Experimental comparison of biomass chars with other catalysts for tar reduction

被引:393
作者
El-Rub, Z. Abu [1 ]
Bramer, E. A. [1 ]
Brem, G. [1 ,2 ]
机构
[1] Univ Twente, Lab Thermal Engn, NL-7500 AE Enschede, Netherlands
[2] TNO, NL-7300 AH Apeldoorn, Netherlands
关键词
biomass char; catalysts; tar; gasification;
D O I
10.1016/j.fuel.2008.01.004
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
In this paper the potential of using biomass char as a catalyst for tar reduction is discussed. Biomass char is compared with other known catalysts used for tar conversion. Model tar compounds, phenol and naphthalene, were used to test char and other catalysts. Tests were carried out in a fixed bed tubular reactor at a temperature range of 700-900 degrees C under atmospheric pressure and a gas residence time in the empty catalyst bed of 0.3 s. Biomass chars are compared with calcined dolomite, olivine, used fluid catalytic cracking (FCC) catalyst, biomass ash and commercial nickel catalyst. The conversion of naphthalene and phenol over these catalysts was carried out in the atmosphere of CO2 and steam. At 900 degrees C, the conversion of phenol was dominated by thermal cracking whereas naphthalene conversion was dominated by catalytic conversion. Biomass chars gave the highest naphthalene conversion among the low cost catalysts used for tar removal. Further, biomass char is produced continuously during the gasification process, while the other catalysts undergo deactivation. A simple first order kinetic model is used to describe the naphthalene conversion with biomass char. (C) 2008 Elsevier Ltd. All rights reserved.
引用
收藏
页码:2243 / 2252
页数:10
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