• Proceedings of the Membrane Society of Korea Conference
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• 1995.04a
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• pp.56-57
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• 1995

막반응기는 반응물이나 생성물을 선택적으로 분리함으로써 반응과 분리를 동시에 수행한다. 이러한 막반응기는 주로 열역학적인 평형에 의해 전화율이 제약되는 반응의 전화율을 높이기 위해서 연구되어 왔다. 수소의 저장 방법의 하나인 액상 하이드라이드법에서 저장된 수소를 다시 분리해 내기 위해 사용되는 사이클로헥산의 탈수소화 반응에 대해 많은 연구가 이루어졌다. 그러나 앞선 연구자들의 결과는 막의 투과도가 낮아서 반응기의 performance가 투과율에 의해 결정된다고 보고하였다. 본 연구에서는 막의 투과도와 촉매 양의 변화에 따른 사이클로헥산 탈수소화 반응의 전화율 변화를 전산모사함으로써, 최적 혹은 최대의 전화율을 나타내는 투과도 및 촉매 양을 결정하는 방법을 제시한다.

• Journal of the Korean Vacuum Society
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• v.3 no.4
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• pp.414-419
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• 1994

Surface of Pt/$Al_2O_3$ model catalyst was produced on an aluminum foil with surface area of 1 $cm^2$ The aluminum surface was oxidized under $10 ^5Torr$Torr oxygen and platinum was deposited on top of the oxide layer using a plasma evaporation source. Conversion of I-butene was performed on the model catalyst surface. Isomerization was the major reaction in I-butene conversion on the aluminum oxide layer. Addition of Pt on the aluminum oxide layer induces hydrogenation of I-butene. Selectivity for the hydrogenation increases as the amount of Pt on alumina increases.

• KSBB Journal
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• v.18 no.1
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• pp.65-69
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• 2003

Two molecular imprinted polymers (MIPs) were prepared by using pentoxifylline and a mixture of caffeine-theophylline (2:1, mole ratio) as the templates, MAA as the monomer, and EDMA as the crosslinker The obtained polymer particles (particle size 25-35 $\mu\textrm{m}$) were packed into a HPLC column (150$\times$3.9mm). The selectivity and chromatographic characterization of the imprinted polymers were studied using pentoxifylline, caffeine, theophylline, theobromine as samples and acetonitrile as the mobile phase, Both imprinted polymers showed increased affinity for structural analogues. By using a mixture of caffeine-theophylline templates MIPs, good separations of caffeine, theobromine and theophylline were obtained, and pentoxifylline and caffeine were partly separated.

• Journal of Nuclear Fuel Cycle and Waste Technology(JNFCWT)
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• v.3 no.1
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• pp.41-47
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• 2005

Preparation of ferrocyanide-anion exchange resin and adsorption test of the prepared resin on the Cs$^{+}$$ion were performed. Adsorption capability of the prepared resin on the Cs$^{+}$ion in the simulated citric acid based soil decontamination waste solution was 4 times greater than that of the commercial cation exchange resin. Adsorption equilibrium of the prepared resin on the Cs$^{+}$ion reached within 360 minutes. Adsorption capability on the Cs$^{+}$ion became to decrease above the necessary Co$^{2+}$ion concentration in the experimental range. Recycling test of the spent ion exchange resin by the successive application of hydrogen peroxide and hydrazine was also performed. It was found that desorption of Cs$^{+}$ion from the resin occurred to satisfy the electroneutrality condition without any degradation of the resin.

• Journal of Korea Soil Environment Society
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• v.4 no.3
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• pp.17-24
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• 1999

The effects of hydrophobic chain length and its structure of nonionic surfactants on surfactant adsorption and contaminated diesel removal were studied in kaolin soil. Hydrocarbon chain length and double bond in hydrophobic tail group of nonionic surfactants affected surfactant adsorption and diesel removal efficiency from kaolin soil. The degrees of surfactant adsorption and diesel removal were closely related each other. Among nonionic surfactants we studied, surfactants with shorter hydrophobic chain length and higher HLB value showed lower degree of adsorption and higher efficiency of diesel removal. The existence of unsaturated carbons in the structure of hydrophobic chain enhanced diesel removal by reducing surfactant adsorption to kaolin soil. The best diesel removal was obtained after adsorption saturation was reached. If surfactant concentration was higher than a critical value, diesel removal was reduced probably because of precipitation. liquid crystal formation, or coacervation of surfactants at high concentration.

• Analytical Science and Technology
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• v.9 no.2
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• pp.161-167
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• 1996

An investigation was made of possible ways in which one could control the relative rates of cadmium deposition and hydrogen evolution by binary additive systems. Benzyl alcohol was employed as an additives due to its ability to form a hydrophobic film which inhibit the electroreduction of water to form hydrogen. The second additive was chosen to make the cadmium(II) ion less hydrophilic and increase its ability to cross the hydrophobic benzyl alcohol film and be electrodeposited at the cathode. It was shown by voltammetric and current efficiency studies that ion pairing and complexing additives could be used to accelerate the reduction of cadmium in the presence of the benzyl alcohol film. It was also shown that the benzyl alcohol film lowered the dielectric constant of the solution near the electrode enough to obtain ion pairing between the sodium ion and the negative chloride complex of cadmium and accelerate the reduction of the cadmium. This acceleration did not occur in the sulfate solution in the absence of chloride since cadmium(II) is primarily present as a positive aquo complex and ion pairing, if it occured, would not accelerate but would hinder reduction of cadmium.

• Proceedings of the Membrane Society of Korea Conference
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• 1992.10a
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• pp.59-60
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• 1992

고분자막을 이용한 분리기술은 에너지 절약과 높은 효율성으로 인해 현재 광범위하게 연구되어 지고 있다. CO$_2$와 CH$_4$를 주성분으로 하는 natural gas 분리나 수소회수, $H_2/CO_2$ 분리등의 실제 분리목적을 수행하기 위해서는 동시에 투과도와 선택도가 높은 막의 개발이 필요한데, 이러한 두가지 분리막 특성을 향상시키기 위해 새로운 고분자 재질의 개발이나 박막화등을 시도하여 왔다.

• Applied Chemistry for Engineering
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• v.16 no.1
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• pp.144-149
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• 2005

Sulfonated poly(ether ether ketone) (SPEEK) was blended with poly(ether sulfone) (PES) at various compositions. To investigate the possibility of using the blend membranes as polymer electrolyte membranes for direct methanol fuel cell, the blend membranes were characterized in terms of methanol permeability, proton conductivity, ion exchange capacity, and water content. Both proton conductivity and methanol permeability of SPEEK were relatively high. As the amount of PES increased, methanol permeability decreased more rapidly compared to proton conductivity. The experimental results indicated that the blend membrane with 40 wt% PES was the best choice in terms of the ratio of proton conductivity to methanol permeability.

• Korean Journal of Food Science and Technology
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• v.29 no.4
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• pp.687-692
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• 1997

During the hydrogenation of rapeseed oil, reaction kinetics and physicochemical characteristics with catalysts (UP9900, DM3, Nysosel 222) were determined. Hydrogenation reaction rates for the UP 9900, Nysel DM3 and Nysosel 222 were $1.6{\pm}0.1\;({\times}10^{-2}),\;1.2{\pm}0.1\;(10^{-2}),\;1.2{\pm}0.1\;(10^{-2})$, respectively. The selectivities for the linoleic acid and oleic acid were determined to be $0.9{\sim}1.5\;and\;39{\sim}44$ at 20 min. From these results, the use of catalysts was shown to be non-selective. Trans isomer content in Nysosel 222 was 32% when the reduction rate of iodine value was 38%, that in Nysel DM3 was 28% at the reduction rate of 45%. UP9900 showed no influence on the trans isomer content. Below the melting point of $35^{\circ}C$, oleic acid and trans isomer acid were increased. On the other side, over the melting point of $35^{\circ}C$, oleic acid was decreased and trans isomer acid was constant. And this tendency was also appeared at the reduction rate of iodine value of 38%.

• Membrane Journal
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• v.20 no.3
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• pp.210-216
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• 2010

The hydrogen permselective membrane were prepared by chemical vapor deposition (CVD) aiming at the applications to hydrogen iodide decomposition in the thermochemical IS process, and it was evaluated for the possibility as a separation membrane. An electron probe X-ray microanalyzer (EPMA) and SEM picture were used to analyze the morphology and structure of the prepared membranes. It was confirmed that Zr-Si-O layer exist in the surface of the prepared membrane using zirconia coated support. Single-component permeance to $H_2$ and $N_2$ were measured at $300{\sim}600^{\circ}C$. Hydrogen permeance through the Z-1 membrane at a permeation temperature of $600^{\circ}C$ was about $1{\times}10^{-7}\;mol{\cdot}Pa^{-1}{\cdot}m^{-2}{\cdot}s^{-1}$. The selectivities of $H_2/N_2$ at $600^{\circ}C$ were 5.0 and 5.75 for Z-1 and Z-2 membrane, respectively.