• Applied Chemistry for Engineering
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• v.23 no.3
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• pp.253-258
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• 2012

The effects of active sites and valence states were investigated over $Pd/TiO_2$ catalyst on simultaneous oxidation of $CH_4$ and CO. The Pd species (PdO) crystallite size increased with increasing Pd loadings, which results in enhancement of the activity of $CH_4$ oxidation. Different results from the activity of $CH_4$ and CO oxidation were shown to be dependent on the Pd valence state on the surface of the catalyst prepared through a thermal treatment. XRD and $H_2-TPR$ analysis confirmed that $Pd^{2+}$species was predominated in the calcination catalyst, while $Pd^0$species was predominated in the reduction catalyst. Additionally, it could be found that the valence state of Pd was a more important factor on the catalytic activity than that of factors as the surface area and pore volume. The reaction mechanism of $CH_4$ and CO followed by the valence state of Pd could be identified using FT-IR analysis.

• Journal of the Korean Chemical Society
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• v.29 no.2
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• pp.111-120
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• 1985

The oxidation reaction of CO on the catalysts 4 mol%, 8 mol%, and 12 mol% Cd-doped ${\alpha}-Fe_2O_3$ is individually investigated. Regardless of Cd doping level, over-all reaction order for the oxidation of CO is 1.5; the first order with respect to CO and the one-half order with respect to $O_2$. Over the temperature range of 350∼$460^{\circ}C$, the activation energy for CO oxidation is 10.10∼11.30Kcal/mol. From the agreement between the kinetic data and conductivity measurements, the reaction mechanism is suggested. Especially from the effect of Cd doping, the fact that catalytic activity of ${\alpha}-Fe_2O_3$ is due to the excitation of electrons which are traped on oxygen vacancy is found, and the adsorption sites for reactant molecules are found.

• Applied Chemistry for Engineering
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• v.10 no.1
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• pp.58-66
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• 1999

The catalytic oxidation of vinyl chloride was investigated over $CrO_x$ impregnated on $Al_2O_3$ at temperature between 200 and $400^{\circ}C$. The major carbonaceous products were CO and $CO_2$, and the selectivity of $CO_2$ was gradually increased with increasing reaction temperature, while that of CO was dropped consequently. This suggests that CO is the first product which is further oxidized to $CO_2$ in the oxidation of vinyl chloride over $CrO_x/Al_2O_3$. The addition of HCl in the feed didn't affect the conversion of vinyl chloride, but the selectivity of $CO_2$ decreased by adding HCl. It implies that HCl inhibits, the complete oxidation of vinyl chloride to $CO_2$. When oxidizing vinyl chloride in dry air, significant amounts of $Cl_2$ were observed, while no $Cl_2$ was detected in the humid condition. The activities of several catalysts including various precious metals and other transition metal oxides were measured, it was found that the catalytic activity of 12% $CrO_x/Al_2O_3$ was higher than other catalysts except 1% $Pt/Al_2O_3$. The reaction rate of 12% $CrO_x/Al_2O_3$ was 1.2 times lower than that of 1% Pt/alumina, but it was 3 to 8 times more active than other catalysts for vinyl chloride oxidation at $275^{\circ}C$.

• Journal of the Korean Chemical Society
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• v.37 no.2
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• pp.183-190
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• 1993

The properties of oxidation reactions of carbon monoxide on ZnO (1010) were studied at the temperature range of 298∼573 K by measuring the capacitance and conductance in the insulating layer of two contacting crystal faces which vary with ZnO-gas interaction mechanisms. Exposure of the sample to CO resulted in an increase in the layer depth at 298∼373 K, while it decreased above 473 K. But the variation of the layer depth was very small in all measurements. When CO was admitted to the sample previously treated with $O_2$ at the same temperature, we observed the different features compared with the case of CO adsorption. From these results we discussed the mechanisms of CO oxidation in connection with the adsorbed oxygen species at each temperature.

• Proceedings of the KIEE Conference
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• 1997.11a
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• pp.294-295
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• 1997

CO-Cr 수직자기기록 매체의 우수한 하지층을 개발하기 위하여, 스피넬 결점막$(Fe,M)_3O_4$ (M=Ni,Zn)이 스핀스프레이 페라이트 플레이팅 방법으로 유리 기판 위에 제작되었다. 반응액과 산화액은 기판이 회전하는 반응용기로 분사되었다. 반응은 기판의 회전소독, 반응온도, 반응액과 산화액의 유속 그리고 반응액과 산화액의 농도에 의해 영향받았다. 반응액과 산화액의 유속은 60(ml/min)으로 하고, 반응온도는 90[$^{\circ}C$] 그리고 기판의 회전속도는 150[rpm]의 조건하에서, 페라이트 플레이팅 반응에 미치는 반응액과 산화액 농도의 영향이 화학적 조성, 결정학적 및 자기적 특성의 관점에서 연구되었다. $Ni_{0.34}Zn_{0.66}Fe_2O_4$의 조성에서, 우리는 가장 안정한 결정학적 및 자기적 특성을 얻었다.

• Korean Chemical Engineering Research
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• v.55 no.2
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• pp.156-162
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• 2017

CuO(x)/0.3Al-0.7Ce catalysts with different CuO loadings (x = 2~20 wt%) were prepared by impregnation method and investigated the effects of CuO loadings on the low temperature CO oxidation. Of the used catalysts, the CuO(10)/0.3Al-0.7Ce catalyst showed the highest catalytic performance in the absence or presence of water vapor. In the presence of water vapor, the catalytic performance was drastically decreased, with a temperature of 50% CO conversion ($T_{50%}$) shifted to higher temperature by $50^{\circ}C$ compared to the those in dry conditions because of the competitive adsorption of water vapor on the active sites. The copper metal surface area calculated from $N_2O$-titration analysis and the oxygen capacity from CO-pulse experiments were increased with the CuO loadings and showed a maximum at 10 wt%CuO/0.3Al-0.7Ce catalyst. These trends are in good agreement with the tendency of $T_{50%}$ of the catalysts. From these characteristic aspects, it could be deduced that the catalytic performance was closely related to the oxygen capacity and the copper metallic surface area.

• 한국신재생에너지학회:학술대회논문집
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• 2011.05a
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• pp.157.1-157.1
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• 2011

선택적 CO 산화반응(PrOx)에 사용되는 촉매 중 Pt, Ru, Rh 등의 귀금속 계 촉매들은 비귀금속 계 촉매에 비해 활성이 좋은 반면 가격이 비싸다는 경제적인 제한점이 있다. 따라서 소량의 귀금속을 사용하여 높은 활성의 촉매를 제조하고자 활성금속의 고분산 담지 방법에 대한 연구가 이루어지고 있다. 본 연구에서는 담체인 ${\gamma}-Al_2O_3$ 표면에 활성금속인 Pt의 고분산 담지를 위해 증착-침전법(Deposition-precipitation)을 적용하였으며 용액의 pH 변화에 따른 Pt 금속 입자의 분산도에 대한 영향을 살펴보았다. Pt의 함량은 1wt%로 고정하였고 침전제로 NaOH를 사용하여 용액의 pH를 pH 7.5 ~ 10.5로 변화시켰다. 제조된 촉매는 세척 후 $400^{\circ}C$, 3시간 소성 하였다. 제조된 1wt% Pt/$Al_2O_3$ 촉매의 특성분석을 위해 BET, TPR, CO-chemisorption을 수행하였다. PrOx 반응 실험은 GHSV=60,000 $ml/g_{cat}{\cdot}h$, $T=100{\sim}200^{\circ}C$, ${\lambda}$=4 조건에서 수행되었으며 반응 전에 촉매는 $400^{\circ}C$, 3시간 환원 후 사용하였다. 촉매의 특성분석과 PrOx 반응 실험 결과를 통해 촉매가 담체 위에 고분산 되는 최적의 pH를 확인할 수 있었으며, 기존의 함침법으로 제조된 촉매와 성능 비교를 통해 제조방법에 따른 영향을 살펴보았다.

• Journal of the Korean Chemical Society
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• v.19 no.6
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• pp.423-427
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• 1975

Changes in the electrical conductivity of gallium doped zinc oxide during the dehydrogenative oxidation of ethanol between 250 and $350^{\circ}C$ have been studied. Both dehydrogenation and dehydration of ethanol takes place on ZnO. At $300^{\circ}C$ and above formation of $CO_2$ was observed accompanied by an increase in the electrical conductivity. This seems to be due to oxidation of CO formed by the decomposition of acetaldehyde. Addition of oxygen to ethanol increases the amount of acetaldehyde formed, while no change is observed in ethylene formation. It may be that oxygen which is present primarily as $O^-$ provides a favorable site for the adsorption of ethanol and for subsequent hydrogen substraction.

• Journal of Life Science
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• v.2 no.2
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• pp.91-96
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• 1992

효소에 의한 carotenoid의 co-oxidationgus상은 lipoxygenasechrao하에서 지방산인 linoleic acid가 산화되어 이때 만들어진 free radical에 의해 carotenoid가 쉽게 산화되기 때문에 일어나는 현상이다. 이화같이 carotenoid의 co-oxidation에서 lipoxygenase는 free radical을 만들면서 반응속도를 빠르게 하는 촉매제의 역할을 다음과 같이 담당하고 있다고 할 수 있다. Lipoxygenase에 의한 carotenoid의 co-oxidation 현상을 처음 발견한 것은 대두가루를 밀가루와 혼합하여 사용할 때였다. 대두가루 속에 다량 함유된 lipoxygenase에 의해 밀가루의 carotenoid 색소가 표백되는 것을 보고 이 현상은 lipoxygenase에 의해 기질은 지방산이 산화되는 동안 caroenoid가 쉽게 co-oxidation되기 때문이라는 것을 알아내었다. 즉, carotenoid는 지질이 존재하는 반응시스템에서 항산화제로서 혹은 secondary substrate로서 작용한다고 할 수 있다.

• Clean Technology
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• v.17 no.1
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• pp.41-47
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• 2011

[ $MnO_2$ ]catalysts were prepared by precipitation method using potassium manganate and manganese acetate. The effect of calcination temperatures of $MnO_2$ catalysts for CO oxidation has been studied and their physicochemical properties were studied by X-ray diffraction (XRD), $N_2$ sorption, temperature programmed reduction of $H_2$ ($H_2-TPR$), and temperature programmed desorption of CO (CO-TPD) techniques. $MnO_2$ calcined at $300^{\circ}C$ catalyst has a large surface area $181m^2/g$ having a narrow pore size distribution at 9 nm. The results of XRD and $H_2-TPR$ showed that the catalysts calcined at different temperatures showed mixed oxidation states of Mn such as $Mn^{4+}$ and $Mn^{3+}$. CO-TPD showed that the quantity of $CO_2$ desorbed was decreased with increasing the calcination temperatures. The catalytic activity over the catalyst calcined at $300^{\circ}C$ exhibited the highest conversion reaching to 100% at $200^{\circ}C$. $H_2O$ vapor showed an inhibiting effect on the efficiency of the catalyst because of co-adsorption with CO on the active sites of manganese oxide catalysts and the initial catalytic activity of CO oxidation could be regenerated by removing $H_2O$ vapor in the reactants.