Page 114 - Aeronautical Engineer Data Book
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90      Aeronautical Engineer’s Data Book
      Table 5.4 Isentropic flows


      Pipe flows   –dp  du
                        = M  2
                        � u
      Convergent   Flow velocity u =
      nozzle flows
                                    k
                                     –1


                             0 p
                        k  ��
 ���
 �
�  �
                                   ρ  k
                     2           1 –
                   � � � 1k  –  ρ 0   p  0
                   Flow rate m =  uA
                                      1
                                          �

      Convergent­              �  2   � �
                                           1/k
                                     k– 1  p 0
      divergent            A
                                         p
                                k + 1
                   Area ratio   =
      nozzle flow          A*
                                    �
                             ��
 �
                                       �
                                k –1 �
                                        p �
                                         (1– k)
                                k + 1


                                       p 0 k
                                 1 –

      Table 5.4 shows equations relating to conver­
      gent and convergent-divergent nozzle flow.
      5.6 Compressible 1D flow
      Basic equations for 1D compressible flow are
      Euler’s equation of motion in the steady state
      along a streamline:
                   �
 �
         1   dp  d   1
              +      u  2  = 0
             ds   ds  2
        or
          dp   1
           +     u 2   = constant
        ∫      2
        so:
          k         1
                       2
           RT +   u = constant
         k – 1      2
               T 0
         p 0  ��  k/(k – 1)   �
  k – 1   2 � k/(k – 1)
           =           =  1 + 
  M
         p     T               2
        where T = total temperature.
                0
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