• 한국막학회:학술대회논문집
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• 한국막학회 2003년도 The 4th Korea-Italy Workshop
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• pp.77-80
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• 2003

Hydrocarbon-hydrocarbon separations are one of the most important processes in petroleum refining. Distillation process has been used for separating hydrocarbons, but this conventional process is very energy consuming. Pervaporation separation through polymeric membranes is an emerging process alternative to distillation because of energy savings, compact system installation, reduced capital investment, and other performance attributes. In hydrocarbon separations, polymeric membranes are easily swollen by hydrocarbons and can lose mechanical strength. Chemically robust membranes are needed for the separation of hydrocarbons. In this study, the blend membrane was applied to separate benzene and cyclohexane. This is a model system for aliphatic and aromatic separation. Cyclohexane is also physically very similar to benzene and as a result of the very closing boiling points (0.6$^{\circ}C$), benzene and cyclohexane form an azetrope. Thus the system provides a good model for azeotrope breaking by pervaporation. The semi-quantitative thermodynamic model predicts that the calculated selectivity increases with increasing Hydrin contents in the blend membranes. Pervaporation experiments utilizing various operating temperatures and feed concentrations with different blend membranes are compared with the result from semi-quantitative thermodynamic calculations.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2009년도 춘계학술대회 논문집
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• pp.415-417
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• 2009

A low temperature decal (LTD) transfer method is tried to fabricated hydrocarbon (HC) membrane based MEA. Sandwiched structures of outer ionomer/catalyst/carbon coating/substrate, which had been developed for Nafion membrane, are used for transfer of catalyst to the HC membrane. Performances of the HC MEA before and after 500hr continuous operation are compared and it is found that a severe delamination occurs at the interface between the HC membrane and the catalyst layer, which is the main reason of the low performance and its degradation. The delamination is due probably to the different nature of HC membrane to the Nafion ionomer. A substitutional method, therefore, is suggested to overcome this. In such a way, the outer ionomer process is removed and the low transfer rate of catalyst by skipping the ionomer process is compensated with optimization of other process variables such as transfer time or temperature. The resulting performance is superior to the original LTD method, which can be explained in terms of low resistive components both in ohmic and kinetic.

• 한국막학회:학술대회논문집
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• 한국막학회 2004년도 Proceedings of the second conference of aseanian membrane society
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• pp.51-54
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• 2004

Utilization of membranes offers the promise of extraordinary energy savings if successfully applied to hydrocarbon-hydrocarbon and other organic separations. Membranes are bound to enter into refining and petrochemical operations involving liquid separations once appropriate materials and modules are developed. Hybrid processes such as utilizing membrane modules to break azeotropes formed during distillation are particularly attractive because they offer less process complexity and reduced capital investment[1,2].(omitted)

• 멤브레인
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• 제30권6호
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• pp.395-408
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• 2020

고분자 전해질 막 연료전지(polymer electrolyte membrane fuel cell, PEMFC)는 환경오염물질 배출이 없는 친환경 에너지 변환 장치로 주목을 받고 있다. PEMFC의 구성요소 중 고분자 전해질 막(polymer electrolyte membrane, PEM)은 음극에서 발생되는 수소이온을 양극으로 전달하는 역할과 동시에 분리막으로써 연료의 투과를 차단하는 역할을 수행하는 핵심 소재이다. 대표적으로 Nafion®과 같은 과불소화계 고분자 전해질 막이 상용화 되어있지만 높은 단가 및 분해 시 환경오염물질이 배출되는 단점이 존재하여, 이를 대체할 탄화수소계 고분자를 활용한 전해질 막 개발에 관한 연구들이 수행되고 있다. 높은 수소이온 전도도를 가지며 동시에 우수한 물리·화학적 안정성을 갖는 탄화수소계 고분자 기반 전해질 막을 개발하기 위해 가교 구조가 도입된 전해질 막을 개발하는 연구들이 보고되고 있다. 본 총설은 가교 전해질 막을 제조하기 위해 이온교환 작용기가 도입된 탄화수소계 고분자를 활용하여 다양한 종류의 가교 전해질 막을 제조하는 방법에 대해 논하였다.

• 멤브레인
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• 제25권4호
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• pp.310-319
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• 2015

음이온 교환막의 치환체 특성을 파악하기 위하여 탄화수소의 분자구조가 다른 세 종류의 음이온 교환기를 vinyl benzyl chloride (VBC) base 막에 도입하였다. 지방족계로 trimethylamine (TMA), 고리형계로 N-methylpiperidine (MP), 방향족계로 pyridine (Py)은 아민화 반응을 통하여 도입되었다. 각각의 반응속도는 막저항(MER)과 이온교환능력(IEC) 변화의 관측으로부터 Py < MP < TMA의 순서로 반응하고 있음을 보여주었다. 한편 SEM image에서는 Py 치환체 막이 가장 균일하고 치밀한 구조를 보여주었으며, 전기화학적 특성에서도 Py이 상용막(AMX)과 비슷한 막저항($5.0{\Omega}{\cdot}cm^2$ >, in 0.5 mol/L NaCl)을 나타내었다. 이 모든 결과로부터 치환체의 공명구조는 균질한 이온교환막의 제조에 기여하고 있음을 알 수 있었다.

• Korean Chemical Engineering Research
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• 제54권4호
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• pp.453-458
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• 2016

고분자전해질 연료전지용 MEA (Membrane and Electrode Assembly)와 돼지분뇨를 이용해 미생물연료전지(MFC)를 구동하였다. 미생물 연료전지에서 과불소계막과 탄화수소막의 성능을 비교하였다. 탄화수소막으로 sPAES 막을 사용하였고 과불소계막은 Gore 막을 사용했다. sPAES MEA가 Gore MEA보다 OCV는 50mV 높았고 출력 밀도는 비슷했다. sPAES 막을 강화시킴으로써 성능을 안정시킬 수 있었다. 미생물 연료전지의 셀 온도 $45^{\circ}C$에서 최고의 성능을 얻었고 배양액 순환속도 50 ml/min에서 최고의 성능을 얻었다. 최적 조건에서 돼지 분뇨를 이용한 미생물연료전지에서 최고 $1,100mW/m^2$의 출력 밀도가 발생하였다.

• 한국막학회:학술대회논문집
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• 한국막학회 2002년도 제10회 하계 Workshop
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• pp.103-128
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• 2002

• 한국수소및신에너지학회논문집
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• 제28권3호
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• pp.246-251
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• 2017

To fabricate a hydrocarbon polymer electrolyte composite membrane incorporated with Pt nanoparticle, the polymer electrolyte membrane made of a sulfonated-fluorinated hydrophilic-hydrophobic block copolymer (SFBC) and sulfonated poly (ether ether ketone) (SPEEK) blend in the wight ratio of 1 : 1 was synthesized, and a simple drying process was used in order to incorporate Pt nanoparticle into the SFBC/SPEEK film by reducing platinum (II) bis (acetylacetonate), Pt $(acac)_2$. The distribution of the Pt nanoparticles was observed by transmission electron microscopy (TEM), and mechanical and thermal properties were tested by universal testing machine (UTM) and thermogravimetry analyzer (TGA). Cation conductivity, ion exchange capacity (IEC) and I-V characteristics were estimated.

• The Korean Journal of Physiology and Pharmacology
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• 제7권3호
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• pp.119-124
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• 2003

To elucidate the molecular mechanism of pharmacological action of local anesthetics, we studied membrane actions of tetracaine, bupivacaine, lidocaine, prilocaine and procaine. Fluorescence polarization of n-(9-anthroyloxy)stearic acid (n-AS) was used to examine the effects of these local anesthetics on differential rotational mobility of different positions of the number of synaptosomal plasma membrane vesicle (SPMV) phospholipid carbon atoms. The four membrane components differed with respect to 3, 6, 9 and 16-(9-anthroyloxy)stearic acid (3-AS, 6-AS, 9-AS and 16-AP) probes, indicating that differences in the membrane fluidity might be present. Degrees of the rotational mobility of 3-AS, 6-AS, 9-AS and 16-AP were different depending on depth of hydrocarbon interior. In a dose-dependentmanner, tetracaine, bupivacaine, lidocaine, prilocaine and procaine decreased anisotropy of 3-AS, 6-AS, 9-AS and 16-AP in the hydrocarbon interior of the SPMV. These results indicate that local anesthetics have significant disordering effects on hydrocarbon interior of the SPMV, thus affecting the transport of $Na^+$ and $K^+$ in nerve membranes and leading to anesthetic action.

• 멤브레인
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• 제17권2호
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• pp.112-117
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• 2007

The application of membrane bioreactors for the depuration of wastewater coming from the washing of mineral oil storage tanks is described. Microfiltration hollow-fibre membranes were used in the submerged configuration. Filtration tests were carried out with a biomass concentration of about 15 g/L in order to assess the critical flux of the hollow fibre membrane used. Then particular care was taken in carrying out the performance runs in the sub-critical flux region. The reactor performance was very high, with removal efficiencies ranging between 93% and 97% also when the concentration of hydrocarbon was very high. Some kinetic parameters for the COD and the hydrocarbon removal were estimated.