• 제목/요약/키워드: New catalyst

검색결과 800건 처리시간 0.025초

제올라이트에 담지된 전이금속 촉매상에서 메탄의 이산화탄소 개질반응에 관한 연구 (A study on the Reforming of Methane by Carbon Dioxide on the Transition Metal Catalysts Supported Zeolite)

  • 정헌도;김권일;김태환;이범석;박종기
    • 한국수소및신에너지학회논문집
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    • 제14권1호
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    • pp.69-80
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    • 2003
  • Nickel catalyst has been used for natural gas reforming with carbon dioxide, In this study, catalyst support used was HY zeolite. The optimum loading of Ni in the catalysts was 13 wt%. The effect of promoters, such as Mg, Mn, and K, was also studied. The addition of promoters to Ni catalyst improved the stability of catalysts and carbon deposition on Ni catalyst was suppressed. The reforming reactivity of promoter-added Ni catalyst was higher than that of Ni catalyst without any promoters. SEM, XRD, BET, TGA and FTIR tests were tried to characterize the catalyst structure before and after reaction.

Pt 촉매를 이용한 HI분해반응에서 지지체에 따른 영향 (Effect of Support in HI Decomposition Reaction using Pt Catalyst)

  • 고윤기;박주식;강경수;배기광;김영호
    • 한국수소및신에너지학회논문집
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    • 제22권4호
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    • pp.415-423
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    • 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.

니켈계 유사 하이드로탈사이트 촉매상에서 n-헥사데칸의 수증기 개질에 의한 수소 생산 (Hydrogen Production from Steam Reforming of n-Hexadecane over Ni-Based Hydrotalcite-Like Catalyst)

  • 이승환;문동주
    • 한국수소및신에너지학회논문집
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    • 제21권5호
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    • pp.412-418
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    • 2010
  • Steam reforming of n-hexadecane, a major component of diesel over Ni-based hydrotalcite-like catalyst was carried out at $900^{\circ}C$ at atmospheric pressure with space velocity of $10,000h^{-1}$ and feed molar ratio of steam/carbon=3.0. Ni-based hydrotalcite catalyst was prepared by a solid phase crystallization (spc) method and characterized by $N_2$-physisorption, CO chemisorption, TPR., XRD, and TEM techniques. It was found that spc Ni/MgAl catalyst showed higher catalytic stability and inhibition of carbon formation than Ni/$\gamma-Al_2O_3$ catalyst under the tested conditions. The results suggest that the modified spc-Ni/MgAl catalyst after optimization may be applied for the SR reaction of diesel.

Asymmetric Michael Addition of Ketones to Nitroolefins Catalyzed by a New Chiral Catalyst

  • Wang, Lian-Jun;Hu, Feng-Feng
    • Bulletin of the Korean Chemical Society
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    • 제31권5호
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    • pp.1280-1282
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    • 2010
  • A new chiral catalyst was synthesized and found that it could catalyzed the asymmetric Michael reaction of ketones with nitroolefins smoothly at room temperature, giving the desired adducts in 71 - 92% yields with excellent diastereoselectivities and high enantioselectivities (up to 95% ee).

Effects of Catalysts on Hydrazine Monopropellant Thruster Performances

  • Goto, Daisuke;Kagawa, Hideshi;Kajiwara, Kenichi;Ueno, Fumihiro;Umeda, Joji;Iihara, Shigeyasu
    • 한국추진공학회:학술대회논문집
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    • 한국추진공학회 2004년도 제22회 춘계학술대회논문집
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    • pp.137-141
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    • 2004
  • Many monopropellant thrusters use a catalyst for decompose the propellant, hydrazine. The catalyst directly affects the thruster performances and lifetime. Therefore, it is important to confirm that the catalyst is suitable for our thrusters. Until 2002, we used She1l405 catalyst, for satellite RCS thrusters, and H-IIA and M-V launch vehicle upper-stage RCS thrusters. In 2002, however, Shell Chemical Inc. ceased manufacturing She1l405 catalyst and transferred the product to AEROJET, where it was renamed S405. We subsequently investigated the characteristics of AEROJET's S405 catalyst and SOLVAY's KC12GA catalyst, (SOLVAY is a Belgian chemical company, and KC12GA is used for ASTRIUM's thruster) and conducted thruster firing tests using the new catalysts. After conducting, we confirm that the KC12GA catalyst was suitable for our thrusters, and decided to use KC12GA for two satellite programs.

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과산화수소 분해반응을 이용한 Pt계 촉매의 인산피독 특성 평가 방법 (The Analysis Method for Evaluation of Phosphoric Acid Poisioning of Pt Based Catalyst by Using Hydrogen Peroxide Decomposition Reaction)

  • 박정진;양승원;정용진;권용재
    • 한국수소및신에너지학회논문집
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    • 제28권6호
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    • pp.669-674
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    • 2017
  • In this study, the novel electrochemical and colorimetric analysis methods are suggested to estimate the degree of phosphoric acid ion poisoning on Pt based catalyst surface and to confirm the possibility of replacing the expensive and long time consumed conventional methods. As the ways, the electrochemical half cell tests such as cyclic voltammetry (CV) and linear sweep voltammetry (LSV) are used and the change in chemical behavior by absorption of the phosphoric acid ion on Pt based catalyst surface and hydrogen peroxide decomposition reaction are successfully recognized by colorimetric measurements. Conclusively, it is proved that the new methods show superior sensitivity for identifying the degree of phosphoric acid poisoned on Pt based catalyst.

Ni 기반 촉매를 이용한 HI 분해 반응 특성 (Characteristics of Hydrogen Iodide Decomposition using Alumina-Supported Ni Based Catalyst)

  • 김지혜;박주식;김창희;강경수;정성욱;조원철;김영호;배기광
    • 한국수소및신에너지학회논문집
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    • 제26권6호
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    • pp.507-515
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    • 2015
  • HI decomposition reaction requires a catalyst for the efficient production of hydrogen as a key reaction for hydrogen production in sulfur-iodine thermochemical water-splitting (SI) cycle. As a catalyst used in the reaction, the performance of platinum catalyst is excellent. While, the platinum catalyst is not economical. Therefore, studies of a nickel catalyst that could replace platinum have been carried out. In this study, the characteristics of the catalytic HI decomposition on the amount of loaded nickel (Ni = 0.1, 0.5, 1, 3, 5, 10 wt%) were investigated. As the supported Ni amount increased up to 3 wt%, HI decomposition was found to increase in linear proportion. However, the conversion of $Ni/Al_2O_3$ catalyst loaded above 3 wt% was not linear. It was thought that the different HI decomposition characteristics was caused in the size and metal dispersion of Ni particles of catalyst. The physical property of catalyst before and after HI decomposition reaction was characterized by BET, chemisorption, XRD and SEM analysis.

Eco-AZ91 MgH2의 반응열 제어에 미치는 촉매 분산 효과 (Effects of Catalyst Dispersion for Reaction Energy Control on Eco-AZ91 MgH2)

  • 이수선;석송;홍태환
    • 한국수소및신에너지학회논문집
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    • 제34권6호
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    • pp.631-640
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    • 2023
  • This study selected Eco-AZ91 MgH2, which shows high enthalpy as a material for this purpose, as the basic material, and analyzed the change in characteristics by synthesizing TiNi as a catalyst to control the thermodynamic behavior of MgH2. In addition, the catalyst dispersion technology using graphene oxide (GO) was studied to improve the high-temperature aggregation phenomenon of Ni catalyst and to secure a source technology that can properly disperse the catalyst. XRD, SEM, and BET analysis were conducted to analyze the metallurgical properties of the material, and TGA and DSC analysis were conducted to analyze the dehydrogenation temperature and calorific value, and the correlation between MgH2, TiNi catalyst, and GO reforming catalyst was analyzed. As a result, the MgH2-5 wt% TiNi at GO composite could lower the dehydrogenation temperature to 478-492 K due to the reduction of the catalyst aggregation phenomenon and the increase in the reaction specific surface area, and an experimental result for the catalyst dispersion technology by GO could be ensured.