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CHAPTER TEN



              Entropy and chemical equilibrium










                   10.1 Introduction
                   Many practical applications involve complex processes with numerous
              chemical reactions, e.g., combustion of fuel, gasification of biomass, steam
              reforming of hydrocarbons. The byproducts of the reactions often consist of
              several substances. The product of biomass gasification, as an example, is a
              mixture of mainly H 2 , CO, CO 2 ,CH 4 , and H 2 O with trace of other heavy
              hydrocarbons such as C 2 H 4 ,C 2 H 6 ,C 6 H 6 [1]. To correctly and accurately
              predict the gasification process, one needs to account for various transport
              mechanisms coupled with the kinetics of the reactions involved. Develop-
              ment of a mathematical model that includes these effects and the numerical
              solution of such models is a challenging task, but the outcome is rewarding.
                 A solution of a coupled transport-kinetic model applied to a reactive flow
              allows prediction of species concentrations, temperature, and velocity along
              the flow path. For instance, the predicted composition of the gasification
              products, also called producer gas, using such models is shown to be highly
              accurate [2,3]. It is important to realize that the transport-kinetic models rest
              on the laws of nature—the primary reason for their high accuracy. The
              transport equations are indeed analytical expressions of the conservation
              laws. The kinetic models that are employed to predict the rates of formation
              or consumption of chemical compounds are also based on experimental
              observations.
                 Now the question is whether one may determine the composition of a
              chemical reaction at the state of chemical equilibrium by mere laws of ther-
              modynamics. This problem was investigated in the late 19th century by
              Gibbs, and later by Nernst who examined the theory of Gibbs through a
              limited number of experiments. The criterion proposed by Gibbs postulates
              that at chemical equilibrium the Gibbs energy of a system maintained at
              fixed temperature and pressure is a minimum.

                                           dG ¼ 0                        (10.1)

                                                          © 2020 Elsevier Inc.
              Entropy Analysis in Thermal Engineering Systems              149
              https://doi.org/10.1016/B978-0-12-819168-2.00010-6  All rights reserved.
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