Sorption enhanced catalytic steam gasification process: a direct route from lignocellulosic biomass to high purity hydrogen

被引:82
作者
Fermoso, Javier [1 ]
Rubiera, Fernando [2 ]
Chen, De [1 ]
机构
[1] Norwegian Univ Sci & Technol NTNU, Dept Chem Engn, NO-7491 Trondheim, Norway
[2] Inst Nacl Carbon INCAR CSIC, Oviedo 33080, Spain
关键词
FLUIDIZED-BED; METHANE;
D O I
10.1039/c2ee02593k
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
We report for the first time on the one-stage production of high purity hydrogen from raw solid lignocellulosic biomass by sorption enhanced catalytic steam gasification (SECSG) in a combined downdraft flow fluidized bed and fixed bed reactor. A Pd/Co-Ni catalyst derived from a hydrotalcite-like material (HT) and dolomite as a CO2 acceptor are fed together with a biomass (chestnut wood sawdust) as the reactor feed. Almost pure hydrogen (>99.9 vol%) and high H-2 yields (up to 90%) can be achieved by this process, which combines conventional gasification/steam reforming, water-gas shift (WGS) reaction and H-2 separation by CO2 capture in one step. The in situ removal of CO2 by the carbonation reaction of dolomite shifts the equilibrium of steam reforming and WGS reactions towards H-2 production. The hydrotalcite derived Pd/Co-Ni catalyst has shown high activity in the cleavage of C-C and C-H bonds during the conversion of tars and hydrocarbons resulting from fast pyrolysis and catalytic steam gasification (CSG), as a result of which further char formation is reduced. The catalyst, which does not require pre-reduction, has shown a good activity and stability after several reaction-regeneration cycles.
引用
收藏
页码:6358 / 6367
页数:10
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