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微通道反应器中Cu-Ce-Zr-O催化剂催化氧化去除富氢气体中CO的研究 被引量:3

Removal of carbon monoxide from hydrogen-rich gas by catalytic oxidation over Cu-Ce-Zr-O catalysts in micro-channel reactor
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摘要 利用溶胶-凝胶法制备Cu-Ce-Ze-O催化剂并将其负载于微通道反应器内,用于富氢气体中CO的选择性氧化。考察了Zr的掺杂量、焙烧温度以及催化剂预处理对催化剂性能的影响,并确定反应的最佳空速。结果表明,Cu1Zr2Ce9Oδ催化剂催化作用下,在反应温度180℃~240℃,CO转化率达99%以上;在温度210℃~230℃内,产品气中φ(CO)降到10×10-6以下。与新鲜催化剂相比,经H2处理后的催化剂反应性能有了较大的提高,且低温活性较好。空速的增加有利于反应的选择性提高。 Cu-Ce-Ze-O catalysts were prepared by sol-gel methods and supported inside microchannel reactor for removal of carbon monoxide from hydrogen-rich gas by catalytic oxidation. The effects of Zr doped amount, calcination temperature, and pretreatment methods on the performances of the catalysts were investigated, and the optimum space velocity was determined. The results showed that for the Cu1Zr2Ce9O8 catalyst carbon monoxide conversion was above 99% in reaction temperature range of 180℃- 240℃, and carbon monoxide volume fraction in the gas could be degraded to below 10×10^-6 in reaction temperature range of 210℃-230℃. The catalysts with hydrogen pretreatment had better performances and low temperature activity. Increasing space velocity Could improve reaction selectivity.
出处 《天然气化工—C1化学与化工》 CAS CSCD 北大核心 2009年第2期40-44,共5页 Natural Gas Chemical Industry
基金 国家自然科学基金(20576023) 广东省自然科学基金(06025660)
关键词 富氢气体 微通道反应器 一氧化碳选择性氧化 催化剂 hydrogen-rich gas micro-channel reactor carbon monoxide selective oxidation catalyst
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  • 1Mehta V,Cooper J S.Review and analysis of PEM fuel cell design and manufacturin[J].J Power sources,2003,114:32-53.
  • 2Amphlett J C,Mann R F,Peppley B A.On board hydrogen purification for steam reformation/PEM fuel cell vehicle power plant[J].Int J Hydrogen Energy, 1996, 21 (8):673-678.
  • 3Kahhch M J,Gasteiger H A,Behm R J.Kinetics of the selective low-temperature oxidation of CO in H2-rich gas over Au/α-Fe2O3[J] .J Catal, 1999,182:430-440.
  • 4王乐夫,张美英,李雪辉,黄仲涛.微化学工程中的微反应技术[J].化学反应工程与工艺,2001,17(2):174-179. 被引量:15
  • 5韦广梅,曾尚红.微反应器的发展现状[J].世界科技研究与发展,2005,27(5):45-50. 被引量:11
  • 6Johnson B R,Canfield N L, Tran D N,et al.Engineered SMR catalysts based on hydrothermally stable, porous, ceramic supports for microchannet reactors[J]. Catal Today,2007,120:54-62.
  • 7郑亚锋,赵阳,辛峰.微反应器研究及展望[J].化工进展,2004,23(5):461-467. 被引量:57
  • 8Chen G W,Li S L,Yuan Q.Pd-Zn/Cu-Zn-Al catalysts prepared for methanol oxidation reforming in microchannel reactors[J].Catal Today,2007,120:63-70.
  • 9董新法,邹汉波,林维明.富氢气体中CO选择性氧化催化剂及其制备方法[P].CN:1768926A,2006.
  • 10Yu X H,Tu S T,Wang Z D,et al.Development of a microchannel reactor concerning steam reforming of methanol[J].Chem Eng J,2006,116:123-132.

二级参考文献87

  • 1黑瑟尔.沃尔克,勒韦.霍尔格.微反应器研究与应用新进展[J].现代化工,2004,24(7):9-16. 被引量:13
  • 2刘源,王哓燕,白雪.氧化铈气凝胶担载的铜催化剂对氢气中一氧化碳选择氧化的催化性能[J].中国稀土学报,2004,22(4):543-546. 被引量:6
  • 3董林,金永漱,陈懿.CuO在CeO_2载体上的存在状态研究——氧化物-氧化物相互作用的“嵌入模型”[J].中国科学(B辑),1996,26(6):561-566. 被引量:13
  • 4[1]Zech T, Honicke D. Microreaction Technology: Potentials and Technical Feasibility[J]. Erdol Erdgas Kohle, 114, Jahrgang, Heft 12, Dezember 1998:578~581.
  • 5[2]Irven H Rinard. 4th International Conference on Microreaction Technology, 138th street at Convent Avenue New York, NY 10031, 2000.
  • 6[3]WieBmeier G, Schubert K, Honicke D. Monolithic Microreactors Possessing Regular Mesopore Systems for the Successful Performance of Heterogeneously Catalysed Reaction[M]. in: Ehrfeld W. (eds.): Microreaction Technology, Springer Verlag, Berlin, Herdelberg, 1998,20~26.
  • 7[4]WieBmeier G, Honicke D. Microfabricated Components for Heterogeneously Catalysed Reaction[J]. J Micromech Microeng. 1996,6(2):285~298.
  • 8[5]Cussler E L. Diffusion, Mass Transfer in Fluid Systems[M]. 2nd ed. Cambridge University Press, Cambridge,1997.
  • 9[6]Keisuke Kageyama, Jun-ichi Tamazawa, Takuzo Aida, Extrusion Polymerization: Catalyzed Synthesis of Crystalline Linear Polyethylene Nanofibers Within a Mesoporous Silica[J]. Science, 1999, 285(24): 2113~2115.
  • 10殷慧龄,1992年

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