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Downstream Chapter  10 409


             Since these forces are produced at or near the rotor mid-span, which coincides
             with the point of maximum rotor deflection, their effect on rotor stability is
             maximized (unless a damper seal design is used). For the conventional straight
             through compressor arrangement, the balance piston is located closer to a bear-
             ing centerline and is often considered to have less of an influence on rotor sta-
             bility compared to a mid-span located back-to-back center seal. If this center
             seal causes the rotordynamics to be unstable or exhibit a low or negative log
             decrement, then other types of center seal designs to reduce aerodynamic exci-
             tation such as the use of shunt holes or swirl breaks can be investigated. If these
             designs are insufficient to suppress an instability then other type seals such as a
             honeycomb or hole pattern seals may be required. The compressor manufac-
             turer experience with all of these designs should be carefully reviewed.



             Centrifugal Compressor Design and Performance
             The behavior of a compressor stage can be characterized in terms of parameters
             which specify its operating conditions as well as its performance. The dimen-
             sionless representation makes it possible to disregard the actual dimensions of
             the machine and its real operating conditions (flow rate and speed of rotation)
             and is thus more general as compared to the use of dimensional quantities.
                Parameters commonly used to describe the performance of centrifugal com-
             pressors are as follows:
                Machine Mach number. The Mach number, M U , is defined as the ratio
             between the machine tip speed and the velocity of sound at the reference
             conditions.
                                              U 2
                                         Mu ¼                          (10.1)
                                              a 0
             where U 2 ¼impeller peripheral speed; A 0 ¼speed of sound at inlet conditions.
                Flow coefficient. The inlet flow coefficient for a centrifugal compressor is
             defined as follows:

                                             4Q
                                       φ ¼    2                        (10.2)
                                        1
                                           π D U 2
             where
                Q¼volume flow
                D¼impeller tip diameter
                U¼impeller tip speed
                Reynolds number. The Reynolds number, Re, is defined as the ratio between
             inertial forces and viscous forces, evaluated in relation to assigned reference
             conditions. For centrifugal machines the following formulation is frequently
             used:
                                           U 2 b 2 ρ 00
                                       Re ¼                            (10.3)
                                              μ 0
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