Biogas upgrading for on-board hydrogen production: Reforming process CFD modelling

被引:18
|
作者
Hamedi, M. R. [1 ]
Tsolakis, A. [1 ]
Lau, C. S. [1 ]
机构
[1] Univ Birmingham, Sch Mech Engn, Birmingham B15 2TT, W Midlands, England
关键词
Biogas upgrade; Fuel reforming; Hydrogen; CFD; Reaction kinetics; PARTIAL OXIDATION; METHANE; DIESEL; GAS; ENGINE; SIMULATION; H-2;
D O I
10.1016/j.ijhydene.2014.06.017
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
Hydrogen production through fuel reforming can be used to improve IC (internal combustion) engines combustion characteristics and to lower vehicle emissions. In this study, a computational fluid dynamics (CFD) model based on a detailed kinetic mechanism was developed for exhaust gas reforming of biogas to synthetic gas (H-2 and CO). In agreement with experimental data, the reactor's physical and chemical performance was investigated at various O-2/CH4 ratios and gas hourly space velocities (GHSV). The numerical results imply that methane reforming reactions are strongly sensitive to O-2/CH4 ratio and engine exhaust gas temperature. It was also found that increasing GHSV results in lower hydrogen yield; since dry and steam reforming reactions are relatively slow and are both dependent on the flow residence time. Furthermore, the hot spot effect, which is associated to oxidation reforming reactions, was investigated for catalyst activity and durability. Copyright (C) 2014, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:12532 / 12540
页数:9
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