Study about the kinetic processes of biomass steam gasification

被引:131
作者
Dupont, Capucine
Boissonnet, Guillaume
Seller, Jean-Marie
Gauthier, Paola
Schweich, Daniel
机构
[1] CEA, DTN, SE2T, LPTM, F-38054 Grenoble 09, France
[2] CNRS, ESCPE, LGPC, F-69616 Villeurbanne, France
关键词
biomass; gasification; modelling;
D O I
10.1016/j.fuel.2006.06.011
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 [动力工程及工程热物理]; 0820 [石油与天然气工程];
摘要
Modelling approaches of biomass steam gasification are investigated that take into account both chemical and physical kinetic limitations. The gas phase can be described by two independent reactions: (i) the steam reforming of CH4, which is kinetically limited under the operating conditions (1073 < T < 1273 K, p = 1 bar), (ii) the water-gas shift reaction, which would be close to equilibrium under the operating conditions (1073 < T < 1273 K, p = I bar). Concerning solid, a time scale analysis of the main phenomena has been performed. For particles of 500 mu m, the transformation can be seen as two successive steps: (i) pyrolysis of biomass, which is both chemically and heat-transfer controlled; (ii) steam gasification of residue, which is chemically controlled. (c) 2006 Elsevier Ltd. All rights reserved.
引用
收藏
页码:32 / 40
页数:9
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