Page 138 - Subyek Teknik Mesin - Forsthoffers Best Practice Handbook for Rotating Machinery by William E Forsthoffer
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Be st Practice 3 .3           Compressor Best Practices

                                                                                  Fig 3.3.4   Compressor impellers




















                                                                                 Fig 3.3.5   Enclosed impellers (Courtesy
                                                                                 of IMO Industries, Inc.)




























       welding, brazing, etc.) today make possible the use of enclosed  inlet flow (rated flow) the head required by the process is in
       first stage impellers for all multistage compressor applications.  equilibrium with the head produced by the compressor.
       Finally, radial bladed impellers (whether open or enclosed)  Vendor calculation methods then determine how many
       produce an extremely flat (almost horizontal) head curve. This  compressor impellers are required based on mechanical limita-
       characteristic renders these impellers unstable in process sys-  tions (stresses) and performance requirements (quoted overall
       tems that do not contain much system resistance. Therefore,  efficiency). Once the head required per stage is determined, the
       radial impellers are to be avoided in process systems that do not  compressor speed is optimized for highest possible overall effi-
       contain much system resistance (plant and instrument air  ciency using the concept of specific speed as shown in
       compressors, charge gas compressors and refrigeration applica-  Figure 3.3.6.
       tions with side loads).                                It is a proven fact that the larger the specific speed, the higher
                                                            the attainable efficiency. As shown, specific speed is a direct
       Enclosed impellers                                   function of shaft speed and volume flow and an inverse function
       Enclosed impellers are shown in Figure 3.3.5.        of produced head. Since the vendor at this point in the design
          Note that the first stage impeller in any multistage configu-  knows the volume flow and head produced for each impeller,
       ration is always the widest. That is, it has the largest flow pas-  increasing the shaft speed will increase the specific speed and
       sage. As a result, the first stage impeller will usually be the  the compressor efficiency.
       highest stressed impeller. The exception is a refrigeration  However, the reader is cautioned that all mechanical design
       compressor with side loads (economizers).            aspects (impeller stress, critical speeds, rotor stability, bearing
          Dynamic compressor vendors use a specific speed to select  and seal design) must be confirmed prior to acceptance of
       impellers based on the data given by the contractors and end  impeller selection. Often, too great an emphasis on perfor-
       user. The vendor is given the total head required by the process  mance (efficiency) results in decreased compressor reliability.
       and the inlet volume flow. As previously discussed, at the stated  One mechanical design problem can quickly offset any power

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