Evaluation of thermochemical routes for hydrogen production from biomass: A review

被引:378
作者
Arregi, Aitor [1 ]
Amutio, Maider [1 ]
Lopez, Gartzen [1 ]
Bilbao, Javier [1 ]
Olazar, Martin [1 ]
机构
[1] Univ Basque Country UPV EHU, Dept Chem Engn, POB 644, E-48080 Bilbao, Spain
关键词
Biomass; Bio-oil; Gasification; Pyrolysis; Reforming; Hydrogen; OIL AQUEOUS FRACTION; RICH GAS-PRODUCTION; PYROLYSIS BIO-OIL; SUPERCRITICAL WATER GASIFICATION; FLUIDIZED-BED REACTOR; NI-BASED CATALYSTS; OF-THE-ART; STEAM-GASIFICATION; ACETIC-ACID; MODEL COMPOUNDS;
D O I
10.1016/j.enconman.2018.03.089
中图分类号
O414.1 [热力学];
学科分类号
摘要
H-2 is regarded as one of the cleanest future energy carrier that can be generated from renewable sources and will give rise to a reduction of CO2 emissions and environmental problems related to the use of petroleum based feedstock. Thus, the thermochemical routes from biomass for sustainable H-2 production compared to other biomass treatment routes have a great potential for its industrial implementation. Gasification of biomass and reforming of the bio-oil produced by biomass pyrolysis are the most researched pathways, although some studies dealing with supercritical water gasification and bio-oil gasification can also be found in the literature. Nevertheless, pyrolysis and in-line catalytic steam reforming strategy is gaining great attention due to its advantages compared to gasification and bio-oil reforming, especially those related to the optimization of each step (pyrolysis and catalytic steps) and bio-oil feeding. This review deals with the different reactor configurations, operating conditions and catalysts used in each process and compares the different alternatives in terms of H-2 production, with emphasis placing on the advantages of the two-step strategy.
引用
收藏
页码:696 / 719
页数:24
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