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of the flowing parts of the turbine that is flowed gases with high velocities. In the heat
            exchanger speed gases less, so the rate of erosion less.
                  Secondly,  the  closed-cycle  GTE  work  fluid  pressure  can  be  significantly  higher
            then atmospheric before compressor. This allows to significantly reducing the size of
            compressor, turbine and heat exchanger.
                  Thirdly, the combustion in the combustion chamber of the gas turbine closed type
            can be arranged in such a way as to minimize environmental pollution.



                3. PARAMETERS OF A WORKING FLUID AT THE CHARACTERISTIC

                  3.1  For  the  calculation  it  is  assumed  that  the  state  of  the  working  fluid  (WF)  is
            described  by  the  equation  of  an  ideal  gas  state  and  the  heat  capacity  WF  does  not
            depend at a temperature. Therefore, the unknown value of one of the thermal parameters
            of the working fluid (P,V,T) can be determined from the equation of an ideal gas state
            when the three values are known.

                  3.2  The  relationship  between  the  parameters  of  the  working  fluid  at  the  start
            (P s,V s,T s) and at the end (P e,V e,T e) adiabatic compression process WF is determined by
            the ratios:

                                              k 1
                             T        P       k
                                             
                                    e  T s      e  P s                                                                 (3.1)
                                     
                                           k  1 
                                    T e     s                                                         (3,2)
                                     
                                T       
                                 s      e  
                                            k
                              P          
                                     e      s                                                            (3.3)
                                P        
                                  s      e 

                  The adiabatic constant k for these formulas depends from which gas is the working
            fluid (see Appendix a). These formulas can be used to determine the parameters of the
            WF  in  the  process  of  adiabatic  expansion.  For  isobaric  process  parameters  RT  is
            determined from the equations:


                                                  T    
                                                          s      e                                                   (3.4)
                                                      T
                                                e      s  

                         and the change of entropy:

                                                    T    
                                                  s   C  ln   e                                                                  (3.5)
                                              pm       T
                                                        s  
             where   C pm   - the average specific heat capacity at a constant pressure,  kg J   К 


                  3.3 Determination of the average specific heat capacity at a constant pressure.

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