• Transactions of the Korean Society of Mechanical Engineers B
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• v.36 no.9
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• pp.885-894
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• 2012

A numerical study of a microchannel steam methane reforming reactor has been performed to understand the characteristics of heat and mass transfer. The integration of Rh-catalyzed steam methane reforming and Pt-catalyzed methane combustion has been simulated. The reaction rates for chemical reactions have been incorporated into the simulation. This study investigated the effect of contact time, flow pattern (parallel or counter), and channel size on the reforming performance and temperature distribution. The parallel and counter flow have opposite temperature distribution, and they show a different type of reaction rate and species mole fraction. As the contact time decreases and channel size increases, mass transfer between the catalyst layer and the flow is limited, and the reforming performance is decreased.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.35 no.6
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• pp.641-648
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• 2011

Off-gases emitted from the anode of a molten carbonate fuel cell (MCFC) at high temperatures for power generation are used as fuel in catalytic combustion. The heat generated in the catalytic combustor is utilized as the heat for the endothermic reaction required for steam reforming. Among the various operational conditions of the integrated reactor, we varied the inlet gas compositions of the catalytic combustor according to fuel utilization in the MCFC and the ratio of steam to carbon in the reformer. Subsequently, the thermal behaviors and reaction characteristics of the integrated reactor were investigated experimentally. The fundamental data from this experimental study will be useful for the design and fabrication of a more practical integrated reactor in the future.

• Clean Technology
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• v.20 no.3
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• pp.256-262
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• 2014

Catalytic oxidation characteristics of benzene as a VOC was investigated in a fixed bed flow reactor using $Cu/{\gamma}-Al_2O_3$ catalyst. The parametric tests were conducted at the reaction temperature range of $200{\sim}500^{\circ}C$, benzene concentration of 400~650 ppm, gas flow rate of 50~100 cc/min, and space velocity range of $7,500{\sim}22,500hr^{-1}$. The property analyses by using the BET, SEM, TGA and the conversion of catalytic oxidation of benzene were examined. The experimental results showed that the conversion was increased with decreasing benzene concentration, gas flow rate and space velocity. Benzene oxidation reaction over $Cu/{\gamma}-Al_2O_3$ catalyst could be expressed as the first order homogeneous reaction of which the activation energy was 17.2 kcal/mol and frequency factor was $1.33{\times}10^6sec^{-1}$.

• Journal of the Korean Ceramic Society
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• v.37 no.10
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• pp.938-943
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• 2000

TiCl$_4$, 물 및 1-propanol의 혼합용액으로부터 미립 TiO$_2$분말 제조시, 1-propanol과 물의 부피비, 반응온도, 반응유지시간 및 TiCl$_4$mole 농도에 따른 분말 특성 및 결정상 생성에 대해 조사하였다. 반응온도가 3$0^{\circ}C$ 이상일 때 Ti 수화물의 초기 침전이 생성되었고 반응온도가 TiCl$_4$mole 농도가 증가함에 따라 입자크기는 증가하였고 $600^{\circ}C$ 하소시 1-propanol과 물의 부피비가 2보다 크고 반응온도가 7$0^{\circ}C$보다 낮을 때 주결정상은 anatase였다. 입자크기가 미세하고 입자크기 분포가 좁은 범위를 갖는 조건은 1-propanol과 물의 부피비가 2, 반응온도가 7$0^{\circ}C$, TiCl$_4$mole 농도가 0.2 mole/ι일 때였으며, 결정상의 생성은 1-propanol과 물의 부피비가 2, 반응온도가 3$0^{\circ}C$ 이상일 때 anatase에서 rutile로 전이하는 온도가 높아졌다. 이와 같은 반응인자에 따른 효과는 용매의 유전상수, 티타니아의 용해도, 입자의 표면전위 등의 효과와 관계가 있었다.

• Journal of the Korean Solar Energy Society
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• v.21 no.3
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• pp.1-8
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• 2001

The chemical heat storage as the one way of utilization for high temperature solar energy was considered. The stram reforming reaction of methane was chosen for endothermic reaction. The reactor was made of stainless steel and the dimension was 6.25 mm I.D. and 30 cm long coiled tube because of the geometry requirement of solar receiver. The methane conversion was increased linearly with reaction temperature and nickel content of catalyst. The methane conversion was 60% at $600^{\circ}C$ and 90% at $900^{\circ}C$. The feasibility of steam reforming of methane as the conversion of solar energy to chemical heat storage was confirmed.

• Journal of Korean Society of Environmental Engineers
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• v.22 no.4
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• pp.651-659
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• 2000

The characteristics of ammonia removal by natural neutralizer were studied by using a scrubber type equipment. As operation parameters, neutralizer dilution ratio, neutralizer inlet flowrate, air flowrate and initial ammonia concentration were selected and their effects on ammonia removal efficiency were investigated. The optimal removal effect was achieved at neutralizer dilution ratio of 1.0% and neutralizer inlet flowrate of $60m{\ell}/min$. On the other hand, with respect to air flowrate and initial ammonia concentration, there was no significant effect on removal efficiency, when loading rate was considered. In addition, ammonia removal reaction was investigated by analyzing the ammonia oxides, such as nitrites and nitrates, after reacting ammonium solution with natural neutralizer. The result shows a partial oxidation by natural neutralizer besides dominant absorption of ammonia.

• Korean Journal of Materials Research
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• v.9 no.3
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• pp.307-314
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• 1999

The effect of manufacturing variables, such as reactant powder$(TiB_2, B_4C)$, sintering temperature, and sintering time has been investigated on the microstructure and the mechanical properties of in-situ processed Ti/TiB composites. The mechanical properties were evaluated by measuring the compressive yield strength. The compressive yield strength of the in-situ processed composites was higher than that of the Ti-6AI-4V. The compressive yield strength of the composite made with TiE, reactant powder was higher than that of $B_4C$, mixed at the same volume fraction of reinforcement. It is because bonding nature between the matrix and the $TiB_2$, reactant powder was more strong than that of the other materials. It was proven by the examining the crack propagation path.

• Applied Chemistry for Engineering
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• v.22 no.6
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• pp.653-657
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• 2011

Conversion characteristics of $CH_4$ and $CO_2$ was studied using an atmospheric pressure plasma for the preparation of synthesis gas composed of $H_2$ and CO. The effects of delivered power, total gas flow rate, and gas residence time in the reactor on the conversion of $CH_4$ and $CO_2$ were evaluated in a plasma reactor with the type of dielectric barrier discharge. The increase of reactor temperature did not affect on the increase of conversion if the temperature does not reach to the appropriate level. The conversion of $CH_4$ and $CO_2$ largely increased with increasing the delivered power. As the $CH_4/CO_2$ ratio increased, the $CH_4$ conversion decreased, whereas the $CO_2$ conversion increased. Generally, the $CH_4$ convesion was higher than the $CO_2$ conversion through the variation of the process parameters.

• Proceedings of the Materials Research Society of Korea Conference
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• 1999.11a
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• pp.113-113
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• 1999

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 1997.10a
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• pp.54-58
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• 1997