Thermodynamic analysis of hydrogen production by partial oxidation reforming
Department
Mechanical Engineering
Document Type
Article
Publication Title
International Journal of Hydrogen Energy
ISSN
0360-3199
Volume
29
Issue
8
DOI
10.1016/j.ijhydene.2003.09.015
First Page
809
Last Page
816
Publication Date
7-1-2004
Abstract
This paper presents thermodynamic analysis of hydrogen production by partial oxidation reforming. The analysis applies two approximations to the chemistry: global reaction balances and chemical equilibrium. The global reaction analysis provides theoretical upper limits on the process in the form of algebraic expressions involving the steam-to-carbon ratio and the oxygen-to-carbon ratio as process parameters. The equilibrium computations provide a more realistic estimate of the expected product composition and thermal efficiency of the process. The equilibrium predictions are compared to experimental data obtained using a first generation plasmatron reformer operated on diesel fuel. The efficiency of this compact reformer was considerably below the theoretical maximum. © 2003 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.
Recommended Citation
Lutz, A. E.,
Bradshaw, R. W.,
Bromberg, L.,
&
Rabinovich, A.
(2004).
Thermodynamic analysis of hydrogen production by partial oxidation reforming.
International Journal of Hydrogen Energy, 29(8), 809–816.
DOI: 10.1016/j.ijhydene.2003.09.015
https://scholarlycommons.pacific.edu/soecs-facarticles/298