Catalytic pyrolysis of woody biomass

被引:15
作者
Aho, A. [1 ]
Kumar, N. [1 ]
Eranen, K. [1 ]
Salmi, T. [1 ]
Holmbom, B. [2 ]
Backman, P. [3 ]
Hupa, M. [3 ]
Murzin, D. Yu [1 ]
机构
[1] Abo Akad Univ, Lab Ind Chem & React Engn, Proc Chem Ctr, FI-20500 Turku, Finland
[2] Abo Akad Univ, Lab Wood & Paper Chem, Proc Chem Ctr, FI-20500 Turku, Finland
[3] Abo Akad Univ, Lab Inorgan Chem, Proc Chem Ctr, FI-20500 Turku, Finland
来源
BIOFUELS-UK | 2010年 / 1卷 / 02期
基金
芬兰科学院;
关键词
Biomass; Bio-oil; Fluidized bed reactor; Zeolites; Catalytic pyrolysis; Catalytic upgrading;
D O I
10.4155/BFS.09.26
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
A review of the literature published between 2006 and 2009 concerning the pyrolysis of woody biomass and the catalytic upgrading of bio-oil is presented. The main results of our group regarding catalytic pyrolysis of woody biomass are also overviewed. Three different methods for investigating the effect of catalysts on the catalytic pyrolysis of woody biomass were investigated. The first method was conventional thermogravimetry, but, due to the lack of gas analysis, valuable information could not be obtained by this method. The second method of investigation was simultaneous pyrolysis and upgrading over zeolites in a fluidized bed reactor. In the third method, the pyrolysis occurred in a fluidized bed reactor and the pyrolysis vapors were upgraded downstream over zeolites in another fluidized bed reactor. For laboratory-scale pyrolysis, this method was the most suitable for screening of different zeolite catalysts, which was the main objective. It was possible to deoxygenate the bio-oil over zeolites in both fluidized bed reactor set-ups, resulting in higher CO and water formation.
引用
收藏
页码:261 / 273
页数:13
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