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16 Fluid Mechanics, Thermodynamics of Turbomachinery
                          Stagnation temperature and pressure

                            If the fluid is a perfect gas, then h D C p T, where C p D 
R/.
  1/, so that the
                          stagnation temperature can be defined as

                                       1 2
                              T 0 D T C c /C p ,
                                       2
                                               c 2
                              T 0      1                 1        2
                                 D 1 C .
   1/     D 1 C .
   1/M ,                      .1.13a/
                               T       2       
RT       2
                                                           p
                          where the Mach number, M D c/a D c/ 
RT.
                            The Gibb’s relation, derived from the second law of thermodynamics (see
                          Chapter 2), is
                                         1
                              Tds D dh    dp.


                          If the flow is brought to rest both adiabatically and isentropically (i.e. ds D 0), then,
                          using the above Gibb’s relation,

                                           dp
                              dh D C p dT D  RT
                                           p
                          so that
                              dp    C p dT    
   dT
                                 D        D         .
                               p    R T     
   1 T
                          Integrating, we obtain

                              ln p D ln constant C   ln T,
                                                
  1

                          and so,
                                         
/.
 1/                
/
 1
                              p 0    T 0              
   1  2
                                 D             D  1 C      M                             (1.13b)
                               p     T                  2
                          From the gas law density,   D p/.RT/, we obtain   0 /  D .p 0 /p/.T/T 0 / and hence,
                                         1/.
 1/                1/.
 1/
                                0    T 0              
   1  2
                                 D             D  1 C      M         .                   (1.13c)
                                     T                  2


                          Compressible fluid analysis

                            The application of dimensional analysis to compressible fluids increases, not unex-
                          pectedly, the complexity of the functional relationships obtained in comparison with
                          those already found for incompressible fluids. Even if the fluid is regarded as a
                          perfect gas, in addition to the previously used fluid properties, two further char-
                          acteristics are required; these are a 01 , the stagnation speed of sound at entry to
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