Aqueous-phase reforming of ethylene glycol on Co/ZnO catalysts prepared by the coprecipitation method

被引:41
作者
Chu, Xianwen
Liu, Jun
Sun, Bo
Dai, Rui
Pei, Yan [1 ]
Qiao, Minghua
Fan, Kangnian
机构
[1] Fudan Univ, Dept Chem, Shanghai 200433, Peoples R China
关键词
Co/ZnO; Coprecipitation; Ethylene glycol; Aqueous-phase reforming; Hydrogen; SUPPORTED COBALT CATALYSTS; GAS SHIFT REACTION; OXYGENATED HYDROCARBONS; OXIDE CATALYSTS; H-2; PRODUCTION; HYDROGEN-PRODUCTION; NI CATALYSTS; ETHANOL; FE; METHANOL;
D O I
10.1016/j.molcata.2010.11.024
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
Co/ZnO catalysts with different Co/Zn ratios have been prepared by the coprecipitation method. It is revealed that below the nominal Co/Zn molar ratio of 2, the calcined Co/ZnO samples were constituted by ZnO and ZnCo2O4 spinel. At the nominal Co/Zn ratio of 2, a small amount of Co3O4 spinet emerged. After reduction, the catalysts were composed of fcc Co and ZnO. In aqueous-phase reforming (APR) of ethylene glycol, it is found that the intrinsic activity and selectivity to H-2 increase with the increment of the ZnO content. H-2 selectivities over the Co/ZnO catalysts ranged from 52% to 89%, which are substantially higher than that of the Raney Ni catalyst at similar conversion. Moreover, the Co/ZnO catalysts produced much less CO in the product gas. With the aid of literature works as well as additional experiments on APR of acetic acid, methanol, and ethanol, the reaction pathways of ethylene glycol in the presence of water on the Co/ZnO catalysts were discussed. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:129 / 135
页数:7
相关论文
共 40 条
[1]  
Chu XW, 2009, CHINESE J CATAL, V30, P595
[2]   Hydrogen from catalytic reforming of biomass-derived hydrocarbons in liquid water [J].
Cortright, RD ;
Davda, RR ;
Dumesic, JA .
NATURE, 2002, 418 (6901) :964-967
[3]   Hydrogen production by biological processes: a survey of literature [J].
Das, D ;
Veziroglu, TN .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2001, 26 (01) :13-28
[4]   A review of catalytic issues and process conditions for renewable hydrogen and alkanes by aqueous-phase reforming of oxygenated hydrocarbons over supported metal catalysts [J].
Davda, RR ;
Shabaker, JW ;
Huber, GW ;
Cortright, RD ;
Dumesic, JA .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2005, 56 (1-2) :171-186
[5]   Catalytic reforming of oxygenated hydrocarbons for hydrogen with low levels of carbon monoxide [J].
Davda, RR ;
Dumesic, JA .
ANGEWANDTE CHEMIE-INTERNATIONAL EDITION, 2003, 42 (34) :4068-4071
[6]   Aqueous-phase reforming of ethylene glycol on silica-supported metal catalysts [J].
Davda, RR ;
Shabaker, JW ;
Huber, GW ;
Cortright, RD ;
Dumesic, JA .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2003, 43 (01) :13-26
[7]   Preparation and characterization of Fischer-Tropsch active Co/SiO2 catalysts [J].
Ernst, B ;
Libs, S ;
Chaumette, P ;
Kiennemann, A .
APPLIED CATALYSIS A-GENERAL, 1999, 186 (1-2) :145-168
[8]   Alkali metal-doped cobalt oxide catalysts for NO decomposition [J].
Haneda, M ;
Kintaichi, Y ;
Bion, N ;
Hamada, H .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2003, 46 (03) :473-482
[9]   Current status of hydrogen production techniques by steam reforming of ethanol: A review [J].
Haryanto, A ;
Fernando, S ;
Murali, N ;
Adhikari, S .
ENERGY & FUELS, 2005, 19 (05) :2098-2106
[10]   Production of liquid alkanes by aqueous-phase processing of biomass-derived carbohydrates [J].
Huber, GW ;
Chheda, JN ;
Barrett, CJ ;
Dumesic, JA .
SCIENCE, 2005, 308 (5727) :1446-1450