Research trends: Effects of the water-gas shift reaction on MCFC performance

M. H. Kim, H. K. Park, G. Y. Chung, H. C. Lim, S. W. Nam, T. H. Lim, S. A. Hong

Research output: Contribution to specialist publicationArticle

1 Citation (Scopus)

Abstract

Simulation results for MCFC temperature and voltage distribution, conversion and performance, including and excluding the water-gas shift reaction, were compared. The shift reaction caused the temperature profile to become non-uniform. At the entrance, hydrogen was consumed rapidly to reach equilibrium in the shift reaction. Hydrogen conversion decreased along the gas flow because of hydrogen generated by the shift reaction. Therefore, hydrogen conversion was higher than in a practical cell when the shift reaction is excluded. At the same current density, the voltage calculated without the shift reaction would be higher than the "real" value. The effect of the shift reaction on voltage distribution and cell performances was quite small. This is an abstract of an article originally published in J. of Power Stations 103(2) 245-252 (1 January 2002).

Original languageEnglish
Pages245-252
Number of pages8
Volume2002
No.5
Specialist publicationFuel Cells Bulletin
Publication statusPublished - 2002 May

ASJC Scopus subject areas

  • Renewable Energy, Sustainability and the Environment
  • Energy Engineering and Power Technology
  • Strategy and Management

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    Kim, M. H., Park, H. K., Chung, G. Y., Lim, H. C., Nam, S. W., Lim, T. H., & Hong, S. A. (2002). Research trends: Effects of the water-gas shift reaction on MCFC performance. Fuel Cells Bulletin, 2002(5), 245-252.