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Centrifugal Pumps, Fans and Compressors  203

































                                FIG. 7.3. Mollier diagram for the complete centrifugal compressor stage.


                          Inlet casing

                            The fluid is accelerated from velocity c 0 to velocity c 1 and the static pressure falls
                          from p 0 to p 1 as indicated in Figure 7.3. Since the stagnation enthalpy is constant
                          in steady, adiabatic flow without shaft work then h 00 D h 01 or,

                                   1 2
                                             1 2
                              h 0 C c D h 1 C c .
                                   2 0       2 1
                          Some efficiency definitions appropriate to this process are stated in Chapter 2.


                          Impeller

                            The general three-dimensional motion has components of velocity c r ,c   , and c x
                                                                              2
                                                                                  2
                                                                                           2
                                                                                       2
                          respectively in the radial, tangential and axial directions and c D c C c C c .
                                                                                  r        x
                            Thus, from eqn. (2.12e), the rothalpy is
                                     1
                                            2
                                        2
                              I D h C .c C c C c 2  2Uc   /.
                                     2  r       x
                                                   2
                                                1
                            Adding and subtracting U this becomes
                                                2
                                     1
                                              2
                                                   2
                                                            2
                              I D h C f.U   c   / C c C c 2  U g.                          (7.1)
                                     2             r   x
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