Gasification of cellulose over Rh/CeO2/SiO2 catalysts:: Combustion of coke and reforming of tar

被引:11
作者
Tomishige, K [1 ]
Miyazawa, T [1 ]
Asadullah, M [1 ]
Ito, S [1 ]
Kunimori, K [1 ]
机构
[1] Univ Tsukuba, Inst Mat Sci, Tsukuba, Ibaraki 3058573, Japan
关键词
cellulose; biomass; gasification; rhodium catalyst; cerium oxide catalyst; synthesis gas;
D O I
10.1627/jpi.46.69
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The conventional methods for biomass gasification to hydrogen and synthesis gas are carried out at high temperature. Recently Rh/CeO2 based catalysts has been shown to be very effective for the catalytic gasification of cellulose at low reaction temperatures. The catalyst performance of Rh/CeO2/SiO2 catalysts was investigated using a continuous feed fluidized bed reactor and cellulose as a model compound of biomass. The performance of the Rh/CeO2/SiO2 catalysts was very dependent on the loading amount of CeO2, so the optimum loading was determined. Furthermore, analysis of the product distribution over various catalysts suggests that coke is removed by combustion with oxygen and tar is converted to synthesis gas via the reforming reaction. The low temperature catalytic gasification of cellulose requires high catalyst activity for combustion and reforming, and our optimized catalyst showed adequate activities for both reactions.
引用
收藏
页码:69 / 76
页数:8
相关论文
共 22 条
[1]   A NEW CATALYST FOR THE CATALYTIC GASIFICATION OF BIOMASS [J].
ARAUZO, J ;
RADLEIN, D ;
PISKORZ, J ;
SCOTT, DS .
ENERGY & FUELS, 1994, 8 (06) :1192-1196
[2]   Catalytic pyrogasification of biomass. Evaluation of modified nickel catalysts [J].
Arauzo, J ;
Radlein, D ;
Piskorz, J ;
Scott, DS .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (01) :67-75
[3]   Energy efficient production of hydrogen and syngas from biomass: Development of low-temperature catalytic process for cellulose gasification [J].
Asadullah, M ;
Ito, SI ;
Kunimori, K ;
Yamada, M ;
Tomishige, K .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2002, 36 (20) :4476-4481
[4]   Biomass gasification to hydrogen and syngas at low temperature: Novel catalytic system using fluidized-bed reactor [J].
Asadullah, M ;
Ito, S ;
Kunimori, K ;
Yamada, M ;
Tomishige, K .
JOURNAL OF CATALYSIS, 2002, 208 (02) :255-259
[5]   Catalytic performance of Rh/CeO2 in the gasification of cellulose to synthesis gas at low temperature [J].
Asadullah, M ;
Fujimoto, K ;
Tomishige, K .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2001, 40 (25) :5894-5900
[6]  
ASADULLAH M, 2001, CATAL COMMUN, V2, P63
[7]   Commercial steam reforming catalysts to improve biomass gasification with steam-oxygen mixtures. 2. Catalytic tar removal [J].
Aznar, MP ;
Caballero, MA ;
Gil, J ;
Martin, JA ;
Corella, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (07) :2668-2680
[8]   Partial oxidation of methane -: Effect of reaction parameters and catalyst composition on the thermal profile and heat distribution [J].
Basile, F ;
Fornasari, G ;
Trifirò, F ;
Vaccari, A .
CATALYSIS TODAY, 2001, 64 (1-2) :21-30
[9]   CATALYSIS IN THERMAL BIOMASS CONVERSION [J].
BRIDGWATER, AV .
APPLIED CATALYSIS A-GENERAL, 1994, 116 (1-2) :5-47
[10]   Biomass gasification with air in fluidized bed. Hot gas cleanup with selected commercial and full-size nickel-based catalysts [J].
Caballero, MA ;
Corella, J ;
Aznar, MP ;
Gil, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2000, 39 (05) :1143-1154