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低温高活性甲醇水蒸气重整制氢催化剂的研究 被引量:5

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作者 李永红 任杰
出处 《化工催化剂及甲醇技术》 2000年第5期1-2,共2页 Chemical Catalysts and Methanol Technology
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  • 1秦建中,张元东.甲醇裂解制氢工艺与优势分析[J].玻璃,2004,31(5):29-32. 被引量:2
  • 2周仁贤,陈平,郑小明,陈林深.CuO/ZrO_2活性组分与载体相互作用及其TPR特性[J].物理化学学报,1996,12(5):464-467. 被引量:17
  • 3TetsueT.Catalytic steam reformer for producing H2-rich gases in fuel cells[P].JP 08217403.1996-10-16.
  • 4Adamson K A, Pearson P. Hyda'ogen and methanol: a comperison of safety, economics, efficiencies and emissions[ J]. J Power Sources, 2000, 86(2) : 548-555.
  • 5Ma L, Gong B, Tran T. Cr2O3 promoted skeletal Cu catalysts for the reaction of methanol steam reforming and water gas shift[J].Catal Today, 2000, 63(4):499-505.
  • 6Shen G C, Fujita S I, Takezawa N. Steam reforming of methanol on binary Cu/ZnO catalysts: effect of preparation condilion upon precursors, surface structure and catalytic activity[J]. J Mole Catal A: Chem, 1997, 124(3):123-126.
  • 7Wies W, Emonts B. Methanol steam reforming in fuel cell drive system[J]. J Power Sources, 1999, 84(2): 187-193.
  • 8Peppley B A, Amphlett J C. Methanol steam reforming on Cu/ZnO/AlO3. Part 1: the reaction network[J]. Appl Catal A, 1999,179(1) : 21-29.
  • 9Lin Y M, Rei M H. Process development for generating high purity hydrogen by using supported palladium membrane reactor as steam reformer[J]. Int J Hydrogen Energy, 2000, 25(3) :211-219.
  • 10Toshimasa U, Koshi S. CO removal by oxygen-assisted water gas shift reaction over supported Cu catalysts[ J]. Appl Catal A,2000, 194(1):21-26.

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