Biomass to hydrogen via fast pyrolysis and catalytic steam reforming of the pyrolysis oil or its fractions

被引:370
作者
Wang, D
Czernik, S
Montane, D
Mann, M
Chornet, E
机构
[1] NATL RENEWABLE ENERGY LAB,GOLDEN,CO 80401
[2] UNIV SHERBROOKE,SHERBROOKE,PQ J1K 2R1,CANADA
关键词
D O I
10.1021/ie960396g
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Pyrolysis of lignocellulosic biomass and reforming of the pyroligneous oils are being studied as a strategy for producing hydrogen. A process of this nature has the potential to be cost competitive with conventional means of producing hydrogen. We propose a regionalized system of hydrogen production, where small- and medium-sized pyrolysis units (< 500 Mg/day) provide bio-oil to a central reforming unit to be catalytically converted to H-2 and CO2. Thermodynamic modeling of the major constituents of the bio-oil has shown that reforming is possible within a wide range of temperatures and steam-to-carbon ratios. In addition, screening tests aimed at catalytic reforming of model compounds to hydrogen using Ni-based catalysts have achieved essentially complete conversion to Ha. Existing data on the catalytic reforming of oxygenates have been studied to guide catalyst selection. A process diagram for the pyrolysis and reforming operations is discussed, as are initial production cost estimates. A window of opportunity clearly exists if the bio-oil is first refined to yield valuable oxygenates so that only a residual fraction is used for hydrogen production.
引用
收藏
页码:1507 / 1518
页数:12
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