more flocculants and chlorine due to a gradual decline in the quality of source water. Therefore, the problem of the remaining aluminium and DBPs in purified water is on the rise. To solve this problem, the process of membrane filter has recently come into the spotight. This study reaches the following conclusions concerning TMP variation in order to solve the dropping of flux throgh a membrane filter when operating a membrane filter system in the process of water purification. 1. In case that a cohesion-precipitation process was introduced to pre-treatment of a membrane filter, initial TMP was very satisfactory(0.27kg/cm) in producing the constantly safe quality of water, $0.04{\sim}0.1$(mean 0.05) NTU by pouring 2mg/l of PACI(10% $Al_2O_3$) used for the existing process of water purification in high-density turbidity at a dry or flood season and at occurrence of high algae. 2. As flux increased at 0.5m/day.m, TMP increased 0.05 kgf/cm. 3. As filtering, operation mode of PVDF MF membrane filtering was 48 minutes and 1 cycle of back washing was 42 minutes, flux was increased 1.5m/day.m and TMP increased $0.25{\sim}0.27kgf/cm$. Without back washing, TMP increased 0.03 kgf/cm per a cycle.

• 상하수도학회지
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• 제19권2호
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• pp.144-148
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• 2005

The industrial development of large scale deep bed filters has been a very important step in the process of drinking water production and more recently in the tertiary treatment of wastewater. The target of deep bed filtration is the retention is the retention of small particles generally smaller than 30 microns at relatively small concentration, generally less than 30 mg/l from natural water (surface water or aquifers) or secondary treated wastewater. The relation between the retention efficiency and the characteristics of the particles has been extensively studied experimentally and through different models of retention. During the last years the development of new technologies (fiber filter, membrane modules) lead to more intensive processes compared to conventional sand filtration. Fiber filters can combine intensification with a decrease in specific energy needed however they cannot be operated under gravity like sand filters. Membrane filters (UF or MF) are much more intensive and efficient than sand filters. The specific energy needed is not so high (about $0.1Kwh/M^3$) but is higher than sand or fiber filter. A Life Cycle Analysis (LCA) has to be made for a complete comparison between these technologies taking in account that the efficiency of particle retention obtained by membrane filters is unique.