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1400
                                     К         2'                                     3
                                   1200



                                   1000
                                                                                       4


                                    800
                                                           6                  5
                                    600

                                               2
                                 Т
                                    400
                                                                                      4'
                                    200



                                      0
                                        0,5     1,0     1,5    2,0      2,5     3,0  кДж  3,5
                                                        S
                                                                                    кг  К
                              T 1 = 308,2 К; Т 2 = 432,3 К; Т 3 = 1249,2 К; Т 4 = 952,6 К;
                                       S 1 = S 2 = 1,0  кДж  ;   S 3 = S 4 = 3,27   кДж  ;
                                                      кг   К                  кг   К
                               T– is an absolute temperature;   S– is specific entropy.
                       Figure 4.2 - Heat diagram of the Briton cycle  and the Carnot’s cycle


                               5. ENERGY AND ECONOMIC CHARACTERISTICS
                                                    OF THE CYCLES.

                  5.1 The characteristic cycle a gas turbine with regeneration.
            The thermal efficiency of the cycle

                                             t   1     m                                        (5.1)

                                   P                 k 1  
                          where       2  P 1    ,    а     m   k  .


                  The absorbs specific heat energy  by   work fluid

                                              q 1 = C pm·(T 3 – T 2)                                    (5.2)

                  The reject specific heat from WF

                                          q 2 = C pm·(T 1 – T 4)                                             (5.3)

                  The specific work of adiabatic compression of WF

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