Page 45 - Advanced Gas Turbine Cycles
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22                         Advanced gas turbine cycles

              For  an  ‘irreversible’ Carnot  type  cycle  (ICAR) with  all  heat  supplied at  the  top
           temperature  and  all  heat  rejected  at  the  lowest  temperature  (Tmm = T3, Tmin = To,
                = 0,  &;CAR = l), but  with  irreversible  compression  and  expansion  (qcm =
           uB/crA < I), Eqs. (2.33) and (1.17) yield


                                                                               (2.35)


              However, use of Eqs. (2.34) and (2.35) together does not yield Eq. (2.33b) because the
           values of IQ and IF” are not the same in the LTB, JB and ICAR cycles.



           2.4.  The maximum work output in a chemical reaction at To

              The (maximum) reversible work in steady flow between reactants at an entry state
           Ro(po, To) and products at a leaving state Po(po, To) is

                                                                               (2.36)


              It is supposed here that the various reactants entering are separated at (po.To); the
           various products discharged are similarly separated at (po,To). The maximum work may
           then be written as




           where G is the Gibbs function, G = H - TS. This is the maximum work obtainable from
           such a combustion process and is usually used in defining the rational efficiency of an open
           circuit plant. However, it should be noted that if the reactants and/or products are not at
           pressure po, then the work of delivery or extraction has to be allowed for in obtaining the
           maximum possible work from the reactants and products drawn from and delivered to the
           atmosphere. The expression for maximum work has to be modified.
             Kotas [3] has drawn a distinction between the ‘environmental’ state, called the dead
           state by Haywood [ 11,  in which reactants and products (each at po, To) are in restricted
           thermal and mechanical equilibrium with the environment; and the ‘truly or completely
           dead state’, in which they are also in chemical equilibrium, with partial pressures (pk) the
           same  as  those  of  the  atmosphere. Kotas  defines the  chemical exergy  as  the  sum  of
           the maximum work obtained from the reaction with components at po, To, [ - AGO], and
           work extraction and delivery terms. The delivery work term is xkMkRkTo In(po/pk), where
           pk is a partial pressure, and is positive. The extraction work is also xkMkRkTo In( po/pk) but
           is negative.
             In general, we shall not subsequently consider these extraction and delivery work terms
           here, but use [-AGO] as an approximation to the maximum work output obtainable from a
           chemical reaction, since the work extraction and delivery quantities are usually small.
           Their relative importance is discussed in detail by Horlock et al. [4].
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