• 한국막학회:학술대회논문집
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• 한국막학회 1991년도 추계 총회 및 학술발표회
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• pp.29-33
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• 1991

Alumina UF membranes were prepared by sol-gel process and their gas permeabilities were characterized. Alumina MF membrane with average pore diameter about 0.12$\mu$m and tubular shape was used as a support. Gas permeation measurements of helium and nitrogen gas exhibited the permeabilities of 1.58 $\times$ 10E-6 and $0.63 \times 10E-6 cc\cdot cm(STP)/cm^2\cdot sec \cdot cmHg$, respectively. The permeability ratio was 2.5. This means the gas permeation is fully governed by knudsen diffusion mechanism.

• Korean Chemical Engineering Research
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• 제49권4호
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• pp.460-464
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• 2011

Poly(ether-block-amide)(PEBA, $PEBAX^{TM}$)는 열가소성 탄성체(thermoplastic elastomer, TCU)로서 hard-rigid amide block과 soft-flexible ether block으로 구성되어 있으며, 분자량과 두 block간의 구성비에 따라 여러 종류가 있다. $PEBAX^{TM}$는 분리막소재로 이용할 경우, $PEBAX^{TM}$의 hard amide block은 우수한 기계적 특성과 선택도를, 그리고 soft ether block은 높은 투과도를 제공할 수 있다. 따라서 본 연구에서는 2종류의 $PEBAX^{TM}$를 사용하여 기체분리막을 제조하고, 종류에 따른 이산화탄소와 메탄의 투과특성 변화를 연구하였다. 또한 순수 $PEBAX^{TM}$ 분리막의 투과특성을 향상시키기 위해 무기전구체로서 TEOS(tetraethoxysilane)를 사용하여 $PEBAX^{TM}$/TEOS 하이브리드막을 제조하고, 그 투과특성을 순수 $PEBAX^{TM}$ 분리막의 결과와 비교하였다. 순수 $PEBAX^{TM}$-1657과 $PEBAX^{TM}$-2533 분리막의 투과도 측정 결과, ether block의 비율이 상대적으로 높은 $PEBAX^{TM}$-2533 분리막의 투과도 계수가 보다 높은 투과도 계수값을 가졌다. 이는 $PEBAX^{TM}$-2533의 경우, 상대적으로 높은 ether block 함량 때문에 고분자 사슬의 유연성이 보다 크기 때문으로 볼 수 있다. $PEBAX^{TM}$/TEOS 하이브리드 분리막의 투과특성을 순수 $PEBAX^{TM}$ 분리막의 결과와 비교할 때, 하이브리드 분리막의 기체 투과도 계수가 보다 높음을 알 수 있다. 이는 TEOS의 축합반응으로 생성된 silica domain에 의해 결정성이 감소하고 또한 이산화탄소와 silanol group과의 친화도(affinity) 증가에 따른 용해도가 증가하기 때문으로 볼 수 있다. 하이브리드 분리막의 투과도 계수 증가에도 불구하고 이상분리인자는 거의 비슷하거나 약간 감소하였음을 알 수 있다. 이는 이산화탄소와 silanol group의 친화도 증가로 인한 용해선택도의 증가에 기인한 것으로 볼 수 있다.

• 멤브레인
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• 제20권2호
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• pp.106-112
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• 2010

본 연구에서는 poly(phenylene oxide) (PPO)의 막 표면에 100 ppm의 농도를 갖는 불소가스를 접촉시켜 표면불소화하였다. 표면 개질된 막의 특성을 알아보기 위하여 표면접촉각, XPS, 기체투과 실험을 수행하였다. 표면특성 분석 결과 불소처리 시간이 증가함에 따라 막 표면에 $-CF_2$, $-CF_3$의 perfluoro group의 결합으로 인해 막의 소수성이 증가함을 알 수 있었다. 기체투과 측정으로부터 불소화시간이 증가함에 따라 기체에 대한 투과도는 감소하였으며, 불소노출이 60분 경과한 막의 경우 질소 33%, 산소 23%, 이산화탄소 3%의 감소율을 나타내었다. 선택도의 경우 질소 대비 산소의 경우 3.92로부터 4.47로, 이산화탄소에 대한 질소의 경우 18.09에서 25.4로 증가함을 얻었다.

• Macromolecular Research
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• 제15권6호
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• pp.565-574
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• 2007

In this study, five representative, commercially available polymers, Ultem 1000 polyetherimide, Kapton polyimide, phenolic resin, polyacrylonitrile and cellulose acetate, were used to prepare pyrolyzed polymer membranes coated on a porous {\alpha}-alumina$ tube via inert pyrolysis for gas separation. Pyrolysis conditions (i.e., final temperature and thermal dwell time) of each polymer were determined using a thermogravimetric method coupled with real-time mass spectroscopy. The surface area and pore size distribution of the pyrolyzed materials derived from the polymers were estimated from the nitrogen adsorption/desorption isotherms. Pyrolyzed membranes from polymer precursors exhibited type I sorption behavior except cellulose acetate (type IV). The gas permeation of the carbon/{\alpha}-alumina$ tubular membranes was characterized using four gases: helium, carbon dioxide, oxygen and nitrogen. The polyetherimide, polyimide, and phenolic resin pyrolyzed polymer membranes showed typical molecular sieving gas permeation behavior, while membranes from polyacrylonitrile and cellulose acetate exhibited intermediate behavior between Knudsen diffusion and molecular sieving. Pyrolyzed membranes with molecular sieving behavior (e.g., polyetherimide, polyimide, and phenolic resin) had a $CO_2/N_2$ selectivity of greater than 15; however, the membranes from polyacrylonitrile and cellulose acetate with intermediate gas transport behavior had a selectivity slightly greater than unity due to their large pore size.

• 한국산업융합학회 논문집
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• 제4권1호
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• pp.77-85
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• 2001

This paper was to investigate the preparation of polysulfone(PS), polyethersulfone(PES) and polyphenylsulfone(PPS) membrane. The thermal property of PPS was higher than that of others. From the result of SEM, the concentration of polymer was found to have a significant effect on the structure of membrane, and the structure of membrane made of PES is found to have regular micell form of asymmetry. Permeability and selectivity for oxygen and nitrogen gas in the air were analyzed by GC. Permeabilities of the membrane made of PES for oxygen and nitrogen in air, 1.5 and $0.7(x10^9[cm^3(STP)cm/cm^2seccmHg]) $, respectively was higher than that of others. and Selectivity of the membrane made of PPS for oxygen to nitrogen gas in air was 2.9.

• 한국세라믹학회지
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• 제29권11호
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• pp.905-911
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• 1992

Model equations for the gas permeation through a ceramic composite membrane were derived for examining the existence of crack, the reproducibility, and the microstructural properties of composite membranes. From the results of analyzing the nitrogen permeability data through alumina-tube supported TiO2 and SiO2 composite membranes, the extent of cracking, and the formation and structure of membrane top-layers were modelled. It was proved that the crack-free and reproducible composite membranes could be easily prepared only by the pore-filled coating within pores of the support in the sol-gel coating process.

• 멤브레인
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• 제22권6호
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• pp.435-440
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• 2012

본 연구에서는 용매열합성법(solvothermal method)을 이용해 나노기공 HKUST-1 분리막을 제조하였다. In-situ 용매열합성법을 이용하는 경우, 매크로 기공의 알루미나 지지체 위에 균일하고 균열이 없는 HKUST-1 층을 형성하기 어렵다. 본 연구에서는 용매열합성 전에 알루미나 지지체의 표면을 가열한 상태에서 용매열합성의 전구체 용액을 분무하므로 연속적이고 균열이 없는 HKUST-1 분리막을 제조할 수 있었다. 합성된 HKUST-1 분리막은 XRD, FE-SEM 및 단일 기체투과 실험 등을 통해 분석하였다.

• 한국막학회:학술대회논문집
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• 한국막학회 2003년도 The 4th Korea-Italy Workshop
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• pp.129-132
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• 2003

Silica/SUS composite membranes were prepared for CO removal from products of methanol steam reforming. A support was prepared by coating Ni powder of sub-micron and SiO$_2$ sols of particle size of 500nm and 150nm in turns on a porous stainless steel (SUS) substrate. Silica top layer was coated on the modified support using colloidal sol with nanoparticle. As a result of mixture gas permeation test of silica composite membrane using H$_2$(99%)/CO(1%), CO concentration of 10000 ppm was reduced to under 81 ppm, which is acceptable in PEMFC anode gas specification. Permeation mechanism through the membrane was mainly molecular sieving.

• 한국막학회:학술대회논문집
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• 한국막학회 2004년도 Proceedings of the second conference of aseanian membrane society
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• pp.33-38
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• 2004

Molecular modeling of gas permeation through zeolite membranes with/without intercrystalline region was carried out. Molecular dynamics (MD) and Monte Carlo (MC) simulations were performed to estimate the diffusion coefficient and adsorption parameters respectively, and our proposed combined method of molecular simulation techniques with a permeation theory (CMP) was used to estimate gas permeability. The calculated permeability of gases (Ar, He, Ne, $N_2$, $0_2$, $CH_4$) at 301 K for the single crystal membrane model was about one order of magnitude larger than the experiential values, although the dependence on the molecular weight of the permeating species agreed with experiments. On the other hand, the estimated permeability using the diffusivity and adsorption parameters of the intercrystalline region model was in good agreement with the experiments. The consistency between experiments and the estimated values means the importance of considering the intercrystalline region and the validity of CMP method to predict the performance of zeolite membranes.

• 한국막학회:학술대회논문집
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• 한국막학회 2003년도 The 4th Korea-Italy Workshop
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• pp.47-50
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• 2003

Carbon-silica membranes were Prepared by Pyrolyzing polyimide/silica composite obtained from ill-situ polymerization of alkoxy silanes via sol-gel reaction. In this study, effects of silica content and silica network in polyimide matrix were focused on the gas permeation and separation properties of the final carbon-silica membrane. The membranes prepared were characterized with a field emission scanning electron microscopy (FE-SEM), a solid state $^{29}$ Si nuclear magnetic resonance spectroscopy ($^{29}$ Si-NMR), an electron spectroscopy for chemical analysis (ESCA), a thermogravimetric analysis (TGA) and gas permeation tests.