Page 28 - Advanced Gas Turbine Cycles
P. 28

Chapter 1.  A brief review of power generation thennodynamics   5

        is simply the thermal or cycle efficiency,
                  W
             q"  -
                 QB  '

        where W is the net work output and QB is the heat supplied. Wand QB may be measured for a
        mass of fluid (M) that circulates over a given period of time. Thus, the efficiency may also be
        expressed in terms of the power output (w and the rate of heat transfer (QB),
                  w
             q= -,
                 QB
        and  this  formulation  is  more  convenient  for  a  steady  flow  cycle.  In  most  of  the
        thermodynamic analyses in this book, we shall work in terms of W, QB and mass flow M (all
        measured over a period of time), rather than in terms of the rates W, QB and &f (we call M a
        mass flow and M a mass flow rate).
          The heat supply to the cyclic gas turbine power plant of Fig. 1.2 comes from the control
        surface 2. Within this second control surface, a steady-flow heating device is supplied with
        reactants (fuel and air) and it discharges the products of combustion. We may define a
        second efficiency for the 'heating device' (or boiler) efficiency,

                                                                            (1.3)


        QB is the heat transfer from 2 to the closed cycle within control surface Y, which occurs
        during the time interval that Mf, the mass of fuel, is supplied; and [CV],  is its calorific
        value per unit mass of fuel for the ambient temperature (To) at which the reactants enter.
        F = Mf[CVl0 is equal to the heat (eo) that would be transferred from 2 if the products
        were to leave the control surface at the entry temperature of the reactants, taken as the
        temperature of the environment, To. Fig.  1.7 illustrates the definition of calorific value,


                                           + w=o
                                  -                   - -
                       I-                 t                      I
                                           I
                       II
                                                                 I     Po -To





              H
               RO
                                               --I

                   CONTROL VOLUME             Q,  = M,[CVlo
                       Fig. 1.7. Determination of calorific value [CV], (after Ref. [2]).
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