Page 135 - Subyek Teknik Mesin - Forsthoffers Best Practice Handbook for Rotating Machinery by William E Forsthoffer
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Compressor Best Practices    Be st Practice 3.2
                                                                   Efficiency


                                                                   Compressor efficiency, regardless of the type of compressor, can
                                                                   best be understood by referring to a typical Mollier Diagram as
                                                                   depicted in Figure 3.2.7.
                                                                     All produced heads shown on performance curves (iso-
                                                                   thermal, isentropic and polytropic) represent the ideal
                                                                   reversible head produced to compress a given gas from P 1 to P 2 .
                                                                   This then is the theoretical compression path of the gas. That is,
                                                                   the energy required to compress a gas if the efficiency is 100%.
                                                                     However due to friction, sudden expansion etc., the effi-
                                                                   ciency is less than 100%. Therefore the actual compression path
                                                                   requires more head (energy) to compress the gas from P 1 to P 2 .
                                                                   The efficiency then is equal to:

                                                                                 DE Ideal ðE 2 Ideal-E 1 Þ
                                                                     Efficiency ¼
              Fig 3.2.7   Efficiency                                             DE Actual ðE 2 Actual-E 1 Þ
                                                                     Note that () is used to represent any ideal reversible path
              performance (efficiency) results in decreased compressor re-  (isothermal, isentropic, polytropic).
              liability. One mechanical design problem can quickly offset
              any power savings realized by designing a compressor for a
              higher efficiency.                                    Horsepower
                Referring back to Figure 3.2.6, calculation of specific speed
              for the first impeller by the contractor or end user will give an  Gas Horsepower is defined as the total actual energy (work)
              indication of the type of dynamic compressor blading to be  required to compress a given gas from P 1 to P 2 when
              used. One other comment; Sundstrand Corporation success-  compressing a given mass flow:
              fully employs an integral high speed gear box design for low
              flow, high head applications or for low specific speed    HeadðÞ m   kgf ft   lbf  ðMassFlow   kg=hrðlb=minÞÞ
              applications.                                                  kgm     lbm
                The use of a speed increasing gear box (for speeds up to  3,600 (33,000) (Efficiency) ()
              34,000 RPM) enables the specific speed to be increased, and
              therefore gives higher efficiency and less complexity than  Note: () must be for the same ideal reversible compression
              would be obtained with a multistage compressor design  path. The brake horsepower is the sum of the gas horsepower
              approach.                                            and the mechanical losses of the compressor.





                                                                                       Fig 3.2.8   The Fan Laws






























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