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Production of fuel-cell grade hydrogen by thermal swing sorption enhanced reaction concept
被引:36
|作者:
Lee, Ki Bony
[1
]
Beaver, Michael G.
[1
]
Caram, Hugo S.
[1
]
Sircar, Shivaji
[1
]
机构:
[1] Lehigh Univ, Dept Chem Engn, Bethlehem, PA 18015 USA
关键词:
hydrogen;
fuel-cell grade;
sorption enhanced reaction;
thermal swing sorption;
chemisorption;
promoted hydrotalcite;
equilibrium model;
D O I:
10.1016/j.ijhydene.2007.10.018
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:
The performance of a novel thermal swing sorption enhanced reaction (TSSER) concept for production of fuel-cell grade hydrogen (<20ppm CO) by low temperature (similar to 490 degrees C) catalytic steam-methane reforming (SMR) is simulated. The process simultaneously carries out the SMR reaction and removal Of CO2 from the reaction zone by chemisorption on K2CO3 promoted hydrotalcite in a single unit. The chemisorbent is periodically regenerated by steam purge at similar to 590 degrees C. The concept efficiently utilizes the CO2 sorption capacity of the chemisorbent and requires a relatively low amount of steam for its regeneration. A compact, small foot-print H-2 generator can be designed for a residential or industrial hydrogen fuel-cell unit by the concept. Recently measured equilibrium isotherms and column dynamics for ad(de)sorption of CO2 on the chemisorbent are reviewed and parametric evaluations of design variables like catalyst: sorbent ratio and feed gas conditions (pressure, temperature, and H2O: CH4 ratio) are carried out. (C) 2007 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.
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页码:781 / 790
页数:10
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