New nickel-based material (Sr12Al14O33) for biomass tar steam reforming for syngas production

被引:12
作者
Li, Chunshan [1 ]
Wang, Murong [1 ]
Dai, Fei [1 ]
Suzuki, Kenzi [2 ]
机构
[1] Chinese Acad Sci, Beijing Key Lab Ion Liquids Clean Proc, State Key Lab Multiphase Complex Syst, Inst Proc Engn, Beijing 100190, Peoples R China
[2] Nagoya Univ, EcoTopia Sci Inst, Nagoya, Aichi 4648603, Japan
基金
中国国家自然科学基金;
关键词
CATALYTIC DECOMPOSITION; HYDROGEN-PRODUCTION; GASIFICATION GAS; MODEL; DOLOMITE; NAPHTHALENE; REMOVAL; OLIVINE; TOLUENE; PHENOL;
D O I
10.1063/1.4811803
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A new "free oxygen" material, Sr12Al14O33 (Sr(12)A(7)), was developed as a Ni support for biomass tar steam reforming. Toluene was chosen as the model compound for biomass gasification tar. The steam reforming process was investigated in a fixed-bed reactor. The influence of the operating parameters (i.e., reaction temperature, steam-to-carbon ratio, and space time) on catalyst activity and product selectivity were studied. Ni/Sr(12)A(7) (5 wt %) showed a higher activity compared with a similar commercial catalyst, Ni/Dolomite. The influence of the steam/carbon (S/C) molar ratio on gas yields at values ranging from 1.5 to 4.0 was investigated. The results show that the H-2 and CO2 yields increased, whereas the CO yield decreased, when the S/C ratio was increased. The influence of space-time (w(cat)/F-toluene) was also determined. The H-2, CO2, and total gas yields increased when the ratio was increased. Catalyst ageing experiments were characterized by Brunauer-Emmett-Teller (BET), X-ray diffraction (XRD), and energy dispersive X-ray spectrometer (EDX). Based on the results, the kinetic model is proposed as a first-order reaction for toluene with an activation energy of 131.2 kJ.mol(-1), as generally accepted in the literature. (C) 2013 AIP Publishing LLC.
引用
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页数:11
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