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Compressors, Pumps, and Turbines                              217


            Optimum Compression Ratio

            When compressing a gas to a high pressure, the  compressor may be  divided  into
            two or more stages. The pressure ratio per stage for various compressors are given
            in  Table  5.4.  The  pressure  ratio  for  a  compression  stage  is  determined  by  me-
            chanical  considerations  and  is  the  concern  of  mechanical  engineers.  If  the  gas
            temperature rises too high, then the gas must be cooled after  one or more compres-
            sion stages.  This is illustrated  in Figure  5.16  for a centrifugal  compressor, where
            the gas is removed, cooled in an external heat exchanger, called an intercooler, and
            returned to the compressor. The objective is to calculate the number of intercoolers
            because they affect  the work of compression.
                The  minimum work  of compression  is  obtained  if the  compression  is iso-
            thermal. Figure  5.17  illustrates this, where the isothermal work is compared with
            the adiabatic work by  comparing the area under to the left  of the  curves. Thus,
            the  compressor  should be  operated  isothermally, but practically  it is  difficult  to
            remove heat  fast  enough to obtain isothermal operation because the surface  area
            needed  for heat transfer  cannot be  contained  inside the  compressor.  Isothermal
            operation  can be  approached by removing the  gases  from  the  compressor peri-
            odically and cooling the gases in an intercooler, as illustrated in Figure 5.17.
                After  specifying  the  compressor  inlet  and  discharge  pressures,  then  the
            problem is to find the pressure ratio for each stage of compression. A stage may
            contain one or more impellers. We define  a stage of compression as one or more
            impellers  in  series  with  no  intercooler  between  the  impellers.  Thus,  the  com-
            pressor  in Figure  5.16  contains two  stages  and each stage contains three impel-
            lers.  If part of the gases condenses after  cooling, then there will also be a



                           Inlet                        Outlet


                                  L















            Figure  5.16 A  centrifugal  compressor  with  intercooling.  (Source  Ref.
            21).




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