• KSBB Journal
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• 제4권2호
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• pp.177-184
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• 1989

항생물질 발효액의 균사체 분리에 있어서 Modified regenerated cellulose 막을 이용한 Cross-flow filtration으로 높은 Flux를 얻을 수 있었다. 막분리시 가급적 높은 유속, 높은 온도, 특정 균사체농도(약 20% PMV)에서 높은 Flux를 보여주었으며 Fouling 정도는 균사체 농도가 높을수록 또한 유속이 낮을수록 심각한 것으로 나타났다. 발효액을 농축 분리할 때의 Flux profile은 1단계 Sublayer형성에 의한 급속감소, 2단계 평형, 3단계 Fouling에 의한 급속감소의 세 구간으로 나눌 수 있었으며 Diafiltration의 적용으로 3단계의 Flux 감소 현상을 현저히 완화시킬 수 있었다. 한편 Diafiltration에 의한 항생물질 회수시 초기부터Diafiltration하는 것보다는 특정 PMV까지 농축시킨 후 Diafiltration하는 경우에 작업시간과 여액의 Volume을 최소화 할 수 있었으며 본 실험에서는 98%의 회수율을 얻기 위해서 Di-afiltration을 시작하는 Optimum PMV는 20%였다.

• 한국식품과학회지
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• 제24권3호
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• pp.199-203
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• 1992

한외여과를 이용하여 다시마 열수추출물로 부터 가용성 저분자량의 정미성분을 회수하는데 필요한 조건을 최적화하기 위해, 분리막 선정 및 온도, 압력, Flow rate의 영향을 고찰하였고 선정된 최적 조건하에서 한외여과와 Diafiltration을 실시하여 투과유량의 flux profile과 정미성분의 회수율을 비교하였다. 분리막은 소수성인 GR 51PP가 친수성인 FS 형태보다 높은 투과유량을 유지하였다. Flow rate의 증가에 따라서 투과유량도 증가하는 경향을 보였으나 3.7 l/min에서 한계값을 나타내었다. 한편, 압력이 높은 경우에는 Steady-state에서 투과유량이 감소하는 경향을 보였고 온도 증가에 따라서는 큰 변화는 없었다. 한외여과와 Diafiltration 실시에 따른 투과유량의 Flux profile과 전체 고형분과 정미성분의 회수율을 조사한 결과 한외여과를 실시한 경우가 비교적 높은 회수율을 보였으나 투과유량은 전반적으로 Diafiltration 보다 낮았다.

• 한국막학회:학술대회논문집
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• 한국막학회 1994년도 춘계 총회 및 학술발표회
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• pp.21-22
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• 1994

정밀화학공업에서 고부가 제품을 생산하기 위해 다양한 정제공정을 사용하고 있다. 특히 염료, 안료 제조공정에서 사용되는 다량의 염을 정제공정에서 효과적으로 분리시키는 것은 중요하다. Diafiltration을 이용한 탈염공정에는 주로 UF막이 분자량이 큰 물질의 탈염에 사용되었다. 그러나 NF막의 개발에 따라 분자량이 작은 의약품, 염료등의 정체에 분리막을 이용한 Diafiltration이 적극 사용되고 있다. 본 연구에서는 염료 중간체인 2-formylbenzene sulfonic acid, sodium salt(FBS)의 정체에 NF막의 적용가능성을 상업용 막을 이용하여 조사하였다.

• 멤브레인
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• 제30권6호
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• pp.373-384
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• 2020

바이오의약품 중에서도 항체의약품의 수요가 증가함에 따라 항체를 상업용으로 개발하기 위한 연구가 활발히 진행되고 있다. 항체의약품의 제조공정 중 downstream 공정은 의약품 성능에 직접적으로 영향을 미치기 때문에 중요하게 다뤄지며, 본 총설은 그 중에서도 농축 및 제제화를 목적으로 행해지는 한외여과 및 정용여과 공정에서 사용되는 한외여과막의 주요 제품 및 공정 특성을 살펴보고, 최근 연구 동향에 대해 소개하고자 한다.

• 기술사
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• 제32권2호
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• pp.99-109
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• 1999

The dried sea tangle added for soup prepatation to improved the taste in Korean and Japaness for long time. Attempts were made to develop the best procedures for extraction and removal of alginate by ultrafiltration and diafiltration. The summerized results of this study are as follows: 1) For hot water extraction in temperature range of 60～100$^{\circ}C$ for 4 hours, the higher temperature resulted higher yields in solids and protein. 2) Optimum sea tangle hot water extraction condition were 60～65$^{\circ}C$ for 1 hour which was cheap operating cost and high yield of good taste components. 3) The membrane flux was more higher GR 51 PP. and increase of flow rate permeate flow rate was accordingly increased. but limiting flow volume was 3.7 l/min. 4) It was found that ultration was relatively of higher recovery rate, solid and taste components, and low rejection coefficient rate than diafiltration.

• Korean Membrane Journal
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• 제8권1호
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• pp.58-66
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• 2006

The ${\beta}-glucosidase$ from olive fruit is of particular interest compared to the ones from other sources because it has shown to have high specifity to convert the oleuropein into dialdehydes, which have antibacterial activity and are of high interest for their application in the food and pharmaceutical fields. The enzyme is not yet commercially available and advanced clean and safe technologies for its purification able to maintain the functional stability are foreseen. The purification of this protein from fruit extracts has been already tempted by electrophoresis but either enzyme deactivation or high background with unclear profiles occurred. In this work, fruit extracts obtained from the ripening stage that showed the highest enzyme activity have been processed by diafiltration and ultrafiltration. Asymmetric membranes made of polyamide or polysulphone having 50 and 30 kDa molecular weight cut-off, respectively, were tested for the diafiltration process. Ultrafiltration membranes made of polyethersulfone with 4 kDa molecular weight cut-off were used to concentrate the dia-filtered permeate solutions. The efficiency of the separation processes was evaluated byenzyme activity tests using the hydrolysis of p-D-nitrophenyl-${\beta}$-D-glucopyranoside (pNPGlc) as reaction model. Qualitative and quantitative electrophoresis were applied to analyze the composition of protein solution before and after the membrane separation; in addition dot blot and western blot analyses were applied to verify the presence of ${\beta}-glucosidase$ in the processed fractions. The overall results showed that the ${\beta}-glucosidase$ functional stability was preserved during the membrane operations and the removal of 20 kDa proteins allowed to increase the specific activity of the enzyme of about 52% compared to the one present in the initial fruit extract.

• 공업화학
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• 제3권2호
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• pp.349-359
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• 1992

염료속에 함유된 무기염(NaCl, $Na_2SO_4$)의 선택적 제거를 위해 역확산과 역삼투를 결합한 방법과 nanofiltration(NF)을 각각 이용하였다. 역확산에 의한 염의 제거율은 염의 종류에 따라 1회(one pass)에 1~30%를 나타냈으며 염과 염료의 분리비는 10~500의 매우 큰 값을 갖는 반면 염료의 손실율은 0.3% 이하였다. 염료용액을 순환시킬수록 음이온인 $Cl^-$ 이온의 제거율이 증가하고 양이온인 $Na^+$ 이온의 제거율이 감소하는 도난투석현상이 관찰되었다. 또한 공급용액의 유속이 염의 제거에 미치는 영향을 살펴보았다. 역확산에 의해 염이 제거된 염료를 평판형 역삼투막을 사용하여 농축하였으며 $Cl^-$ 이온의 배제율을 solution-diffusion 모델식에 적용하였다 2회의 Diafiltration(DF)을 수행한 NF에서도 역확산에서와 마찬가지로 도난투석에 의해 $Cl^-$ 이온의 배제율 감소와 음배제율을 관찰하였다. 특히 두번째 DF에서 도난투석의 효과는 더욱 크게 나타났다.

• Archives of Pharmacal Research
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• 제20권4호
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• pp.324-329
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• 1997

AB-type amphiphilic copolymers (abbreviated as LE) composed of poly (L-leucine) (PLL) as the A component and poly (ethylene oxide) (PEO) as the B component were synthesized by the ring-opening polymerization of L-leucine N-carboxy-anhydride initiated by methoxy polyoxyethylene amine $(Me-PEO-NH_2)$ and characterized. Core-shell type nanoparticles were prepared by the diafiltration method. Particle size distribution obtained by dynamic light scattering was dependent on PLL composition and the size for LE-1, LE-2 and LE-3 was $369.6{\pm}267$, $523.4{\pm}410$ and $561.2{\pm}364 nm$, respectively. Shapes of the nanoparticies observed by transmission electron microscope (TEM) were almostly spherical. The critical micelle concentration (CMC) of the nanoparticles determined by a fluorescence probe technique was dependent on the composition of hydrophobic PLL, and the CMC for LE-1, LE-2 and LE-3 was $2.0{\times}10^{-6},1.7{\times}10^{-6}$ and $1.5{\times}10^{-6}(mol/l) $, respectively. Clonazepam release from core-shell type nanoparticles in vitro was dependent on PLL composition and drug loading content.

• 대한의용생체공학회:의공학회지
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• 제14권3호
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• pp.221-226
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• 1993

Modules of hemodiafilter were manufactured by using MC-Hp200 and RC-HP4DOA hoi low fiber membranes of Enka Co. in a unique design. The performances of she hemodiafillers were evaluated by measuring the molecular weight cut-off, ultrafiltration rate, clearance, and pressure drop across the hemodiafiter. As a whole, the performances of the RC-HP400A module were superior to those of the MC-Hp200 module. The modules prepared in thls study showed the satisfactory performances for hemodiafiltration.

• Asian-Australasian Journal of Animal Sciences
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• 제18권3호
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• pp.433-438
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• 2005

This investigation was undertaken in order to elicit the relationship between the extent of ultrafiltration processing of whey and its effect on composition and yield of resultant whey protein concentrate (WPC). Cheddar cheese whey was fractionated through ultrafiltration to an extent of 70, 80, 90, 95, 97.5% and 97.5% volume reduction followed by I stage and II stage diafiltration. After each level of ultrafiltration, the composition of WPC was monitored. Similarly, the initial whey was adjusted to 3.0, 6.2 and 7.0 pH levels and ultrafiltration was carried out to elicit the effect of pH of ultrafiltration on the composition. Further, initial whey was adjusted to different levels of whey protein content ranging from 0.5 to 1.0 per cent and subjected to ultrafiltration to different levels. The various range of retentate obtained were further condensed and spray dried in order to assess the yield of WPC per unit volume of whey used and the quantity of whey required to produce unit weight of product. With the progress of ultrafiltration, there was a progressive increase in protein content and decrease in lactose and ash content. The regression study led to good relationships with $R^2$ values of more than 0.95 between the extents of permeate removed and the resultant changes in composition of each of the constituents. Whey processed at pH 3.0 had significantly a very low ash content and high protein content as compared to processing at 6.2 and 7.0. The yield of WPC per unit volume of whey varied significantly with the initial protein content. Higher initial protein content led to higher yield of all ranges of WPC and the quantity of whey required per unit weight of spray dried WPC significantly reduced. Regression equations establishing the relationship between initial protein content of whey and the yield of various types of WPC have been derived with very high $R^2$ values of 0.99. This study revealed that, the yield and composition of whey can be monitored strictly by controlling the processing parameters and WPC can be produced depending on the food formulation requirement.