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6.5 MORE COMPLEX EXAMPLE OF THE USE OF FTT            133




                                0.8



                                0.7

                                0.6

                                0.5
                                 0.4            η er = 1 – (T C  / T H  )  1/2
                                 0.3
                                 0.2
                                 0.1
                                  0
                                    0.2        0.3     0.4   0.5   0.6  0.7  0.8


               FIGURE 6.9
               Thermal efficiency of power plant compared with that of endoreversible cycle (each square depicts data from
               actual plant).
                                                                                  Data from Bejan (1988).

                  Such considerations can also be applied to other situations; whenever an attempt is made to pro-
               duce power, the whole system should be considered. For example, if an electric motor is being driven
               by a battery, it is necessary to assess the effect of the current on the actual voltage achieved at the
               terminals of the battery, reduced by the internal resistance of the cell and then the voltage drops along
               the leads to the motor. Similarly, the ‘thermostatic’ efficiency of a fuel cell (see Chapter 21) can be
               evaluated by considering the open circuit potential difference of the cell, but this potential is reduced
               when drawing a significant current to achieve maximum power output. Hence, new concepts have been
               introduced that enable a broader view of systems operation to be achieved.



               6.5 MORE COMPLEX EXAMPLE OF THE USE OF FTT
               Ma and Turan (2010) describe an analysis of a class of indirectly fired gas turbine (IFGT) cycles using
               FTT. The system is shown in Fig. 6.10, which depicts a ‘closed cycle’ gas turbine indirectly fuelled
               using biogas. The reason for indirect fuelling is that the biogas might contain corrosive particles that
               could cause erosion of the turbine blades.
                  The operating cycle of the system is shown on a T–S diagram in Fig. 6.11. The basic components of
               this class of cycles are the compressor, high-temperature heat exchangers (HTHEs), combustion
               chamber and a gas turbine as shown in Fig. 6.10. The working fluid, air, enters the compressor at state 1
               and is non-isentropically compressed to state 2. After state 2 (ideally to state 2s), the air leaving the
               compressor enters the HTHE and is heated to state 3 by the high temperature burnt biomass gas flow.
               The heated air then enters the turbine and expands non-isentropically to state 4 (ideally to state 4s).
               After leaving the turbine, the air that is still hot enters the combustion chamber and takes part in the
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