Page 53 - The engineering of chemical reactions
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Reactor Mass Balances  37

                             that in general kinetics are empirically determined. These arguments show that near
                             equilibrium the kinetics of reactions must be consistent with thermodynamic equilibrium
                             requirements.
                                 Note also that the description of a reaction as irreversible simply means that the
                             equilibrium constant is so large that  rr  >>  rb.  The notion of an irreversible reaction is an
                             operational one, assuming that the reverse reaction is sufficiently small compared to the
                             forward reaction so that it can be neglected. It is frequently a good approximation to assume
                             a reaction to be irreversible when  AG:   <<  0.
                                 Returning to the energy diagrams of the previous figure, we see that the difference
                             between  Ef  and  Eb   is the energy difference between reactants and products, which is the
                             heat of the reaction A HR.   The heat of reaction is given by the relation
                                                          AHR   =  CjVjHj
                             where  Hj  is the heat of formation of species j. We necessarily described the energy scale
                             rather loosely, but it can be identified with the enthalpy difference A HR   in a reaction system
                             at constant pressure, an expression similar to that derived from classical thermodynamics.
                                 These relations can be used to estimate rate parameters for a back reaction in
                             a reversible reaction if we know the rate parameters of the forward reaction and the
                             equilibrium properties  AG:  and  AH,.
                                 We emphasize several cautions about the relationships between kinetics and thermo-
                             dynamic equilibrium. First, the relations given apply only for a reaction that is close to
                             equilibrium, and what is “close” is not always easy to specify. A second caution is that
                             kinetics describes the rate with which a reaction approaches thermodynamic equilibrium,
                             and this rate cannot be predicted from its deviation from the equilibrium composition.
                                  A fundamental principle of reaction engineering is that we may be able to find a
                             suitable  catalyst  that will accelerate a desired reaction while leaving others unchanged or
                             an  inhibitor  that will slow reaction rates. We note the following important points about the
                             relations between thermodynamics and kinetics:

                             1. Thermodynamic equilibrium requires that we cannot go from one side of the equilibrium
                               composition to the other in a single process.
                             2. Kinetics predicts the rates of reactions and which reactions will go rapidly or slowly
                               towards  equilibrium.


                             One never should try to make a process violate the Second Law of Thermodynamics, but
                             one should never assume that AG;  alone predicts what will happen in a chemical reactor.

             REACTOR MASS BALANCES

                             We need reaction-rate expressions to insert into species mass-balance equations for a
                             particular reactor. These are the equations from which we can obtain compositions and
                             other quantities that we need to describe a chemical process. In introductory chemistry
                             courses students are introduced to first-order irreversible reactions in the batch reac-
                             tor, and the impression is sometimes left that this is the only mass balance that is im-
                             portant in chemical reactions. In practical situations the mass balance becomes more
                             complicated.
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