In-chamber thermocatalytic tar cracking and syngas reforming using char-supported NiO catalyst in an updraft biomass gasifier

被引:11
作者
James, Arthur M. [1 ]
Yuan, Wenqiao [1 ]
Boyette, Michael D. [1 ]
Wang, Donghai [2 ]
Kumar, Ajay [3 ]
机构
[1] N Carolina State Univ, Dept Biol & Agr Engn, Raleigh, NC 27695 USA
[2] Kansas State Univ, Dept Biol & Agr Engn, Manhattan, KS 66506 USA
[3] Oklahoma State Univ, Dept Biosyst & Agr Engn, Stillwater, OK 74078 USA
关键词
biomass gasification; tar cracking; syngas reforming; nickel catalyst; char catalyst; GASIFICATION; CONVERSION;
D O I
10.3965/j.ijabe.20140706.011
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
The objective of this study was to evaluate the performance of an in-chamber tar cracking and syngas reforming unit. This unit was composed of a two-stage tubular reactor placed within the combustion zone of an updraft biomass gasifier. Heat generated in the exothermic combustion reactions of biomass gasification drove tar cracking and syngas reforming in the tubes, eliminating the need of external heating. The performance of the unit was evaluated using char-supported NiO catalysts and was found to be very effective in tar removal and syngas composition enhancement. A tar removal rate of 95% was achieved at 0.3 s residence time and 10% nickel loading. This condition also gave syngas high-heating value increment of 36% (to 7.3 MJ/m(3)). The effect of gas residence time and Ni loading on tar removal and syngas composition of the unit was also studied. Gas residence of 0.2-0.3 s and Ni loading of 5%-10% were found appropriate to produce clean syngas with tar content appropriate for industrial applications (<0.6 g/m(3)) in an updraft biomass gasifier without external heating.
引用
收藏
页码:91 / 97
页数:7
相关论文
共 26 条
[1]  
Annamalai K, 2001, ADV THERMODYNAMICS E, P519
[2]  
[Anonymous], 1998, BIOMASS GASIFIER TAR
[3]  
Basu P, 2010, TAR PRODUCTION DESTR
[4]  
Dayton DA., 2002, Catalyst Today, V71, P227
[5]   The Fischer-Tropsch process: 1950-2000 [J].
Dry, ME .
CATALYSIS TODAY, 2002, 71 (3-4) :227-241
[6]   Experimental comparison of biomass chars with other catalysts for tar reduction [J].
El-Rub, Z. Abu ;
Bramer, E. A. ;
Brem, G. .
FUEL, 2008, 87 (10-11) :2243-2252
[7]   A thermodynamic analysis of methanation reactions of carbon oxides for the production of synthetic natural gas [J].
Gao, Jiajian ;
Wang, Yingli ;
Ping, Yuan ;
Hu, Dacheng ;
Xu, Guangwen ;
Gu, Fangna ;
Su, Fabing .
RSC ADVANCES, 2012, 2 (06) :2358-2368
[8]  
Geyer WA, 1997, WOOD FIBER SCI, V29, P85
[9]   Syngas production from catalytic gasification of waste polyethylene: Influence of temperature on gas yield and composition [J].
He, Maoyun ;
Xiao, Bo ;
Hu, Zhiquan ;
Liu, Shiming ;
Guo, Xianjun ;
Luo, Siyi .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2009, 34 (03) :1342-1348
[10]   An overview of aqueous-phase catalytic processes for production of hydrogen and alkanes in a biorefinery [J].
Huber, GW ;
Dumesic, JA .
CATALYSIS TODAY, 2006, 111 (1-2) :119-132