Steam reforming of dimethyl ether over composite catalysts of γ-Al2O3 and Cu-based spinel

被引:154
作者
Tanaka, Y [1 ]
Kikuchi, R [1 ]
Takeguchi, T [1 ]
Eguchi, K [1 ]
机构
[1] Kyoto Univ, Grad Sch Engn, Dept Energy & Hydrocarbon Chem, Nishikyo Ku, Kyoto 6158510, Japan
关键词
steam reforming; dimethyl ether; Cu-Mn-Fe spinel-type oxide; gamma-Al2O3; methanol steam reforming; XPS; Auger electron spectroscopy;
D O I
10.1016/j.apcatb.2004.11.007
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
Cu-based spinel-type oxides were investigated for steam reforming of dimethyl ether (I)ME). Addition of gamma-Al2O3 to Cu catalysts improved DME conversion since hydrolysis of DME was promoted over acid-sites on gamma-Al2O3. Higher catalytic activity was shown over the composite of gamma-Al2O3 and Cu-Mn, or Cu-Fe, or Cu-Cr oxide than that of gamma-Al2O3 and Cu/ZnO/Al2O3- Cu-Fe and Cu-Mn catalysts demonstrated high activity for methanol steam reforming, which was ascribed to high performance for DME steam reforming. XPS measurements revealed that mono- and zero-valent copper species co-existed on Cu-Mn, Cu-Fe, and Cu/ZnO/Al2O3 catalysts subjected to in Situ H-2 reduction following methanol steam reforming. In the system of gamma-Al2O3 and Cu-Mn-Fe oxide, Mn/Fe ratio was optimized. Mn/Fe ratio exhibited influence on CO2 and CO selectivity. Mn-rich composite catalysts produced more CO than Fe-rich catalysts. The optimized atomic ratio of Cu/Mn/Fe was 2/1/3. DME conversion was not influenced by stearn/DME ratio in the feed gas, while CO formation was suppressed with a rise in steam/DME ratio. Complete DME conversion was attained below 350 T over the optimized composite catalyst. The optimal Al2O3/Cu-Mn-Fe weight ratio was between 1/2 and 1. High catalytic activity and thermal stability of the optimal composite was found by the time-on-steam test at as high as 400 degrees C for 100 h. (c) 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:211 / 222
页数:12
相关论文
共 21 条
[1]   HYDROGENATION ON COPPER CHROMITE CATALYST - ROLE OF THE CUPROUS IONS IN THE METHANOL SYNTHESIS FROM SYNGAS [J].
BECHARA, R ;
ABOUKAIS, A ;
HUBAUT, R ;
WROBEL, G ;
DHUYSSER, A ;
BONNELLE, JP .
JOURNAL DE CHIMIE PHYSIQUE ET DE PHYSICO-CHIMIE BIOLOGIQUE, 1992, 89 (04) :853-866
[2]   Comparative studies of manganese-doped copper-based catalysts: the promoter effect of Mn on methanol synthesis [J].
Chen, HY ;
Lin, J ;
Tan, KL ;
Li, J .
APPLIED SURFACE SCIENCE, 1998, 126 (3-4) :323-331
[3]   THE ACTIVITY AND STATE OF THE COPPER SURFACE IN METHANOL SYNTHESIS CATALYSTS [J].
CHINCHEN, GC ;
WAUGH, KC ;
WHAN, DA .
APPLIED CATALYSIS, 1986, 25 (1-2) :101-107
[4]  
Fleisch TH, 1997, STUD SURF SCI CATAL, V107, P117
[5]   Production of hydrogen from dimethyl ether [J].
Galvita, VV ;
Semin, GL ;
Belyaev, VD ;
Yurieva, TM ;
Sobyanin, VA .
APPLIED CATALYSIS A-GENERAL, 2001, 216 (1-2) :85-90
[6]   Kinetic modeling of the production of hydrogen from the methanol-steam reforming process over Mn-promoted coprecipitated Cu-Al catalyst [J].
Idem, RO ;
Bakhshi, NN .
CHEMICAL ENGINEERING SCIENCE, 1996, 51 (14) :3697-3708
[7]  
KIKO M, 1997, J MOL CATAL A-CHEM, V126, P169
[8]   EXAFS and XPS investigations of Cu/ZnO catalysts and their interaction with CO and methanol [J].
Kulkarni, GU ;
Rao, CNR .
TOPICS IN CATALYSIS, 2003, 22 (3-4) :183-189
[9]   The role of ZnO in Cu/ZnO methanol synthesis catalysts [J].
Nakamura, J ;
Uchijima, T ;
Kanai, Y ;
Fujitani, T .
CATALYSIS TODAY, 1996, 28 (03) :223-230
[10]   Low-pressure DME synthesis with Cu-based hybrid catalysts using temperature-gradient reactor [J].
Omata, K ;
Watanabe, Y ;
Umegaki, T ;
Ishiguro, G ;
Yamada, M .
FUEL, 2002, 81 (11-12) :1605-1609