Thermodynamic analysis of autothermal steam and CO2 reforming of methane

被引:160
作者
Li, Yunhua [1 ]
Wang, Yaquan [1 ]
Zhang, Xiangwen [1 ]
Mi, Zhentao [1 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, Minist Educ, Key Lab Green Chem Technol, Tianjin 300072, Peoples R China
关键词
hydrogen production; steam reforming; CO2; reforming; autothermal reforming; methane; thermodynamic calculations;
D O I
10.1016/j.ijhydene.2008.02.051
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Thermodynamic equilibrium of methane autothermal reforming was studied by Gibbs free minimization for methane and H2O or CO2 conversions, H-2 yield and coke deposition as a function of H2O-to-CH4 ratio, CO2-to-CH4 ratio, O-2-to-CH4 ratio, reforming temperature and pressure. The optimal reaction conditions for reforming and the ways for coke elimination were given. The results showed that coke formed in CO2 reforming was easier than that formed in steam reforming under similar conditions. Coke elimination should be done by increasing the reaction temperatures in CO2 reforming while by increasing steam content fed in steam reforming. The optimal CH4/CO2/O-2 feed ratios 1:0.8-1.0:0.1-0.2 through the analysis of thermodynamic equilibrium in the oxidative CO2 reforming were corresponding to the reaction temperature higher than 800 degrees C. Carbon deposition increased with the increase in pressures while a high temperature can suppress this effect. (c) 2008 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:2507 / 2514
页数:8
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