• KSBB Journal
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• v.8 no.3
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• pp.256-265
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• 1993

In this study, it was observed that hydrogen productivity varied with changes of input g1ucose concentration and dilution rate in FBR( Fixed Bed Reactor), and CSTR(Continuous Stirred Tank Reactor). We evaluated and compared reaction rate Parameters and internal external and overall mass transfer resistances of immobilized carrier in both reactors. Apparent $K_m$ decreased with increasing dilution rate in FBR but showed a constant value above $0.4h^{-1}$ of dilution rate in CSTR. The experimental results in FBR showed nearly analogous to those in CSTR, however, the performance of FBR resulted in lower hydrogen productivity and an external effectiveness factor but a higher internal effectiveness factor than in CSTR. The overall effectiveness factor obtained with various input 91ucose concentrations showed similar values in both reactors.

• Korean Chemical Engineering Research
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• v.46 no.4
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• pp.752-755
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• 2008

Mesoporous SBA-15 silica-supported TsCHDA and TsDPEN ligands have been prepared by reaction of SBA-15 silica with (1R,2R)-N-(trimethoxysilylpropyl-N-sulfonyl)-1,2-cyclohaxanediamine or (1R,2R)-N-(trimethoxysilylpropyl-N-sulfonyl)-1,2-diphenylethylenediamine-1,2-diphenylethylenediamine, respectively. The Ru complexes exhibited excellent catalytic activity and satisfactory enantioselectivity in the asymmetric hydrogen transfer of ketones under microwave conditions. The heterogeneous Ru catalyst was reusable as well as air-stable to allow easy use. Microwave-assisted efficient procedure has been developed for asymmetric hydrogen transfer.

• Proceedings of the Korean Vacuum Society Conference
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• 2010.08a
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• pp.133-133
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• 2010

중성입자빔 입사장치(neutral beam injection, NBI)의 중성빔 에너지 효율은 이온원의 수소 이온밀도 분율이 결정한다. 이온원에서 만들어진 $H^+$, $H_2^+$ 그리고 ${H_3}^+$는 중성화 과정(neutralization) 중 해리(dissociation) 때문에 각각 입사 에너지의 1, 1/2 그리고 1/3을 가진 중성입자가 된다. 중성빔 에너지 효율 제고하기 위해서는 이온원의 전체 이온 중 단원자 수소 이온 밀도 증가가 필요하다. 유도결합형 수소 플라즈마 이온원에서 RF 안테나 주파수에 따른 플라즈마 밀도와 단원자 수소 이온 밀도 비율 변화를 관찰하였다. RF 플라즈마에서 가스 압력이 결정하는 전자의 운동량 전달 충돌 주파수 대비 높은 RF 안테나 주파수(13.56 MHz)와 낮은 RF 안테나 주파수(수백 kHz)의 전력을 인가하였으며, Langmuir 탐침, 안테나 V-I 측정기 그리고 QMS(quadrupole mass spectrometer)을 이용하여 플라즈마 특성을 진단하였다. 플라즈마 밀도와 수소 이온 밀도 분율은 플라즈마 가열 메커니즘과 수소 플라즈마 내 반응 메커니즘에 의해 결정된다. 플라즈마 가열 메커니즘에 따른 실험 결과에 대한 RF 안테나 주파수 효과는 플라즈마 트랜스포머 회로 모델을 통해 해석하였으며, 수소 플라즈마 내 반응은 0-D 정상 상태의 입자 및 전력 평형 방정식 결과로 해석하였다.

• Journal of Hydrogen and New Energy
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• v.7 no.1
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• pp.45-54
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• 1996

Electrochemical oxidation of hydrogen on PdOx and Pd electrodes were investigated in aqueous 30% KOH solution at different temperatures and hydrogen concentrations(partial pressures). Anodic reaction by hydrogen on PdOx electrode was mainly due to the oxidation of adsorbed hydrogen at -0.8V~-0.5V(vs. Hg/HgO). For Pd electrode, the anodic reaction was participated by the adsorbed hydrogen on surface, as well as by the metal hydride formed from direct reaction between Pd and hydrogen at -0.5V~0.0V(vs. Hg/HgO). With the increase of hydrogen concentration the charge transfer resistance decreased and the exchange current increased. The transfer coefficient of PdOx and Pd electrodes were found to be 0.78 and 0.72 respectively, which shows the superior reactivity of Pd electrode. The activation energies of PdOx and Pd electrodes decreased with the increase of overpotential and were found to be 23.9~20.3 kJ/mole and 7.2~3.0kJ/mole, respectively.

• Journal of Hydrogen and New Energy
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• v.7 no.1
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• pp.93-110
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• 1996

금속수소화물은 열에너지 및 수소저장 또는 에너지변환장치 등에 많은 응용이 기대되고 있다. 특히 금속수소화물을 이용한 최근의 에너지 변환기술은 기술적으로 뿐만 아니라 경제성면에서도 그 가능성이 한층 높아지고 있다. 본문에서는 이와 같은 열변환장치의 하나인 열펌프의 제작에 필요한 동적특성을 P-C-T, 열 및 물질전달, 흡 탈착반응속도 그리고 성능 등의 관계에서 그 발전과정을 살펴보고, 그밖에 실용화에 따른 문제성도 논의하였다.

• Journal of the Korean Chemical Society
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• v.30 no.2
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• pp.166-171
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• 1986

Hydrogen atom transfer reactions, $RNH_2+CH_3{\to}RNH+CH_4\;where\;R=H\;and\;CH_3$, were studied by MINDO/3 MO method. It is expected that stable complex may exist between $CH_3\;and\;NH_3$. Transition state characteristics and activation parameters including activation entropies have been determined. In cases of absolute and activation entropies, results are found to agree in general with ab initio and experimental values, wherever comparisions are possible.

• 한국신재생에너지학회:학술대회논문집
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• 2009.11a
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• pp.527-527
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• 2009

1세대 바이오디젤인 fatty acid methyl ester(FAME)의 문제점을 극복하기 위하여 많은 연구가 진행 중 이다. 소위 차세대 바이오디젤은 triglyceride의 산소 화합물을 제거하여 정유 공정을 통해 생산된 디젤과 동일한 특성을 지닌 탄화수소로 전환시킨 오일이다. 이를 위하여 수소를 첨가하여 산소를 제거 시키는 Hydrodeoxygenation(HDO) 반응이 필요하다. 고온($300-400^{\circ}C$), 고압(50-100 bar)의 혹독한 조건에서 높은 수율과 안정성을 보이는 촉매 개발이 필요하다. 이를 위하여 반응물중의 산소를 효과적으로 제거하기 위하여 산소 전달능이 뛰어난 $CeO_2$ 담체에 열안정성을 높이는 $ZrO_2$를 조합한 $Ce-ZrO_2$ 담체를 선정하였으며 수소첨가 탈산소 반응에 활성을 나타낼 것으로 예상되는 니켈을 활성성분으로 선정하였다. 본 연구에서는 15%Ni-$Ce_{(1-x)}Zr_{(x)}O_2$ ($0{\leq}x{\leq}1$)촉매를 공침법(co-precipitation)으로 제조하였으며 $500^{\circ}C$에서 소성하였다. 촉매 특성분석은 XRD, BET, H2-TPR을 이용하였다.

• Transactions of the Korean Society of Mechanical Engineers
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• v.19 no.1
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• pp.202-211
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• 1995

Heat and hydrogen transfer characteristics have been experimentally investigated for a hydride reaction bed, in which hydride material LaN $i_{4,7}$A $l_{0.3}$ is contained for hydrogen storage. This problem is of particular interest in the design of metal hydride devices such as metal-hydride refrigerators, heat pumps, or metal-hydride storage units. Transient behavior of hydrogen transfer through the hydride materials as well as heat transfer is studied during absorption and desorption processes in detail. The experimental results obtained indicate that the mass flow of the hydrogen is strongly affected by the governing parameters, such as the initial pressure of the reaction bed, absorption or desorption period, and cooling or heating temperature. These mass transfer results are along with the heat transfer rate between hydride materials and heat transfer medium in the reaction bed.d.d.

• Applied Chemistry for Engineering
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• v.10 no.8
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• pp.1210-1215
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• 1999

Optimum conditions of the hydrogenation of PNA to pure PPD were determined in a three-phase slurry reactor with suspended Pd/C catalyst particles. Minimization of mass transfer resistances at the interfaces of both gas-liquid and liquid-catalyst particles and control of overall reaction rate on catalyst surface leaded to decrease the hydrogen starvation on reaction active sites and to reduce the side reactions during hydrogenation. The optimum temperature, pressure, and catalysst concentration were confirmed to be in the range of $60^{\circ}C$, 60~70 psig, and 1~2 g-cat/L, respectively. Reaction rate was zero order with respect to the concentration of PNA and 1st order with respect to the pressure of hydrogen(P). Overall rate expression of the reaction was $R_A=6.44{\times}10^6{\cdot}H{\cdot}P{\cdot}m{\cdot}$exp(-4659/T) where H is constant, m is concentration of catalyst, and T is temperature.

• Proceedings of the Korean Nuclear Society Conference
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• 1999.05a
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• pp.325-325
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• 1999