Page 159 - Subyek Teknik Mesin - Forsthoffers Best Practice Handbook for Rotating Machinery by William E Forsthoffer
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Compressor Best Practices    Be st Practice 3.7

                                                                                       Fig 3.7.9   Screw compressor rotor
                                                                                       profiles




























































                                                                   application, due to the development of high efficiency oil sep-
                                                                   aration coalescers and the lower cost of a flooded-screw type
                                                                   compressor unit. Dry screw compressors should be considered
                  External timing gears required                   for sour process services, since sour gas can cause oil quality
                  Normal compression ratio 5:1                     deterioration, which can result in the need for frequent oil
                  Jacket cooling and/or rotor cooling and liquid injection allows  changes and possible component damage. Facts concerning dry
                  operation up to 288°C (550° F) max ratio = 10:1  P max =  screw compressors are noted in Figure 3.7.10.
                  2,585 kPa (375 PSI) with special screw profile
                  Multi staging may be required to prevent high discharge
                                                   3
                  temperature and rotor deflection 500–68,000 m /hr (300–  Twin screw e oil-flooded
                  40,000 acfm)                                     A twin screw, oil-flooded compressor is shown in Figure 3.7.11
                            1
                  Approximately / 3 speed of centrifugal compressors and 3x  with the major components noted.
                  speed of flooded screw compressors                  The oil-flooded twin screw compressor, which was developed
                  Seals required at each end of screws
                                                                   in the 1960s, has become the most widely used variety.
                                                                   The primary reason for its success is its ability to handle very
              Fig 3.7.10   Dry screw compressor facts              high compression ratios without needing external cooling.
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