Page 177 - Subyek Teknik Mesin - Forsthoffers Best Practice Handbook for Rotating Machinery by William E Forsthoffer
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Compressor Best Practices   Best Practice 3 .13
              B.P. 3.13. Supporting Material                       the important concept of an equivalent orifice. Refer to
                                                                   Figure 3.13.2.
                                                                     Given any impeller configuration, specific areas can be re-
              The compressor stage
                                                                   duced to equivalent orifices: the eye or inlet area, the discharge
                                                                   area between any two vanes, the eye seal and the hub or shaft seal.
              To begin our discussion, let us observe a typical compressor  This concept makes it much easier to understand that, for
              stage shown in Figure 3.13.1.                        agiven area, gas flow will change directly proportional to the
                A compressor stage is defined as one (1) impeller, the sta-  differential pressure and the compressor stage. It can be seen in
              tionary inlet and discharge passages known as the inlet guide  Figure 3.13.2 that there is an optimum design velocity for the
              vanes, the diffuser and the seals, namely the eye labyrinth seal  inlet of the impeller and the discharge of the impeller. These
              and the shaft labyrinth seal. Each compressor stage at a given  velocities are controlled by selection of a proper inlet eye area and
              flow and impeller speed will produce a certain amount of head  discharge area based on the impeller flow requirement. Again, the
              (energy) and have a specific stage efficiency. It can be observed
                                                                   concept of an equivalent orifice is helpful in understanding that
              that any dynamic curve (turbo-compressor or pump) has the  the gas velocity is dependent on the geometry of the specific
              characteristic of producing increased energy only at a lower fluid
                                                                   impeller. Also, the process system can be reduced to a simple
              flow assuming the inlet speed and the inlet gas angle are  orifice. In any process, the suction discharge sides of the process
              constant.                                            can be conceived as orifices placed either at the inlet or the dis-
                Before we continue, a few important facts and relationships  charge of the compressor flanges for a given flow condition.
              need to be presented. These relationships are: the definition of  Table 3.13.1 presents the definitions of the facts and re-
              a vector, tip speed, flow as a function of velocity and flow related  lationships necessary for the discussion that follows. Please note
              to conditions and the concept of actual flow. In addition, there is




                                                                                     Fig 3.13.1   The compressor stage and
                                                                                     characteristic curve















































              Fig 3.13.2   Reduce it to an equivalent orifice

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