• 제목/요약/키워드: Co-incipient wetness method

검색결과 17건 처리시간 0.019초

일단 WGS반응용 백금 담지 촉매 최적화 (Optimization of Supported Pt Catalysts for Single Stage Water Gas Shift Reaction)

  • 김기선;정대운;구기영;윤왕래;노현석
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2011년도 춘계학술대회 초록집
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    • pp.156.2-156.2
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    • 2011
  • 본 연구에서는 일단 수성가스전이반응 (Single stage water gas shift reaction)을 위해 높은 활성을 가진 백금 담지 촉매를 함침법 (Incipient wetness impregnation method)으로 제조하여 높은 공간 속도 (Gas hourly space velocity) $45,515h^{-1}$에서 담체에 따른 촉매 활성을 평가하였다. 담체는 $CeO_2$, $ZrO_2$, MgO, MgO-$Al_2O_3$ (MgO = 30 wt%) 그리고 $Al_2O_3$를 사용하였으며 백금의 담지량은 1 wt%로 고정하였다. BET, XRD, TPR, CO-chemisorption 분석을 통하여 담체의 구조적 특성이 촉매 활성에 미치는 영향에 대하여 조사하였다.

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WGS 반응용 Pt-Na/$CeO_2$촉매의 Na 담지량에 따른 성능 평가 (Evaluation in Activity of Pt-Na/$CeO_2$ Catalysts for One-Step Water Gas Shift Reaction via Controlling the Amount of Na Addition)

  • 엄익환;김기선;정대운;이성훈;구기영;윤왕래;노현석
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2010년도 춘계학술대회 초록집
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    • pp.230.1-230.1
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    • 2010
  • 조촉매(Promotor)인 Na은 수성가스전이(Water Gas Shift, WGS) 반응 시 생성된 포름산염의 C-H결합을 쉽게 분해하는 역할을 한다. 본 연구에서는 $Pt/CeO_2$ 촉매의 성능 향상을 위해 Na의 담지량을 변화시켜 촉매적 활성을 비교하여 보았다. 제조된 담체는 침전법(Precipitation)을 사용하여 제조하였으며 $500^{\circ}C$에서 6시간 소성하였다. Pt 담지량은 1wt%로 고정하였고 Na 담지량은 1 wt%~5 wt%로 변화를 주어 동시(공)-함침법(Co-incipient wetness method)으로 담지 시켰다. 반응 실험은 공간속도(Gas Hourly Space Velocity, GHSV) $45,385h^{-1}$에서 수행하였다. WGS 반응 결과 3 wt%의 Na이 담지된 $Pt/CeO_2$ 촉매의 경우를 제외하고 나머지 Na이 담지된 촉매들은 비교적 높은 CO의 전환율을 나타내었다. 특히 2 wt%의 Na이 담지된 $Pt/CeO_2$ 촉매는 가장 높은 CO의 전환율을 나타내었다. 따라서 Na 담지량의 변화가 포름산염의 C-H결합 분해에 영향을 미친다는 것을 알 수 있다.

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Photoacoustic Spectroscopic Study on Cobalt Incorporation onto the Surface of Mesoporous Molecular Sieves

  • 박동호;박성수;최상준
    • Bulletin of the Korean Chemical Society
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    • 제20권6호
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    • pp.715-719
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    • 1999
  • The incorporation of cobalt into mesoporous molecular sieves MCM-41 and MCM-48 was carried out. Co-PO/MCM41 and Co-PO/MCM48 were prepared using Co(II) acetate solution adjusted to pH = 3.0 with phosphoric acid by the incipient wetness method. Photoacoustic spectroscopy (PAS) was used to study the local environments of Co(II) incorporated into mesopores. The band around 500 nm in PAS of as-prepared Co-PO/MCM41 and Co-PO/MCM48 with Co(II) acetate solution was changed to triplet bands around 600 nm. This could be assigned to the 4 A2(F)-> 4T1(P) transition of Co(II) surrounded tetrahedrally by oxygen ions after calcination. It may be attributable to that the octahedral cobalt species containing phosphate ligands in coordination sphere reacting with framework's silanol groups to be dispersed atomically onto the surface of mesoporous molecular sieves as a tetrahedral species. This is unlike that the Co in Co-Cl/MCM41 and direct-synthesized Co-MCM41 transforms to Co oxide phase upon calcination. Co-PO/MCM41 and Co-PO/MCM48 were stable while treated with water.

Low Temperature Catalytic Activity of Cobalt Oxide for the Emergency Escape Mask Cartridge

  • Park, Jae-Man;Kim, Deog-Ki;Shin, Chang-Sub
    • International Journal of Safety
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    • 제1권1호
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    • pp.58-61
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    • 2002
  • A preparation method of cobalt supported alumina catalyst for a emergency escape mask cartridge has been studied. Catalysts were prepared by incipient wetness impregnation method using pre-shaped $\gamma$=alumina powders of 70-100 mesh. The catalyst was tested in a continuous-flow reactor system and characterized by elemental analysis, BET and TGA-DTA techniques. Cobalt shows higher activity than platinum or nickel for carbon monoxide oxidation at room temperature. Optimum loading amount of cobalt was 10 wt.% for CO oxidation and the reaction activity increases gradually with the increase of calcination temperature up to $450^{\circ}C.

The Effect of K Promoter on Ni-Co (Bimetallic) Catalyst for Dry Methane Reforming

  • Dharmasaroja, Nichthima;Phongaksorn, Monrudee;Tungkamani, Sabaithip;Ratana, Tanakorn;Sornchammi, Thana
    • International Journal of Advanced Culture Technology
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    • 제3권2호
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    • pp.110-117
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    • 2015
  • 10 wt% (Ni-Co) catalysts with different Ni and Co content : 10%Ni, 9%Ni1%Co, 7%Ni3%Co, 5%Ni5%Co, 3%Ni7%Co, and 10%Co; were prepared using sol-gel method followed by incipient wetness impregnation method. To investigate the catalytic activity including the stability, dry methane reforming were demonstrated over the pelletized catalysts at $620^{\circ}C$ under atmospheric pressure in a $CH_4:CO_2:N_2$ feedstock for 360 min. The results showed that bimetallic catalysts with the Co content equal to or greater than 3% were more stable than monometallic catalysts (10%Ni and 10%Co). The temperature programmed hydrogenation interpreted that the additional of Co into Ni catalyst improved the carbon resistance from methane cracking. Promoted this type of bimetallic catalyst using 1wt% K (trimetallic catalyst) prevented the carbon formation on the catalyst. The temperature programmed desorption of $CO_2$ indicated that this trimetallic catalyst has a greater number of strong basic sites. Moreover, the appearance of K lowered the number of weak basic sites and decreased the conversion of methane by 12 %.

저급탄화수소 수증기 개질에 의한 수소 제조용 니켈계 촉매개발 (Development of Ni-based Catalyst for Hydrogen Production with Steam Reforming of Light Hydrocarbon)

  • 김대현;이상득;이병권;김명준;홍석인;문동주
    • 신재생에너지
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    • 제4권4호
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    • pp.80-87
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    • 2008
  • Steam reforming of LPG was investigated over spc-Ni/MgAl catalyst in a temperature range of $600{\sim}850^{\circ}C$, feed molar ratio of $H_2O/C=1.0{\sim}3.0$, space velocity of $10,000{\sim}90,000h^{-1}$ and at atmospheric pressure. spc-Ni/MgAl catalyst was prepared by a co-precipitation method, whereas Ni/MgO and $Ni/Al_2O_3$ catalysts were prepared by an incipient wetness method. The characteristics of catalysts were analyzed by N2 Physisorption, CO chemisorption, XRD, TOF-SIMS, SEM and TEM techniques. The Ni/MgO and $Ni/Al_2O_3$ catalysts were deactivated by the formation of carbon. However, the spc-Ni/MgAl catalyst showed higher conversion and $H_2$ selectivity than the other catalysts, even though carbon was formed on the surface of the catalyst during the reaction under the tested reaction conditions.

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촉매 제조방법에 따른 Co-CeO2 촉매의 N2O 분해 특성 연구 (Effect of the Preparation Method on the Activity of CeO2-promoted Co3O4 Catalysts for N2O Decomposition)

  • 김혜정;김민재;이승재;유인수;이광복;전상구
    • 청정기술
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    • 제24권3호
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    • pp.198-205
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    • 2018
  • 본 연구는 $Co-CeO_2$ 촉매의 $N_2O$ 분해 반응에서 촉매의 제조 방법이 활성에 미치는 영향을 고찰하였다. $Co-CeO_2$ 촉매는 공침법(Co-precipitation)과 함침법(Incipient wetness impregnation)으로 제조하였다. 제조된 촉매의 성능을 평가하기 위하여 $N_2O$ 직접 촉매 분해(Direct catalytic $N_2O$ decomposition) 반응을 $250{\sim}375^{\circ}C$에서 실시하였다. 그 결과 공침법으로 제조된 촉매(CoCe-CP)는 $O_2$ 및/또는 $H_2O$의 존재 하에서도 $N_2O$ 분해 반응에서 향상된 성능을 보인 반면에 함침법으로 제조된 촉매(CoCe-IM)는 그렇지 못하였다. 이러한 촉매 활성의 차이를 조사하기 위하여 XRD, BET, TEM, $H_2-TPR$, $O_2-TPD$ 그리고 XPS와 같은 촉매 특성 분석들을 진행하였다. 촉매의 제조 방법에 따라서 입자의 크기 및 표면적이 변화하는 것을 확인하였고 합성 과정이 촉매의 물리적 특성에 영향을 미치는 것을 알 수 있었다. 공침법으로 제조된 촉매의 활성 증가는 $Co^{3+}{\rightarrow}Co^{2+}$의 향상된 환원 특성 및 산소 탈착 속도 향상에 기인한 것으로 여겨진다. 하지만, $N_2O$ 분해와 관련이 있는 촉매의 표면 전하 상태 및 결합에너지는 제조 방법에 따라서 변하지 않는 것을 확인하였다.

Ce가 첨가된 Pt/γ-Al2O3 촉매의 선택적 CO 산화반응 특성 (Preferential CO Oxidation over Ce-Promoted Pt/γ-Al2O3 Catalyst)

  • 김기혁;구기영;정운호;윤왕래
    • 한국수소및신에너지학회논문집
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    • 제23권6호
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    • pp.640-646
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    • 2012
  • The effect of Ce promotion over 1wt% $Pt/{\gamma}-Al_2O_3$ catalysts on the CO conversion and $CO_2$ selectivity was investigated in preferential CO oxidation (PrOx) to reduce the CO concentration less than 10 ppm in excess $H_2$ stream for polymer electrolyte membrane fuel cell (PEMFC). Ce-promoted 1wt% $Pt/{\gamma}-Al_2O_3$ catalysts were prepared by incipient wetness impregnation method and the loading amount of Pt was fixed at 1wt%. The content of Ce promoter which has excellent oxygen storage and transfer capability due to the redox property was adjusted from 0 to 1.5wt%. Ce-promoted 1wt% $Pt/{\gamma}-Al_2O_3$ catalysts exhibit high CO conversion and $CO_2$ selectivity at low temperatures below $150^{\circ}C$ due to the improvement of reducibility of surface PtOx species compared with the 1wt% $Pt/{\gamma}-Al_2O_3$ catalyst without Ce addition. When Ce content was more than 1wt%, the catalytic activity was decreased at over $160^{\circ}C$ in PrOx because of competitive $H_2$ oxidation. As a result, 0.5wt% Ce is optimal content not only to achieve high catalytic activity and good stability at low temperatures below $150^{\circ}C$ in the presence of $CO_2$ and $H_2O$ but also to minimize the $H_2$ oxidation at high temperatures.

알루미나에 담지된 Rh 함유 촉매의 n-옥탄 부분산화반응 (Partial Oxidation of n-Octane over Rh-Containing Alumina-Supported Catalysts)

  • 이신화;서영웅;서동진;박태진;이관영
    • 한국수소및신에너지학회논문집
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    • 제19권1호
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    • pp.10-17
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    • 2008
  • This study has been focused on the partial oxidation(POX) of n-octane over Rh-containing catalysts supported on alumina. The catalysts for this reaction were prepared by incipient wetness(IW) and co-gel(CG) methods, followed by the calcination at $900{\circ}C$ or $1,200{\circ}C$. When applied to the POX of n-octane carried out at $600{\circ}C$ with C/O=3 and GHSV=3,450/h, the catalyst prepared by the CG method and calcined at $1,200{\circ}C$ showed the best activity, yielding 42% syngas($H_2$+CO) with the $H_2$/CO ratio of $2{\sim}2.4$. To enhance the activity and stability of catalysts, bimetallic catalysts were synthesized by the CG method. As a result, the performance of Rh-Ni/$Al_2O_3$ catalyst was superior to that of Rh/$Al_2O_3$ catalyst in terms of the catalyst stability, due to the retarding effect on the Rh-to-$Rh_2O_3$ transition by the addition of Ni. This result was confirmed by XRD, TEM, and TPR characterizations.

금속-세라믹 Core-Shell CoAl2O4@Al 구조체를 적용한 불균일계 촉매의 글리세롤 수소전환 반응특성 (Glycerol Steam Reforming for Hydrogen Production on Metal-ceramic Core-shell CoAl2O4@Al Composite Structures)

  • 김지은;이두환
    • 청정기술
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    • 제21권1호
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    • pp.68-75
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    • 2015
  • 본 연구에서는 높은 열전도성을 갖는 금속-세라믹 core-shell 구조의 CoAl2O4@Al 복합체를 Al 금속의 수열반응을 통하여 합성하고, 이를 Rh 촉매의 담지체로 적용하여 구조적, 촉매화학적 특성을 분석하였다. Rh/CoAl2O4@Al (3 wt% Rh) 촉매는 단순침적법(incipient wetness impregnation)으로 제조하였고, 특성의 비교평가를 위하여 공침법(co-precipitation)으로 합성한 CoAl2O4를 담지체로 하여 Rh/CoAl2O4 (3 wt% Rh) 촉매를 단순침적법으로 제조하였다. 이들 촉매들은 N2 흡착, XRD, 전자 주사현미경, temperature programmed reduction (TPR), CO 화학흡착 분석을 통해서 그 특성을 분석하였고, 글리세롤 수증기 개질 반응(550 ℃)을 통한 수소전환반응에 적용하여 촉매적 특성을 평가하고 분석하였다. 글리세롤 수증기 개질반응에 대하여 Rh/CoAl2O4@Al 촉매는 Rh/CoAl2O4 촉매에 비하여 약 2.8배 높은 글리세롤 전환 turnover frequency (TOF)를 보여주었고, 이는 높은 열전도성을 갖는 금속-세라믹 복합체를 통한 원활한 반응열의 전달에 기인한 것으로 분석되었다. CoAl2O4@Al 및 CoAl2O4 담지체에서도 환원에 의하여 노출된 일부 Co 금속에 의한 촉매적 활성이 관찰되었는데, Rh/CoAl2O4@Al과 Rh/CoAl2O4 촉매에서와 마찬가지로 core-shell 구조체인 CoAl2O4@Al이 CoAl2O4 보다 높은 촉매적 활성을 보였다. 그러나, 이들 촉매는 글리세롤 개질반응에서 비교적 높은 비활성화를 보여주었고 이는 촉매표면의 탄소침적(coking)에 기인한 것으로 판명되었다.