EFFECT OF REFORMER CONDITIONS ON CATALYTIC REFORMING OF BIOMASS-GASIFICATION TARS

被引:72
作者
KINOSHITA, CM [1 ]
WANG, Y [1 ]
ZHOU, JC [1 ]
机构
[1] UNIV HAWAII MANOA,DEPT BIOSYST ENGN,HONOLULU,HI 96822
关键词
D O I
10.1021/ie00048a004
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Parametric tests on catalytic reforming of tars produced in biomass gasification are performed using a bench-scale, fluid-bed catalytic reformer containing a commercial nickel-based catalyst. The product gas composition and yield vary with reformer temperature, space time, and steam: biomass ratio. Under certain catalytic tar reforming conditions, the gas yield increases by 70%; 97% of the tars are cracked into gases; and benzene and naphthalene, the predominant tar species, are virtually eliminated from the product gas.
引用
收藏
页码:2949 / 2954
页数:6
相关论文
共 7 条
[1]   IMPROVED STEAM GASIFICATION OF LIGNOCELLULOSIC RESIDUES IN A FLUIDIZED-BED WITH COMMERCIAL STEAM REFORMING CATALYSTS [J].
AZNAR, MP ;
CORELLA, J ;
DELGADO, J ;
LAHOZ, JQ .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1993, 32 (01) :1-10
[2]   EXPERIMENTAL APPROACH TO THE CATALYZED CRACKING REACTION OF TAR FROM WOOD PYROLYSIS [J].
DONNOT, A ;
MAGNE, P ;
DEGLISE, X .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 1991, 21 (03) :265-280
[3]   MOLECULAR CHARACTERIZATION OF THE PYROLYSIS OF BIOMASS .1. FUNDAMENTALS [J].
EVANS, RJ ;
MILNE, TA .
ENERGY & FUELS, 1987, 1 (02) :123-137
[4]   TAR FORMATION UNDER DIFFERENT BIOMASS GASIFICATION CONDITIONS [J].
KINOSHITA, CM ;
WANG, Y ;
ZHOU, J .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 1994, 29 (02) :169-181
[5]  
MUDGE LK, 1987, PNL5699 INT REP
[6]  
PHILP RJ, 1986, NRCC27143 NAT RES CO
[7]  
WANG Y, 1991, SOL WORLD C 2, V1, P799