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Mn改性Cu/ZnO/Al_2O_3催化剂上甲醇水蒸气重整制氢研究
引用本文:张菊香,史鹏飞,刘春涛,张新荣. Mn改性Cu/ZnO/Al_2O_3催化剂上甲醇水蒸气重整制氢研究[J]. 天然气化工, 2004, 29(4): 11-15
作者姓名:张菊香  史鹏飞  刘春涛  张新荣
作者单位:哈尔滨工业大学应用化学系,哈尔滨,150001
摘    要:研究了Mn改性Cu/ZnO/Al2O3催化剂上的甲醇水蒸气重整制氢反应。考察了催化剂组成、反应温度和水醇比对反应的影响。研究结果表明,当催化剂的组成为Cu45Zn45Al5Mn5,反应温度为220~240℃,n(H2O)/n(CH3OH)=1~1 2,液体空速为3 0h-1左右时,反应具有较好的甲醇转化率、氢气产率和较低的出口CO含量,同时催化剂表现出较好的稳定性。

关 键 词:Cu/ZnO/Al2O3催化剂  甲醇  水蒸气重整  制氢
文章编号:1001-9219(2004)04-11-04
修稿时间:2004-05-13

Hydrogen Production from Steam Reforming of Methanol on Mn Promoted Cu/ZnO/Al2O3 Catalysts
ZHANG Ju-xiang,SHI Peng-fei,LIU Chun-tao,ZHANG Xin-rong. Hydrogen Production from Steam Reforming of Methanol on Mn Promoted Cu/ZnO/Al2O3 Catalysts[J]. Natural Gas Chemical Industry, 2004, 29(4): 11-15
Authors:ZHANG Ju-xiang  SHI Peng-fei  LIU Chun-tao  ZHANG Xin-rong
Abstract:The steam reforming of methanol on Mn promoted Cu/ZnO/Al_2O_3 catalysts was studied in this paper. The effects of catalyst composition, reaction temperatures, ratio of water to methanol and feed velocity on steam reforming reaction of methanol were investigated. Under optimized For Cu45Zn45Al5Mn5 catalyst, when reaction temperature was 220-240℃, molar ratio of water to methanol was 1.0-1.2 and liquid space velocity was about 3.0 h~(-1), higher methanol conversion and hydrogen yield and lower outlet CO concentration were obtained, and catalyst showed good stability.
Keywords:Mn promoted Cu/ZnO/Al_2O_3  methanol  steam reforming  hydrogen production
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