• The Journal of the Korea Contents Association
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• v.11 no.8
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• pp.468-474
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• 2011

Reducing agent was used as process variable for Pt catalyst production process. By using six sigma the optimum operating variables condition for particle size and ICP yield were deduced. With the help of fractional factorial design the major variables were reduction temperature and process time. Also, the optimum number of reduction process, reduction temperature, quantity of reducing agent and process time were 1, $67-88^{\circ}C$, 0.5 ml and 10minutes, respectively.

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 2000.11a
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• pp.83-88
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• 2000

환원공정은 산업 전반에 걸쳐 매우 광범위하게 이용되고 있는 기술로서, 현재 활용되고 있는 환원공정으로 대표적인 것이 일반금속 및 비철금속 등의 열처리 공정이다. 열처리 공정에서의 환원공정은 적용되어지는 제품의 종류에 따라 차이는 있겠으나, 기본적으로는 제품에 적합한 경도 및 조직 구조를 형성하고, 공정 과정 중에 발생할 수 있는 표면 산화를 최소화함으로서 제품의 품질을 향상시키는 역할을 하게 된다. 그러나 기존에 적용되고 있는 이러한 환원공정들은 환원가스의 발생과 에너지원의 공급이 이원화되어 있어 비효율적인 시스템 운영 및 이원화에 따라 공급되어지는 에너지원이 이중적으로 소모될 수 있는 비경제적인 요인을 내포하고 있다. 반면 촉매 연소 방식은 이러한 기존의 단점을 보완, 극복할 수 있는 기술이다.(중략)

• Proceedings of the Korean Radioactive Waste Society Conference
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• 2007.11a
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• pp.43-43
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• 2007

• Clean Technology
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• v.20 no.3
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• pp.212-217
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• 2014

In order to regenerate the sulfidated desulfurization sorbent, oxygen is used as the oxidant agent on the regeneration process. The small amount of oxygen un-reacted in regeneration process is flowed into direct sulfur recovery process. However, the reactivity for $SO_2$ reduction can be deteriorated with the un-reacted oxygen by various reasons. In this study, the deactivation effects of un-reacted oxygen contained in the off-gas of regeneration process flowed into direct sulfur recovery process of hot gas desulfurization system were investigated. Sn-Zr based catalysts were used as the catalyst for $SO_2$ reduction. The contents of $SO_2$ and $O_2$ contained in the regenerator off-gas used as the reactants were fixed to 5.0 vol% and 4.0 vol%, respectively. The catalytic activity tests with a Sn-Zr based catalyst were for $SO_2$ reduction performed at $300-450^{\circ}C$ and 1-20 atm. The un-reacted oxygen oxidized the elemental sulfur produced by $SO_2$ catalytic reduction and the conversion of $SO_2$ was reduced due to the production of $SO_2$. However, the temperature for the oxidation of elemental sulfur increased with increasing pressure in the catalytic reactor. Therefore, it was concluded that the decrease of reactivity at high pressure is occurred by catalytic deactivation, which is the re-oxidation of lattice oxygen vacancy in Sn-Zr based catalyst with the un-reacted oxygen on the catalysis by redox mechanism. Meanwhile the un-reacted oxygen oxidized CO supplied as the reducing agent and the temperature in the catalyst packed bed also increased due to the combustion of CO. It was concluded that the rapidly increasing temperature in the packed bed can induce the catalytic deactivation such as the sintering of active components.

• Proceedings of the Korea Air Pollution Research Association Conference
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• 2002.11a
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• pp.261-262
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• 2002

산업용 보일러나 발전설비와 같은 대규모 고정원에서 다량 배출되는 NOx의 제거를 위한 여러 기술 중에서 현재 암모니아를 환원제로 사용하는 선택적 촉매 환원법(Selective Catalytic Reduction : SCR)이 가장 유망하며, 많은 연구와 더불어 선진국가에서 상업화되어 조업되고 있다. SCR 공정은 시설투자와 운전비가 비교적 저렴하고 높은 NOx 전환율(90%이상)과 폐수처리 등의 후처리 공정이 필요하지 않은 장점이 있다. (중략)

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 1999.11a
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• pp.35-39
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• 1999

현재 NO제거에 주로 사용되는 환원제로서 NH$_3$가 있는데 이는 NO에 대한 선택도가 우수하기 때문이다. 그러나, NH$_3$는 독성이 강하고 부식성이 있어 저장 및 수송에 많은 비용이 든다는 단점이 있다. 따라서 본 연구에서는 SOx/NOx 동시 제거 공정에 효과적으로 알려진 fresh and sulfated CuO/${\gamma}$-A1$_2$O$_3$촉매상에서 독성이 강한 NH$_3$를 대신하는 새로운 환원제로서 urea용액을 이용하여 유동층 반응기에서 SCR을 수행해 보고자 한다.(중략)

• Proceedings of the Korea Air Pollution Research Association Conference
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• 2001.11a
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• pp.425-426
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• 2001

선택적촉매환원(Selective Catalytic Reduciton: SCR)공정은 배기가스 중 질소산화물을 암모니아와 촉매상에서 반응시켜 무해한 질소와 물로 전환하는 기술이다(Bosch, 1988). SCR 공정에서 우수한 촉매가 확보되었을 경우, 설비의 성능은 촉매층로 유입되는 유동의 조건에 따라 좌우되므로 최적의 유동조건을 갖도록 반응기의 구조와 가이드 베인등 유로변경장치를 설계하는 것은 매우 중요하다(Cho, 1994). (중략)

• Nuclear Engineering and Technology
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• v.27 no.4
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• pp.619-625
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• 1995

발전소 계통의 부식의 원인은 여러가지가 있으나 그 중 용존산소에 의한 덴팅이나 점식등은 증기발생기에 심각한 영향을 줄 수 있다. 용존산소를 제거하는 방법은 기계적 방법과 환원제를 사용하는 화학적 방법, 그리고 촉매를 이용하는 방법등이 있는데 이중 촉매를 이용하는 방법이 우수한 것으로 평가되고있다. 본 연구는 촉매탑을 이용하여 용존산소를 제거하는 공정에 있어서 여러가지 촉매를 사용하여 용존산소가 제거되는 것을 실증하였고 각 촉매의 성능을 비교하였다. 그 결과 Lewatit OC-1045 촉매가 가장 우수한 성능을 보였다. 촉매탑 실험시 물질전달 계수를 측정하고 이 값과 촉매탑 모델링을 이용하여 실제 발전소 계통에 부착시켜 응용할 수 있는 촉매탑 설계를 수행하였다.

• Korean Chemical Engineering Research
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• v.44 no.4
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• pp.356-362
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• 2006

The $SO_2$ reduction using CO and $H_2$ over Sn-Zr based catalysts was performed in this study. Sn-Zr based catalysts with Sn/Zr molar ratio (0/1, 1/4, 1/1, 2/1, 3/1, 1/0) were prepared by the precipitation and co-precipitation method. The effect of the temperature on the reaction characteristics of the $SO_2$ reduction with a reducing agent such as $H_2$ and CO was investigated under the conditions of space velocity of $10,000ml/g_{-cat.}h$, $([CO(or\;H_2)]/[SO_2])$ of 2.0. As a result, the activity of Sn-Zr based catalysts were higher than $SnO_2$ and $ZrO_2$. The reactivity for the $SO_2$ reduction with CO was higher than that with $H_2$, and sulfur yield in the $SO_2$ reduction by $H_2$ was higher than that by CO. The reactivity for the $SO_2$ reduction with $H_2$ was increased with the reaction temperature regardless of Sn-Zr based catalyst with a Sn/Zr molar ratio. $SnO_2-ZrO_2$ (Sn/Zr=1/4) had highest activity at $550^{\circ}C$, in the $SO_2$ reduction with $H_2$ and $SO_2$ conversion of 94.4％ and sulfur yield of 66.4％ were obtained at $550^{\circ}C$. On the other hand, in the $SO_2$ reduction by CO, the reactivity was decreased with the increase over $325^{\circ}C$. At the optimal temperature of $325^{\circ}C$, $SO_2$ conversion and sulfur yield were about 100％ and 99.5％, respectively, in the $SO_2$ reduction over $SnO_2-ZrO_2$ (Sn/Zr=3/1). Also, the $SO_2$ reduction using syngas with $CO/H_2$ ratio over $SnO_2-ZrO_2$ (Sn/Zr=2/1) was performed in order to investigate the application possibility of the simulated coal gas as the reductant in DSRP. As a result, the reactivity of the $SO_2$ reduction using syngas with $CO/H_2$ ratio was increased with increasing the CO content of syngas. Therefore, it could be known that DSRP using the simulated coal gas over Sn-Zr based catalyst is possible to be realized in IGCC system

• Journal of the Korea Academia-Industrial cooperation Society
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• v.13 no.11
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• pp.5610-5614
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• 2012

Performance of catalyst was studied with various operating conditions for selective catalytic reduction of $NO_x$ with $NH_3$. It is confirmed that catalysts containing Mn and Cu have a good efficiency in the usage of oxygen by the $H_2$-TPR analysis. In the case of catalyst #1, $NO_x$ conversion was decrease with the increase of reaction temperature. But in the case of catalyst #2, $NO_x$ conversion was increased and then remained constant with the increase of reaction temperature. This phenomenon is due to the difference of the $NH_3$ oxidation of both catalysts.