• Title/Summary/Keyword: 촉매 표면 반응

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A Study on the Sulfur-Resistant Catalysts for Water Gas Shift Reaction II. Effect of Alkali Metal Salt on the Activity of CoMo Catalyst (황에 저항성을 가지는 수성가스 전환반응 촉매의 연구 II. CoMo 촉매의 활성에 미치는 알칼리 금속염의 영향)

  • Kim, Joon Hee;Lee, Ho In
    • Journal of the Korean Chemical Society
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    • v.42 no.6
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    • pp.696-702
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    • 1998
  • The effect of alkali metal salt on the activity of Co-Mo catalyst which has high resistance to sulfur poisoning for water gas shift reaction(WGSR) was studied. Two groups of catalysts were prepared to investigate the effects of anion and cation in alkali metal salts. For K-doped catalysts made with various potassium salts having different anion, the catalytic activity was explained to depend mainly on the BET surface area. Among the catalysts prepared by various nitrates of alkali metal as precursor, the Li-doped catalyst showed the best activity, and the others did not make significant differences giving relatively low activities. And the change of BET surface area by varying the loading of alkali metal showed a similar trend to that of activity. In this case, the activity was dependent on both BET surface area and the ratio of $Mo^{6+}$ with a tetrahedral coordination symmetry to $Mo^{6+}$ with an octahedral one, $Mo^6+[T]/Mo^{6+}[O]$ value.

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Electrocatalytic Activity of Dendritic Platinum Structures Electrodeposited on ITO Electrode Surfaces (전기화학적 석출을 통해 ITO 표면에 형성한 덴드라이트 백금 구조의 전기화학적 촉매 활성)

  • Choi, Suhee;Choi, Kang-Hee;Kim, Jongwon
    • Journal of the Korean Electrochemical Society
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    • v.17 no.4
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    • pp.209-215
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    • 2014
  • We report on the electrocatalytic activities at Pt nanostructure surfaces electrodeposited with different deposition charges on indium tin oxide electrodes for oxygen reduction and methanol oxidation reactions. The surface properties of Pt nanostructures depending on deposition charges were characterized by scanning electron microscopy, electrochemical surface area measurement, X-ray diffraction, and CO stripping analysis, which were correlated to the electrocatalytic activities. Pt nanostructures with deposition charge of 0.03 C exhibited the highest electrocatalytic activity for oxygen reduction and methanol oxidation. The sharp sites of Pt nanostructure and the presence of highly active facet play a key role, whereas the electrochemical surface area does not significantly affect the electrocatalytic activity. The results obtained in this work with regard to the dependence of electrocatalytic activity on the variation of the Pt nanostructures will give insights into the development of advanced electrocatalytic systems.

Hydrogen production by catalytic decomposition of propane over carbon black catalyst in a fluidized bed (유동층 반응기에서 카본블랙 촉매를 이용하는 프로판 분해에 의한 수소 생산)

  • Yoon, Yong-Hee;Lee, Seung-Chul;Han, Gui-Young
    • 한국신재생에너지학회:학술대회논문집
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    • 2007.11a
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    • pp.109-112
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    • 2007
  • 유동층 반응기를 이용한 프로판의 촉매 분해는 $CO_2$를 방출하지 않고 수소를 생성하는 새로운 방식이다. 카본블랙을 이용한 프로판 분해는 메탄보다 상대적으로 분해가 잘되며, 같은 온도에서 전환률이 높기 때문에 수소 생성량이 더 많다. 촉매로 사용된 카본블랙은 반응 중 생성되는 탄소의 침적에도 불구하고 8시간 이상 촉매의 활성이 유지되어 전환율이 일정하게 유지되었다. 프로판 촉매 분해 실험은 상압에서 600 ${\sim}$ $800^{\circ}C$ 온도 변화 실험을 수행하였고, 가스 유속 변화는 2.0 ${\sim}$ $4.0U_mf$에서 실험 조건 변화에 따른 실험을 하였다. 온도, 유속 변화에 따른 생성 가스의 몰분율과 프로판 전환율을 분석하였다. 프로판 분해에 의해 생성된 기체는 수소뿐만 아니라 메탄, 에틸렌, 에탄, 프로필렌과 분해되지 않은 프로판이 배출되었다. 수소를 제외한 여타 가스들은 고온에서 실험을 할수록 몰비가 줄어들었다. 고온에서 프로판의 전환율과 수소 수득률이 증가하였다. 프로판 분해 실험 전후의 카본블랙 표면의 변화는 FE-TEM으로 관측하였다.

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Supported Metal Oxides for Continuous Cat-alytic Wet Oxidation of TCE

  • 김문현;추광호
    • Proceedings of the Korean Environmental Sciences Society Conference
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    • 2004.05a
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    • pp.40-45
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    • 2004
  • 액상 TCE 제거반응을 위한 Hetero-CWO 촉매들 중에서 $CoO_{x}$/$TiO_2$$CuO_{x}$/$TiO_2$가 상대적으로 유망한 것으로 보여졌으며, 특히 5% $CoO_{x}$/$TiO_2$ 촉매의 경우에 반응시간에 따른 활성추이는 TCE 제거반응에서 주요 역할을 할 수 있는 반응 활성점의 변화를 암시하고 있다. $FeO_{x}$ /$TiO_2$와 Fe-MFI 촉매상에서 TCE 제거반응에 대한 시간에 따른 활성거동으로부터 활성점의 redox cycle를 어떻게 제어하는가 하는 점이 매우 중요함을 알 수 있었으며, 촉매표면에서 이를 유지.증진시킬 수 있는 촉매 디자인 기법이 요구되었다.

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The Effects of Cr-Substitution in Ferrite Catalysts and the Catalytic Dehydrogenation of Ethylbenzene (페라이트 촉매의 Cr 치환효과와 에틸벤젠의 탈수소반응)

  • Lim, Ki-Chul;Kim, Eul-San;Lee, Ho-In
    • Applied Chemistry for Engineering
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    • v.2 no.3
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    • pp.279-288
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    • 1991
  • Mg- and Zn-ferrites having spinel structure, a kind of complex oxides showing the advantageous properties of constituent single metal oxides, were selected to find a relationship between their catalytic activities in the dehydrogenation of ethylbenzene to styrene and the catalytic properties. For the structural and physical analyses of ferrites, XRD, BET, TG/DTA, ESCA, TEM, and TPD methods were employed. The effects of Cr-substitution were intensively studied by the experimental methods mentioned above. Chromium which showed a preferential tendency to diffuse to the surface acted as a structural promoter by increasing surface area and stability of catalyst structure. In the dehydrogenation of ethylbenzene, catalytic activity, and the effects of Cr-substitution were investigated. Oxygen mobility was decreased with the amount of Cr-substitution in $MgCr_xFe_{2-x}O_4$, which resulted in the increase of selectivity to styrene and the suppression of total oxidation.

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Toluene Oxidation over Spent Zeolite Catalyst (폐제올라이트 촉매를 이용한 톨루엔 산화반응)

  • Song, Min-Young;Park, Young-Kwon;Park, Sung-Hoon;Jeon, Jong-Ki;Ko, Young-Soo;Jung, Kyeong-Youl;Yim, Jin-Heong;Sohn, Jung-Min
    • Clean Technology
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    • v.14 no.4
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    • pp.271-274
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    • 2008
  • In this work, the feasibility of spent zeolite catalyst for reusing as a support was investigated in catalytic odor removal reaction. As a model reaction for odor removal, toluene was selected as a reactant. 10wt% Cu was impregnated on spent HZSM-5 catalyst and spent FCC catalyst. The catalytic activity of the spent HZSM-S was higher than that of spent FCC catalyst in toluene oxidation. This was due to the fact that the surface area of spent HZSM-S was higher than that of spent FCC catalyst. These results may suggest that spent HZSM-S can be reused as a cheap catalyst for toluene removal.

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Metal Catalyst Encapsulated in Nitrogen-doped Carbon Shell for Fuel Cell Application: Theoretical and Experimental Study (연료전지용 질소 도핑 탄소촉매의 표면 반응에 관한 이론적 연구와 실험적 입증)

  • No, Seung-Hyo;Seo, Min-Ho;Gang, Jun-Hui;;Han, Byeong-Chan
    • Proceedings of the Korean Institute of Surface Engineering Conference
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    • 2017.05a
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    • pp.86-86
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    • 2017
  • 고효율의 에너지 변환 및 친환경적인 이점들을 이유로, 고분자전해질 연료전지(PEMFC)는 차세대 에너지 장치로 이목을 끌어왔다. 반면, 값비싼 백금 촉매의 이용은 연료전지의 상업적 이용에 주요한 결점으로 작용했다. 최근, Zelenay와 연구팀은 폴리아닐린-철-탄소 복합체구조에서 산소환원활성이 백금과 견주어 비슷한 성능을 낼 수 있음을 보고 하였다. Dodelet은 이러한 높은 성능이 전이금속의 영향에 의한 것일 수 있다는 주장을 하였다. 본 연구팀은 지난 연구에서 제일원리전산모사를 통해 니켈, 코발트, 구리등과 같은 전이금속이 질소가 도핑된 탄소 그래핀층에 미치는 거동을 밝혔다. 결론적으로, 금속들은 질소가 도핑된 그래핀의 전자구조를 바꿀 수 있고, 이러한 전자구조의 변화는 산소 환원반응에서 긍정적으로 작용할 수 있음을 확인하였다. 이러한 이론적 연구에 기반하여, 탄소층으로 감싼 금속은 내구성과 활성을 동시에 보유한 향후 전망있는 촉매 물질로 예상되어진다. 특히, 질소가 도핑된 탄소층으로 코팅된 철-코발트 합금은 계산을 통해 산소환원반응에서 우수할 것으로 예측되었다. 본 연구팀은 FeCo@N-C 나노입자를 직접 합성하였고, 이 촉매의 우수한 활성을 전기화학적, 구조적 관점에서 1) 질소의 도핑 효과, 2) 탄소의 두께 효과, 3) 합금효과에 집중하여 분석하였다.

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The novel methods for doping of Ru oxide on TiO2 nanotubes thin-film on Ti substrate by electrochemical anodization (타이타늄 나노튜브 박막 상의 루테늄 산화물의 전기화학적 도핑 방법)

  • Yu, Hyeon-Seok;O, Gi-Seok;Choe, Jin-Seop
    • Proceedings of the Korean Institute of Surface Engineering Conference
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    • 2015.11a
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    • pp.235-236
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    • 2015
  • $TiO_2$는 표면적이 넓고 안정성이 높아 자체의 높은 밴드갭(3.0~3.2 eV)에도 불구하고 산업적으로 염소분해 전극으로써 사용되며, 최근 물분해 전극 적용 연구가 진행되고 있다. 전기화학적 물분해 반응을 위해서는 높은 과전압이 요구되므로 산업적으로 이용하기 위해 전도성을 향상시키기 위한 연구가 필요하다. 이러한 문제를 해결하기 위해 촉매제의 도핑이 연구되고 있으며 본 연구에서는 표면에 촉매를 도핑시키기 위한 두가지 방법을 연구하였다. 일반적으로 촉매로 사용되는 금속은 루테늄과 이리듐 등의 귀금속이며 촉매가 균일하게 도핑이 될수록 성능은 향상된다. 본 연구에서는 루테늄을 촉매로 선택하였으며 서로 다른 도핑 방법과 용매 하에서 물분해 실험을 진행하여 두 가지 방법의 물분해 효율을 비교하였다.

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NO Adsorption and Catalytic Reduction Mechanism of Electrolytically Copper-plated Activated Carbon Fibers (전해 구리 도금된 활성탄소섬유에 의한 NO의 촉매 환원반응 메커니즘 연구)

  • Park, Soo-Jin;Jang, Yu-Sin;Kawasaki, Junjiro
    • Korean Chemical Engineering Research
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    • v.40 no.6
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    • pp.664-668
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    • 2002
  • In this work, the catalytic reduction mechanisms of NO over ACFs/copper prepared by electrolytic copper plating has been studied. It was found that copper content on carbon surfaces increased with increasing the plating time. However, a slightly gradual decrease of adsorption properties, such as, BET specific surface area, was observed in increasing the plating times within the range of well-developed micropore structures. As experimental results, nitric oxide was converted into the nitrogen and oxygen on ACFs and ACFs/copper catalyst surfaces at $500^{\circ}C$. Especially, the surfaces of ACFs/copper catalyst were found to scavenge the oxygen released by catalytic reduction of NO, which could be explained by the presence of another nitric oxide reduction mechanism between ACFs and ACFs/copper catalysts.

Kinetics of Catalytic Oxidation of Vinyl Chloride over CrOx/γ-alumina (CrOx/γ-alumina 촉매상에서 Vinyl Chloride의 산화반응 속도해석)

  • Lee, Hae-Wan;Kim, Young Chai;Moon, Sei-Ki
    • Applied Chemistry for Engineering
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    • v.10 no.1
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    • pp.85-92
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    • 1999
  • The complete catalytic oxidation of vinyl chloride was investigated over chromium oxide supported ${\gamma}$-alumina using a fixed bed micro-reactor at temperature between 240 and $300^{\circ}C$ and concentration between 600 and 3500 ppm. The oxidation of vinyl chloride was nonlinear in the concentration of vinyl chloride and zeroth order in the concentration of oxygen. The addition of HCl and $H_2O$ as products to the feed stream didn't influence the conversion of vinyl chloride. Several kinetic rate model were tested to describe the data over the range of condition investigated, and developed a model which provide the best correlation of experimental data. The resulting model of kinetic rate was derived by assuming that the reacting occurred via adsorption and subsequent decomposition of the vinyl chloride onto the oxygen covered chromium oxide surface, with the reaction being inhibited by the adsorption of vinyl chloride. The percent standard deviation between the predicted and experimental was about 5.2%, and the activation energy was 18.9 kcal/mol.

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