Investigation of a Dual-Bed Autothermal Reforming of Methane for Hydrogen Production

被引:10
作者
Arpornwichanop, Amornchai [1 ]
Wasuleewan, Manatsanan [1 ]
Patcharavorachot, Yaneeporn [1 ]
Assabumrungrat, Suttichai [1 ]
机构
[1] Chulalongkorn Univ, Dept Chem Engn, Fac Engn, Bangkok 10330, Thailand
来源
PRES 2011: 14TH INTERNATIONAL CONFERENCE ON PROCESS INTEGRATION, MODELLING AND OPTIMISATION FOR ENERGY SAVING AND POLLUTION REDUCTION, PTS 1 AND 2 | 2011年 / 25卷
关键词
PARTIAL OXIDATION; CATALYST BED; PERFORMANCE;
D O I
10.3303/CET1125155
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper presents a performance analysis of a dual-bed autothermal reformer of methane for hydrogen production. The first section of Pt/Al2O3 catalyst is designed for oxidation reaction, whereas the second one involves steam reforming reaction based on Ni/MgAl2O4 catalyst. A one dimensional, non-isothermal reactor model was employed to examine the reformer performance regarding important operating conditions such as H2O/CH4 feed ratio; O-2/CH4 feed ratio, temperature and location of steam feed. The simulation results indicate that when the dual-bed reformer was operated at the H2O/CH4 feed ratio of 1.0-2.0 and O-2/CH4 feed ratio of 0.45-0.60, the methane conversion of 93% and the H-2/CO product ratio of higher than 2.9 were obtained. In addition, it was found that adding steam at lower temperatures to the steam reforming section of the dual-bed reformer can produce the synthesis gas with a higher H-2/CO ratio.
引用
收藏
页码:929 / 934
页数:6
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