Page 54 - Reciprocating Compressors Operation Maintenance
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Reciprocating  Compressors and Their Applications  4 1


         Multiple-Service Units


           For sound economic  reasons,  process  plants have been installing  fewer
         compressors  to do a given job,  using larger  sizes and no spares. When a
         process  requires  handling of  many  streams,  a  common  occurrence  in
         some types of plants,  machines can be so configured that several  streams
         may be handled by a single driver.
           It  is rare that more than two  services  are handled in a combination of
         centrifugal  casings  having a  common driver. There  are  problems of
         capacity and pressure control, as well as other  factors.
           With  reciprocating  compressors,  greater  flexibility  is  possible  in  the
         number  and  size  of  streams  that  can  be  handled  on  a  single  driver.
         Desired  capacity control is usually more easily  attained as well. As many
         as six separate streams have been handled on large existing  compressors.


         First Cost


           There  is no formula  for establishing  the relative cost  of the centrifugal
         versus the reciprocating  compressor.  If volume, pressure,  k factor, and all
         other  factors  are  the  same,  then  gas  specific  gravity  can  influence  the
         cost  of  the  centrifugal, but  it  will have little  effect  on  the  reciprocating
         compressor.


         Power  Cost

            As  has been  mentioned earlier,  power  cost  throughout the  service  life
         of  a compressor  is many  times the first  cost. While it is possible that the
         more  efficient  machine  may  be  higher  in  original  installed  cost,  the
         power savings over a period  of years will usually quickly pay off the dif-
         ferential  and return a profit  for the remaining  life.
            Except  at  very  low  ratios  of  compression,  the  centrifugal  compressor
         is inherently less efficient  than the reciprocating  compressor.
            Very large  volumes,  low ratios  of compression, and low final pressures
         favor  the centrifugal compressor.  No one today  would think of using  the
         reciprocating  compressor  for  blast  furnace  blowers.  Conversely,  higher
         ratios  of compression  and higher terminal pressures  favor  the  reciprocat-
         ing compressor in other services.
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