• 전기화학회지
• /
• 제7권4호
• /
• pp.201-205
• /
• 2004

본 연구에서는 Pt-Ru 촉매를 $H_2PtCI_6$ 및 $RuCl_3$ 용액을 화학적 환원에 의해 전도성 고분자인 폴리피롤을 중합시킨 Nafion 막위에 직접 침적시켰다 EDS 분석 결과 Pt 및 Ru 촉매는 Ppy/Nafion 표면에 주로 분포하는 것을 알 수 있었다. 또한 폴리피롤이 중합된 Nanon 위에 침적시킨 Pt-Ru 촉매의 메탄올에 대한 전기화학적 산화특성을 CV로 평가하였다. 메탄을 산화 개시 전위는 Ru촉매에 사용이 증가함에 따라 음전위 방향으로 전이되었다. 따라서 폴리피롤이 중합된 Nafion표면에 Pt-Ru촉매를 직접 함침할 수 있었고. 메탄올 산화 특성을 나타내는 전극을 제작할 수 있었다.

• Korean Chemical Engineering Research
• /
• 제45권4호
• /
• pp.328-334
• /
• 2007

2-propanol/acetone/hydrogen 계 화학반응 열펌프 시스템은 발전소의 폐열 등을 이용하기 위한 가장 적합한 반응계로 알려져 있다. 솔-젤법을 이용하여 2-propanol 탈수소화 반응용 5 wt% Pt-alumina 촉매를 다양한 형태로 제조하여 각각의 특성을 알아보았고 각각의 반응성을 비교하였다. Pt-alumina xerogel 촉매는 기존의 담지촉매보다 우수한 반응성을 보였으며 또한 지속성도 우수한 것으로 나타났다. 또한, Pt-alumina aerogel 촉매가 반응속도 면에서 가장 우수한 결과를 보였다. Aerogel 촉매의 지속성을 유지시키기 위해서는 충분한 시간의 숙성과정이 필요한 것으로 나타났으며 이 과정을 통해서 높은 반응성은 물론 안정적인 지속성도 얻을 수 있었다. Pt-alumina aerogel 촉매의 가장 큰 특징은 높은 반응성은 물론, 일반적으로 반응전에 필수적으로 거쳐야하는 고온의 열처리가 전혀 필요 없다는 것으로서 이는 경제적으로 큰 이점을 가진다. 또한 alumina xerogel에 초기함침법으로 Pt를 담지시킨 촉매는 기계적 강도 및 반응성 면에서 우수한 성능을 보였으며 이를 통하여 alumina xerogel은 금속촉매의 지지체로서도 이용할 수 있다는 사실을 알 수 있었다.

• 공업화학
• /
• 제30권6호
• /
• pp.731-736
• /
• 2019

본 연구에서는 Pt/TiO₂를 파우더 및 허니컴 형태로 제조하고, 촉매의 피독 물질인 SO₂에 대한 영향과 재생 방안을 연구하였다. 이에 따라 Pt/TiO₂의 SO₂ 노출 전·후 촉매 활성을 비교하였다. Pt/TiO₂의 초기 활성은 주입되는 H₂ 농도(1~5%)에 비례하며, 촉매의 온도와 H₂ 전환율이 각각 최대 183 ℃와 95%로 나타났다. 2,800 ppm SO₂를 파우더 및 허니컴 Pt/TiO₂에 노출시켰고, 이때 성능이 나타나지 않았고 촉매 표면에 0.69%의 황(S)이 잔류함을 확인하였다. 피독 촉매에 대한 세척 및 열처리 결과, 파우더 촉매는 세척에 의해 96% 이상의 H₂ 전환율을 나타냈고 허니컴 촉매는 H₂ 또는 air 분위기의 열처리를 통해 촉매 활성이 재생되어 95% 이상의 H₂ 전환율이 확인되었다.

• 한국수소및신에너지학회논문집
• /
• 제19권6호
• /
• pp.467-473
• /
• 2008

This study is to investigate the influence of catalyst loading quantity on the direct methanol fuel cell (DMFC) performance. In this paper, Pt-Ru and Pt-black loading as the catalyst were varied from 1 to $4mg/cm^2$ at the anode and cathode, respectively. The experiment was conducted with single fuel cell consisted of $5cm^2$ effective electrode area, serpentine type flow pattern and Nafion 117 membrane. Also, AC impedance and methanol crossover current were measured to investigate the performance loss precisely. As a result, the performance of fuel cell was significantly increased with the increase of cathode catalyst loading. However, the performance did not increase further above a certain Pt-Ru catalyst loading as the increase of anode catalyst loading.

• Korean Chemical Engineering Research
• /
• 제46권4호
• /
• pp.806-812
• /
• 2008

귀금속촉매 존재하에서 암모니아 전환반응은 배가스내의 암모니아를 처리하는데 중요한 기술이다. 과잉용액 함침법을 이용하여 $Pt-Rh/Al_2O_3$, $Pt-Rh/TiO_2$, $Pt-Rh/ZrO_2$, $Pt-Pd/Al_2O_3$, $Pd-Rh/Al_2O_3$, $Pd-Rh/TiO_2$, $Pd-Rh/ZrO_2$, $Pt-Pd-Rh/Al_2O_3$, $Pd/Ga-Al_2O_3$, $Rh/Ga-Al_2O_3$, 그리고 $Ru/Ga-Al_2O_3$의 촉매를 제조하였다. 제조된 촉매는 1/4"의 반응기에 $10,000{\sim}50,000hr^{-1}$의 공간속도 조건하에서 촉매활성능 실험을 수행하였다. 암모니아의 초기농도는 2,000 ppm (나머지는 공기)으로 유지하였다. $T_{50}$는 암모니아 전환율이 50%일 때를 나타내는 온도를, $T_{90}$은 90%의 전환율일 때의 온도를 나타낸다. 알루미나를 담지체로 사용했을때의 $T_{50}$와 $T_{90}$은 다른 담체를 사용했을때의 $T_{50}$와 $T_{90}$보다 훨씬 낮았다. Pd-Rh촉매의 경우 $Al_2O_3$를 담체로 사용하였을 때 $ZrO_2$나 $TiO_2$보다 저온 활성이 우수하게 나타났다. 황산화물의 피독실험 결과 본 연구에서는 최종적으로 $Pt-Rh/Al_2O_3$ 촉매가 다른 촉매에 비하여 우수함을 보였다. 실험결과 Pt-Rh가 암모니아 전환공정에서 유용한 촉매라는 사실을 알 수 있다.

• 한국신재생에너지학회:학술대회논문집
• /
• 한국신재생에너지학회 2006년도 추계학술대회
• /
• pp.443-446
• /
• 2006

Carbon-supported Platinum (Pt) is the potential electro-catalyst material for anodic and cathodic reactions in fuel cell. Catalytic activity of the metal strongly depends on the particle shape, size and distribution of the metal in the porous supportive network. Conventional preparation techniques based on wet impregnation and chemical reduction of the metal precursors often do not provide adequate control of particle size and shape. We have proposed a novel route for preparing nano sized Pt colloidal particles in solution by oxidation of ethylene glycol. These Pt nano particles were deposited on large surface area carbon support. The process of nano Pt colloid formation involves the oxidation of solvent ethylene glycol to mainly glycolic acid and the presence of its anion glycolate depends on the solution pH. In the process of colloidal Pt formation glycolate actsas stabilizer for the Pt colloidal particle and prevents the agglomeration of colloidal Pt particles. These mono disperse Pt particles in carbon support are found uniformly distributed in nearly spherical shape and the size distribution was narrow for both supported and unsupported metals. The average diameter of the Pt nano particle was controlled in the range off to 3 nm by optimizing reaction parameters. Transmission electron microscopy, CV and RRDE experiments were used to compliment the results.

• 한국재료학회지
• /
• 제18권8호
• /
• pp.401-405
• /
• 2008

Pt-loaded carbon black for the catalyst of a PEM fuel cell was synthesized with different molar ratios of polyvinylpyrrolidone and $H_2PtCl_6$ solution to improve the dispersion of Pt nanoparticles on carbon black and decrease the size of Pt nanoparticles. From transmission electron microscopy results, Pt nanoparticles of a size of approximately 2 nm were highly dispersed when the polyvinylpyrrolidone concentration was 10mM. The electrochemical activity of the synthesized Pt/C catalysts was investigated by cyclic voltammetry, showing that the as-synthesized Pt-loaded carbon black catalyst had the best activity at a polyvinylpyrrolidone concentration of 10 mM.

• Bulletin of the Korean Chemical Society
• /
• 제31권6호
• /
• pp.1577-1582
• /
• 2010

A 20 wt % Pt/C is fabricated and characterized for use as the cathode catalyst in a polymer electrolyte membrane fuel cell (PEMFC). By using the polyol method, the fabrication process is optimized by modifying the carbon addition sequence and precursor mixing conditions. The crystallographic structure, particle size, dispersion, and activity toward oxygen reduction of the as-prepared catalysts are compared with those of commercial Pt/C catalysts. The most effective catalyst is obtained by ultrasonic treatment of ethylene glycol-carbon mixture and immediate mixing of this mixture with a Pt precursor at the beginning of the synthesis. The catalyst exhibits very uniform particle size distribution without agglomeration. The mass activities of the as-prepared catalyst are 13.4 mA/$mg_{Pt}$ and 51.0 mA/$mg_{Pt}$ at 0.9 V and 0.85 V, respectively, which are about 1.7 times higher than those of commercial catalysts.

• 한국수소및신에너지학회논문집
• /
• 제22권4호
• /
• pp.415-423
• /
• 2011

HI decomposition step certainly demand catalytic reaction for efficient production of hydrogen in SI process. Platinum catalyst can apply to HI decomposition reaction as well as hydrogenation or dehydrogenation. Generally, noble metal is used as catalyst which is loaded form for getting high dispersion and wide active area. In this study, Pt was loaded onto zirconia, ceria, alumina, and silica by impregnation method. HI decomposition reaction was carried out under the condition of $450^{\circ}C$, 1atm, and $167.76h^{-1}$ (WHSV) in a fixed bed reactor for measuring catalytic activity. And property of a catalyst was observed by BET, TEM, XRD and chemisoption analysis. On the basis of experimental results, we discussed about conversion of HI according to physical properties of the loaded Pt catalyst onto each support.

• 한국자동차공학회논문집
• /
• 제14권1호
• /
• pp.8-16
• /
• 2006

The research was conducted to characterize of Rh-Pd-Pt TWC with a double-layer washcoat for gasoline vehicle. The physical characteristics on surface of catalyst were inspected by BET, SEM and TEM. The characteristics of catalytic reaction were examined by the TPD/TPR and CO-pulse chemisorption. The catalyst $6Hx(0.35\times11\times3)$ showed superior conversion performance after hydrothermal aging process, which was due to small difference of the surface area between. the fresh and the aged catalyst. The CO-chemisorption and surface area were superior in the 600 cpsi catalyst than other catalysts, this catalyst also shown the higher conversion efficiency of the exhaust emissions. From the TPR test, the conversion performance of the aged catalyst was decreased by the agglomeration and sintering of the PM and metal oxides. From the TPD result, it was found that the NO chemisorption was happed on the bottom-layer washcoat with Pd, and the NO chemisorption was re-happened on the upper-layer washcoat with Pt and Rh in the desorption process.