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Abstract

Three schemes for determination of equilibrium states at prescribed temperature and pressure may be considered, namely, Gibbs function minimization, equilibrium constant formulation, and equating of forward and reverse rates.(1) The first two schemes are well known to be equivalent, “static equilibrium” formulations based on the Gibbs function minimization principle for a mixture at specified temperature and pressure. The third, a “dynamic equilibrium” scheme, is not of practical use, as it is essentially a limiting case of finite-rate kinetics based on infinite reaction time, and therefore has all of the difficulties associated with finite-rate chemistry solutions.

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References

  1. F. J. Zeleznik and S. Gordon, Calculation of complex chemical equilibria, Ind. Eng. Chem. 60, 6 (1968).

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  2. R. F. Anasoulis and H. MacDonald, A Study of Combustor Flow Computations and Comparison with Experiment, Report No. EPA–650/2–73–045, U.S. Environmental Protection Agency (1973).

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  3. S. Gordon and B. McBride, Computer Program for Calculation of Complex Chemical Equilibrium Compositions, NASA SP-273 (1971).

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  4. D. T. Pratt and J. Wormeck, CREK—A Computer Program for Calculation of Combustion Reaction Equilibrium and Kinetics in Laminar or Turbulent Flow, Report WSU-TEL-76–1, Washington State University (1976).

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© 1979 Springer Science+Business Media New York

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Pratt, D.T. (1979). Multicomponent Equilibrium. In: Smoot, L.D., Pratt, D.T. (eds) Pulverized-Coal Combustion and Gasification. Springer, Boston, MA. https://doi.org/10.1007/978-1-4757-1696-2_1

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  • DOI: https://doi.org/10.1007/978-1-4757-1696-2_1

  • Publisher Name: Springer, Boston, MA

  • Print ISBN: 978-1-4757-1698-6

  • Online ISBN: 978-1-4757-1696-2

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