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CH_4部分氧化制氢Ni-CuZrSiO催化剂的研究 被引量:8

STUDY ON Ni-Cu/ZrSiO CATALYST FOR PARTIAL OXIDATION OF CH_4 TO PRODUCE HYDROGEN
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摘要 采用表面反应改性法制备了ZrO2 SiO2(ZrSiO)表面复合物,用等体积浸渍法制备了ZrSiO负载的Ni Cu双金属催化剂,并用IR、TPD、TPSR和微反技术考察了CH4、H2O和O2在催化剂表面上的化学吸附及反应性能。结果表明,在Ni Cu ZrSiO催化剂上存在着Ni Cu金属位,Lewis酸位Znn+和碱位Zr O-三类活性中心;CH4和H2O在金属位和Lewis酸位Znn+和碱位Zr O-的协同作用下可形成解离吸附态;CH4、H2O和O2在Ni Cu ZrSiO催化剂表面上的主要反应产物为H2和CO2,选择性均在95%以上。 The surface complex support ZrO_2-SiO_2 (ZrSiO) was prepared by surface reaction modification, and Ni-Cu/ZrSiO bimetallic catalyst was prepared by isovolumic impregnation. Adsorption and reaction of CH_4 with H_2O and O_2 on the catalyst were characterized by IR, TPD, TPSR and microreactor techniques. The results showed that there exist three kinds of active sites on the catalyst: metal site M, Lewis acid site Zn^(n+) and Lewis basic site Zr-O^-. With the cooperation of metal site M, Lewis acid site Zn^(n+) and Lewis basic site Zr-O^-, CH_4 was activated and dissociated into CO and H_2, H_2O was dissociated into H_2 and O on the catalyst. Under condition of reaction temperature 450?℃, n(CH_4)∶ n(O_2)∶ n(H_20)=1∶0.5∶2.5 and methane space velocity (SVCH_4)=1?200?h^(-1), the main reaction products on Ni-Cu/ZrSiO catalyst are H_2 and CO_2, with a selectivity over 95%.
出处 《燃料化学学报》 EI CAS CSCD 北大核心 2003年第6期531-537,共7页 Journal of Fuel Chemistry and Technology
基金 国家自然科学基金(20076035) ~~
关键词 甲烷 氢气 制备 选择氧化 复合氧化物载体 双金属催化剂 CH4 methane partial oxidation complex oxide support nickel copper bimetallic catalyst
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  • 1Semin G L, Belyaev V D, Demin A K, et al. Methane conversion to syngas over Pt-based electrode in a solid oxide fuel cell reactor[J]. Appl Catal A: 1999, 181(1):131-137.
  • 2Lidia Pino, Vincenzo Recupero, Sabina Beninati, et al. Catalytic partial-oxidation of methane on a ceria-supported platinum catalyst for application in fuel cell electric vehicles[J]. Appl Catal A: 2002, 225(1):63-75.
  • 3Radu Craciun, Wayne Daniell, Helmut Knozinger. The effect of CeO2 structure on the activity of supported Pd catalysts used for methane steam reforming[J]. Appl Catal A: 2002, 230(1-2):153-168.
  • 4Elnasides C, Kondarides D I, Neophytides S G, et al. Partial oxidation of methane to synthesis gas over Ru/TiO2 catalysts: effects of modification of the support on oxidation state and catalytic performance[J]. J Catal, 2001, 198(2):195-207.
  • 5尚丽霞,谢卫国,吕绍洁,邱发礼.碱土金属对甲烷与空气制合成气Ni/CaO-Al_2O_3催化剂性能的影响[J].燃料化学学报,2001,29(5):422-425. 被引量:21
  • 6Tsang S C, Claridge J B, Green M L H. Recent advances in the conversion of methane to synthesis gas[J]. Catal today, 1995, 23(1):3-15.
  • 7Choudhary T V, Sivadinarayana C, Chusuei C C, et al. Hydrogen production via catalytic decomposition of methane[J]. J Catal, 2001, 199(1):9-18.
  • 8钟顺和,黎汉生,王建伟,肖秀芬.CO_2和CH_3OH直接合成碳酸二甲酯用Cu-Ni/ZrO_2-SiO_2催化剂[J].催化学报,2000,21(2):117-120. 被引量:55
  • 9钟顺和,王杰慧.Ni—Cu和MgO—SiO2间的相互作用及其对催化性能的影响[J].Chinese Journal of Catalysis,1995,16(4):263-268. 被引量:4
  • 10钟顺和,黎汉生,王建伟.CO_2在Cu-Ni-Mo O_3-SiO_2催化剂上的吸附与反应[J].燃料化学学报,1999,27(4):305-308. 被引量:5

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