Influence of preparation method on performance of Cu/Zn-based catalysts for low-temperature steam reforming and oxidative steam reforming of methanol for H2 production for fuel cells

被引:189
作者
Shen, JP [1 ]
Song, CS [1 ]
机构
[1] Penn State Univ, Clean Fuels & Catalysis Program, Energy Inst, Dept Energy & Geoenvironm Engn, University Pk, PA 16802 USA
关键词
fuel cell; low-temperature steam reforming; Cu/Zn/Al catalyst; methanol; copper oxide reduction;
D O I
10.1016/S0920-5861(02)00235-3
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Several methods (impregnation, co-precipitation and hydrothermal synthesis) have been comparatively examined for the preparation of precursors to Cu/Zn/Al catalysts. Steam reforming and oxidative steam reforming of methanol was performed using the laboratory-prepared and a commercial Cu/Zn/Al catalysts at a relatively low temperature (230degreesC) for catalytic production of H-2. The, results show that the preparation method significantly affects the catalyst performance with respect to methanol conversion, H-2 yield and CO concentration. The catalyst with lower copper-reduction temperature shows higher activity for methanol conversion at lower temperature. The best Cu/Zn/Al catalyst has been prepared by a co-precipitation method, which shows high activity for methanol conversion (99-100%) and H-2 production (71-76%) with very low CO concentration (0.05-0.15%) in steam reforming (H2O/methanol = 1.43mol ratio) and in oxidative steam reforming (O-2/methanol 0.158-0.474 mol ratio) at a low temperature (230degreesC). (C) 2002 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:89 / 98
页数:10
相关论文
共 23 条
[11]   Synthesis and characterization of Cu-Al layered double hydroxides [J].
Lwin, Y ;
Yarmo, MA ;
Yaakob, Z ;
Mohamad, AB ;
Daud, WRW .
MATERIALS RESEARCH BULLETIN, 2001, 36 (1-2) :193-198
[12]   Cr2O3 promoted skeletal Cu catalysts for the reactions of methanol steam reforming and water gas shift [J].
Ma, L ;
Gong, B ;
Tran, T ;
Wainwright, MS .
CATALYSIS TODAY, 2000, 63 (2-4) :499-505
[13]   Production of carbon monoxide and hydrogen by methanol decomposition over nickel dispersed on porous glass [J].
Matsumura, Y ;
Kuraoka, K ;
Yazawa, T ;
Haruta, M .
CATALYSIS TODAY, 1998, 45 (1-4) :191-196
[14]  
Newson E, 2000, STUD SURF SCI CATAL, V130, P695
[15]   THE SPECIFIC COPPER SURFACE-AREAS IN CU/ZNO METHANOL SYNTHESIS CATALYSTS BY OXYGEN AND CARBON-MONOXIDE CHEMISORPTION - EVIDENCE FOR IRREVERSIBLE CO CHEMISORPTION INDUCED BY THE INTERACTION OF THE CATALYST COMPONENTS [J].
PARRIS, GE ;
KLIER, K .
JOURNAL OF CATALYSIS, 1986, 97 (02) :374-384
[16]   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
[17]   Synthesis of mesoporous molecular sieves: Influence of aluminum source on Al incorporation in MCM-41 [J].
Reddy, KM ;
Song, CS .
CATALYSIS LETTERS, 1996, 36 (1-2) :103-109
[18]  
Reitz T. L., 2000, STUD SURF SCI CATAL, V130, P3645
[19]   Layered double hydroxides with the hydrotalcite-type structure containing Cu2+, Ni2+ and Al3+ [J].
Rives, V ;
Kannan, S .
JOURNAL OF MATERIALS CHEMISTRY, 2000, 10 (02) :489-495
[20]  
SEGAL SR, 2001, AM CHEM SOC DIV FUEL, V46, P654