H2 production by steam reforming with in situ CO2 capture of biomass-derived bio-oil

被引:5
|
作者
Gil, M. V. [1 ]
Esteban-Diez, G. [1 ]
Pevida, C. [1 ]
Chen, D. [2 ]
Rubiera, F. [1 ]
机构
[1] INCAR CSIC, Inst Nacl Carbon, Oviedo 33080, Spain
[2] Norwegian Univ Sci & Technol, Dept Chem Engn, NO-7491 Trondheim, Norway
关键词
H-2; production; sorption enhanced steam reforming (SESR); Pd/Ni-Co catalyst; biomass; bio-oil; HYDROGEN-PRODUCTION; ACETIC-ACID; CHALLENGES; CATALYSTS;
D O I
10.1016/j.egypro.2014.11.715
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
High-purity H-2 was produced by the sorption enhanced steam reforming (SESR) of acetic acid, a model compound of bio-oil obtained from biomass fast pyrolysis. A fixed bed reactor comprising two sections with different temperature was used to favor the reforming reaction in the high-temperature section, and the water gas shift (WGS) and the CO2 capture reactions along the low-temperature segment. A Pd/Ni-Co hydrotalcite-like material (HT) was used as catalyst and a CaO-based material as CO2 sorbent. High H-2 yield (84.4%), with H-2 purity of 99.8%, was obtained at atmospheric pressure and 600 degrees C in the above section of the bed followed by a bed temperature of 500 degrees C at the bottom part. A null CO concentration was achieved, while the CH4 and CO2 contents showed very low values (0.15% and 0.02%, respectively). (C) 2013 The Authors. Published by Elsevier Ltd.
引用
收藏
页码:6815 / 6823
页数:9
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