The effects of ZrO2 on Cu-ZnO-ZrO2 catalysts for hydrogen generation by steam reforming of methanol

被引:4
作者
Yun, H [1 ]
Chen, JH [1 ]
Zhang, H [1 ]
Lin, JD [1 ]
Chen, HB [1 ]
Lin, CJ [1 ]
机构
[1] Xiamen Univ, Dept Chem, Xiamen 361005, Peoples R China
关键词
Cu-ZnO-ZrO2; catalyst; steam reforming of methanol; methanol; hydrogen;
D O I
10.3866/PKU.WHXB20040521
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The effects of Zr in CuO-ZnO-ZrO2 catalysts on the diameter of CuO and ZnO, BET surface area of the catalysts as well as the catalytic activity have been studied by XRD, TEM, BET and the evaluation of catalytic activity for steam reforming of methanol (SRM). The results indicated that the diameter of catalyst particle was lowered from 15 to 10 nm (the average diameters of CuO and ZnO were lowered from 7.7 and 10.4 nm to 3.9 and 8.7 nm, respectively), the BET surface area was increased from 60 to 78 m(2) (.) g(-1) due to the existence of Zr. The conversion of methanol and the sensitivity of both hydrogen and carbon dioxide over Cu-ZnO-ZrO2 catalysts in SRM reaction were changed along with content of Zr in the catalysts. The conversion of methanol of 51.6% and the sensitivity of both hydrogen and carbon dioxide of 100% (content of CO and CH4 was lower than 10(-4)(phi) and can not be detected by 102GC) were obtained under the following reaction conditions: Zr content of 24.0% (omega) in the catalyst, reaction temperature of 220 degreesC and mole ratio of water to methanol of 1.3. These results have important significance in the application of steam reformer of methanol for methanol fuel cell.
引用
收藏
页码:550 / 553
页数:4
相关论文
共 10 条
[1]   Methanol reforming for fuel-cell applications: development of zirconia-containing Cu-Zn-Al catalysts [J].
Breen, JP ;
Ross, JRH .
CATALYSIS TODAY, 1999, 51 (3-4) :521-533
[2]  
CAI YC, 2001, Patent No. 1288854
[3]  
GUO XJ, 1999, IND CATAL, V6, P22
[4]  
HAO SR, 1997, Patent No. 1155511
[5]  
HUANG Z, 1998, Patent No. 1203187
[6]   PRODUCTION OF HYDROGEN FROM METHANOL OVER PROMOTED COPRECIPITATED CU-AL CATALYSTS - THE EFFECTS OF VARIOUS PROMOTERS AND CATALYST ACTIVATION METHODS [J].
IDEM, RO ;
BAKHSHI, NN .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (05) :1548-1557
[7]   PRODUCTION OF HYDROGEN FROM METHANOL .1. CATALYST CHARACTERIZATION STUDIES [J].
IDEM, RO ;
BAKHSHI, NN .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1994, 33 (09) :2047-2055
[8]  
蒋元力, 2001, 燃料化学学报, V29, P347
[9]   SURFACE CHARACTERIZATION OF CUO-ZNO METHANOL-SYNTHESIS CATALYSTS BY X-RAY PHOTOELECTRON-SPECTROSCOPY .1. PRECURSOR AND CALCINED CATALYSTS [J].
OKAMOTO, Y ;
FUKINO, K ;
IMANAKA, T ;
TERANISHI, S .
JOURNAL OF PHYSICAL CHEMISTRY, 1983, 87 (19) :3740-3747
[10]   Methanol-steam reforming on Cu/ZnO/Al2O3.: Part 1:: The reaction network [J].
Peppley, BA ;
Amphlett, JC ;
Kearns, LM ;
Mann, RF .
APPLIED CATALYSIS A-GENERAL, 1999, 179 (1-2) :21-29