• 한국막학회:학술대회논문집
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• 한국막학회 2002년도 제10회 하계 Workshop
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• pp.59-101
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• 2002

PVDF is good material for a hollow fiber membrane with high porosity and excellent hydrophobicity. Asymmetric PVDF hollow fiber membranes were prepared by the Loeb-Sourirajan phase inversion method. Asymmetric PVDF hollow fiber membranes could be controlled in pore size and porosity using various additives(LiCl, ZnCl$_2$) and internal coagulants (water, EtOH/water, and DMAc/water mixture). $CO_2$removal efficiency of asymmetric PVDF hollow fiber membranes was 1.2 times high than that of commercialized PP hollow fiber membranes at MEA 5wt% solution. $CO_2$flux of asymmetric PVDF hollow fiber membranes was 2.5 times higher than that of commercialized PP hollow fiber membranes. $CO_2$removal efficiency and absorption rate of asymmetric PVDF hollow fiber membranes were 30 times higher than those of packed column at absorbent $H_2O$. $CO_2$flux of asymmetric PVDF hollow fiber membranes at MEA 5wt% solution was 48 times higher than that of pure water. In the case of MEA 5wt% solution used as an absorbent, the $CO_2$absorption rate and removal efficiency of PVDF hollow fiber membrane were 2.3 times higher than that of a packed column.

• KSBB Journal
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• 제16권3호
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• pp.259-263
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• 2001

The development of hollow fiber reactor system for the production of chiral 1,2-epoxy-7-octence by epoxide hydrolase for Rhodotorula glutinis was investigated. Dodecane with high solubility of the racemic substrate passed through the lumen side of the hollow fiber reactor and cell suspension was recirculated through the shell side. The 2nd hollow fiber reactor was coupled to the production reactor to extract the diol byproduct which was the inhibitor of epoxide hydrolase. Optically pure (S)-1,2-epoxy-7-octene (0.6 M in dodecane) could be obtained using hollow-fiber reactor system.

• 생약학회지
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• 제34권4호통권135호
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• pp.288-292
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• 2003

We compared the antitumor activity between hollow fiber assay and xenographic animal assay on thirty herbal plants. It is evaluated that the antitumor activity of above 30% is regarded as 'positive response', and its of below 30% is regarded as 'negative response'. The two herbal plants extracts (Ulmus davidiana Hedyotis diffusa) among thirty herbal plants show to be positive in xenographic animal assay and they were also correctly identified as positive by the hollow fiber assay. The correlation of the hollow fiber assay data with xenographic animal assay would suggest that hollow fiber assay presents a potentially unique tool to develop the herbal medicine for cancer.

• 한국막학회:학술대회논문집
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• 한국막학회 1995년도 추계 총회 및 학술발표회
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• pp.5-9
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• 1995

In the dry-jet-wet-spinning process of a hollow fiber membrane, the polymer solution is pumped into a coaxial tube, jet spinneret. The threadline emerging from the spinneret is stabilized by an internal coagulating medium(liquid or gas) as it emerges from the jet orifice. The nascent hollow thread is further stabilized in a quench bath as shown in Fig. 1. In this scheme, three mechanism of formatiota(temperature gradient, solvent evaporation, and solvent-nonsotvent exchange) can be combined. The changes which promote stabilization often play a dominant role in determining the ultimate fiber wall structure as well. Hence, in pratice, hollow fiber stabilization and development of membrane structure are commonly inseparable. However, fiber dimension(the inside diameter and wall thickness of the hollow fiber) is mainly a rheological problem and is determined by dope pumping rate, spinneret diatance from the coagulation bath, inner coagulant flow rate, and fiber draw-rate. Besides rheological phenomena play a prominent part in the final properties of the hollow fiber.

• 한국환경과학회지
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• 제25권3호
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• pp.395-403
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• 2016

This study examined the adsorption effect of aromatic pesticides by hollow fiber NF membrane on rejection and removal properties. Batch type adsorption test and hollow fiber NF membrane filtration were conducted with 5 different kinds of aromatic pesticides. 3 to 15 days were required to reach the equilibrium concentration and $0.3181{\sim}0.8094{\mu}g/cm^2$ were adsorbed to hollow fiber NF membrane. Since 5 hours of separation test were too short to keep steady state for permeate due to the repetition of sorption and desorption, longer times were required to evaluate the rejection performance of NF membrane. Sorption and desorption were confirmed by the separation test equipped with membrane and without membrane. Adsorption contribution of aromatic pesticides to hollow fiber membranes were shown to be ranged from 16.1% to 36.3% and indicated the difference considering sorption effect.

• 멤브레인
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• 제23권4호
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• pp.257-266
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• 2013

본 연구에서는 고온에서 유기용매를 정제할 수 있는 고온, 고압에서 안정한 상업화 규모의 고효율 중공사 투과증발막, 막모듈 개발, 상업 규모의 막분리 장치시스템 개발을 수행하였는데 구성 요소기술은 1) 고온 고압 하에서 사용할 수 있는 브레이드 강화 중공사 막제조, 2) 중공사 막모듈 제조, 3) 막 탈수, 정제장치 시스템 설계 및 제작기술등을 개발하였다. 개발 중 공사 투과증발막은 독일의 슐츠막 보다 막 안정성과 막 성능이 우수하였으며, 막면적 4.6 $m^2$의 고효율 상업적 규모의 중공사막모듈을 개발하였고, 200 L/hr 이상의 처리용량의 Pilot 규모의 투과증발 막장치 시스템을 개발하였다. 기존 평막 혹은 중공사막에서 모듈에서 볼 수 있었던 모듈내부에 공급액의 dead volume형성, 공급액의 채널링 현상들을 제거하기 위해서 본 개발 중공사막과 막모듈의 특징은 고온, 고압의 유기용매를 중공사막 내부로 공급되어 흐르도록 설계되어 있어 막분리 효율이 우수하며 특히 기존의 막제품의 대비 막모듈 가격이 저렴하고, 막성능 및 치수안정성이 우수하다. 또한 공급액의 열손실 적어 에너지 효율이 우수할 뿐 아니라 막모듈 내에 중공사막 사이의 간격이 일정하여 가해주는 진공이 균일하게 각 중공사막의 투과부 표면에 전달될 수 있기 때문에 투과된 투과물을 막 표면으로부터 효과적으로 제거할 수 있으므로 투과속도 또한 우수하다.

• 생명과학회지
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• 제13권6호
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• pp.788-793
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• 2003

Rhodosporidium toruloides SJ-4의 epoxide hydrolase의 입체선택적 가수분해 반응을 이용하여 hollow-fiber 반응기에서 라세믹 phenyl oxirane 기질로부터 광학활성 phenyl oxirane을 생산하였다. 라세믹 에폭사이드 기질의 수용액 상에서의 낮은 용해도로 인한 저농도 반응의 문제점을 극복하기 위하여 dodecane 유기용매에 용해시켜 lumen 부위로 공급하였으며, 생촉매인 R. toruloides 세포 현탁액은 수용액강인 shell 부위에 위치시킴으로써 유기용매 사용에 따른 생촉매 활성 저하를 줄인 1단계 반응기 시스템에서는 200 mM의 고농도에서 (S)-phenyl oxirane을 생산할 수 있었다. 또한, 반응 산물로 생성되는 diol에 의한 생촉매 활성저해효과를 감소시키기 위하여 2단계 hollow-fiber 반응기에서는 완충용액을 이용하여 diol을 제거시킨 결과 300 mM에서 EH 활성을 이용한 입체선택적 가수분해반응을 수행할 수 있었으며, 200∼300 mM의 고농도 라세믹 기질로부터 99% ee 이상의 광학순도를 가진 (S)-phenyl oxirane을 이론 수율 대비 12∼35% 수율로 얻을 수 있었다.

• Membrane and Water Treatment
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• 제5권2호
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• pp.109-122
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• 2014

Polyvinylidene fluoride (PVDF) hollow fiber membrane is widely used for water treatment. However, the weak mechanical strength of PVDF limits its application. To enhance its tensile strength, a double-layer composite hollow fiber membrane, with PVDF and polyetherimide as the external and inner layers, respectively, was successfully prepared through phase inversion technique. The effects of additive content, air gap distance, N,N-dimethyl-acetamide content in the inner core liquid, and the temperature of external coagulation bath on the membrane structure, permeation flux, rejection, tensile strength, and porosity were determined. Experimental results showed that the optimum preparation conditions for the double-layer composite hollow fiber membrane were as follows: PEG-400 and PEG-600, 5 wt%; air gap distance, 10 cm; inner core liquid and the external coagulation bath should be water; and temperature of the external coagulation bath, 40 C. A single layer PVDF hollow fiber membrane (without PEI layer) was also prepared under optimum conditions. The double-layer composite membrane remarkably improved the tensile strength compared with the single-layer PVDF hollow fiber membrane. The permeation flux, rejection, and porosity were also slightly enhanced. High-tensile strength hollow fiber PVDF ultrafiltration membrane can be fabricated using the proposed technique.

• 생명과학회지
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• 제12권5호
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• pp.584-588
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• 2002

Apergillus niger LK의 epoxide hydrolase 활성을 이용하여 chiral styrene oxide를 제조할 수 있는 hollow-fiber 반응기 기반의 비대칭 분할 시스템을 개발하였다. 라세믹 styrene oxide 기질을 dodecane 유기용매에 용해시켜 hollow-fiber 반응기의 lumen 부위로 공급하였으며, 생촉매인 A. niger LK 미세분말은 shell 부위로 공급함으로써 막 표면에서 비대칭 분할 반응을 수행하였다. 반응 산물로 생성되는 phenyl-1,2-ethandiol에 의한 epoxide hydrolase 활성 저해효과를 감소시키기 위하여 2번째 hollow-fiber 반응기에서 완충용액을 이용하여 diol을 추출하여 제거시켰다. 2성분 용매를 사용한 cascade형 hollow-fiber 반응기 시스템을 이용하여 광학적으로 순수한 (ee > 99%) (5)-styrene oxide를 19.5% (이론 수율 대비 39%)의 수율로 얻을 수 있었다.

• 한국환경과학회지
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• 제9권2호
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• pp.173-176
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• 2000

This study was carried out to investigate the filtration characteristics of membrane modules according to hollow fiber dispersion for direct solid-liquid separation of activated sludge. 2 bundle, 4 bundle, and 10 bundle, and 10 bundle module used in this experiment according to hollow fiber dispersion was manufactured at laboratory and permeate flux and transmembrane pressure(TMP) of each module were observed under a suction pressure of 0.5kgf/c$m^2$. As the hollow fibers were dispersed, permeate flux was increased and TMP was decreased. Permeate flux and TMP of each module was 15.0 $\ell$/$m^2$.h and 31.8 cmHg for 2 bundle, 16.0 $\ell$/$m^2$ .h and 17.4 cmHg for 4 bundle, and 20.4 $\ell$/m2 .h and 31.8 cmHg for 10 bundle. In conclusion, the membrane fouling is expected to be decrease by maintaining lower TMP with hollow fiber dispersion.