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Screw Compressors Chapter  6 259



               TABLE 6.1 Pocket Passing Frequency of Different Screw Compressor Types

                                Small Dry      Large Dry       Oil-Flooded
                                Screw          Screw           Screw
               Compressor Type  Compressor     Compressor      Compressor
               Male-rotor speed  18,000        3000            3600
               (rpm)
               Number of lobes on  4           4               5
               male rotor
               Number of working  72,000       12,000          18,000
               cycles per minute
               Pocket passing   1200           200             300
               frequency (Hz)



                The thermodynamic behavior of screw compressors is similar to recip-
             rocating compressors. The power consumption is nearly independent of the
             gas molecular weight. The inlet gas volume flow does not change much
             when the pressure ratio or the molecular weight of the gas changes. There-
             fore, screw compressors do not have a surge line. Due to the insensitivity
             against mole weight changes a screw compressor can operate with a variety
             of gases.
                A screw compressor can operate at very high-pressure ratios as long as the
             allowable discharge temperature or mechanical limits like bearing loads or shaft
             stress limits are not exceeded. With oil-flooded screw compressors pressure
             ratios of as high as 25 in one stage can be achieved. With dry screw compressors
             a pressure ratio up to 10 is possible with liquid injection.
                The compact rotor design with a small number of lobes gives a robust rotor.
             The first lateral critical speed is always higher than the maximum allowable
             speed (“stiff rotor design”). Due to the purely rotating motion the vibrations
             of screw compressors are similar to centrifugal compressors and much lower
             than for reciprocating compressors. While vibration in the machine itself is pos-
             sible (due to imbalance, bearing failure, torsional resonance, etc.), vibration in a
             screw compressor package (piping, vessels, baseframe, etc.) is much more
             likely to come from the effects of gas pulsations than from the motion of the
             compressor itself.
                The clearances between the rotors and the casing are only fractions of a mil-
             limeter which means that any buildup of process gas residues is scraped away
             and the balance status of the rotors is not affected.
                In contrast to reciprocating compressors screw compressors do not have
             valves for controlling the gas inlet and outlet of the working chamber. The
             gas inlet and outlet are controlled by ports in the casing. Therefore, failure
             of valves is not an issue with screw compressors.
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