Page 353 - Reciprocating Compressors Operation Maintenance
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338    Reciprocating  Compressors:  Operation and Maintenance


           One day, a situation arose where the  100 HP compressor was shut down
         because it could not produce pressure. The 40 HP machine could not oper-
         ate because of a highly audible noise.
           A  service  person  was  dispatched  to  investigate  the  situation.  The fol-
         lowing are abbreviated entries from  his notebook.


           A. Checked  100 HP unit by opening discharge  valve to pressurized  sys-
              tems  (with  compressor  shut off). Crankcase  pressurized  (single-act-
              ing  compressor)  which indicated bad  discharge  valves  and possibly
              worn or broken piston rings.
           B. Checked  60 HP compressor  by running and blocking off system and
              venting  discharge  to  atmosphere,  while maintaining  100 psig  dis-
              charge pressure. Checked  full-load  amps, which were at 98% design.
              Therefore,  this compressor  at near full  capacity  of 300 CFM.
           C. Checked  50  HP compressor  the  same  as  B,  This  unit  also  at  full
              capacity or 250 CFM.
           D. Checked  40 HP compressor  by running to maximum design  pressure
              (100  psig).  Unit leaked  severely  at  packing  gland  and could  not be
              adjusted  to correct.  Unit also had loud rap or knock. Unit could  not
              develop  100 psig, due to severe leaks.  Required extensive repairs to
              cylinder and running gear.


           Of the total  1250 CFM capacity, system would only produce 550 CFM,
         CAPACITY REQUIREMENT     DETERMINED


           At  lunch time, the  entire plant was  shut down with no  compressed  air
         requirements.  Both  the  60  HP  and  50  HP  compressors  were  placed  in
         operation to pressurize  the system to  100 psig. But, only a maximum pres-
         sure  of  only  60  psig  could  be  attained.  A short  walk  through  the  plant
         revealed air leaks near every air user. The result was that over  100 HP was
         required  to maintain the leaks  in the plant. (If  100 psig  was to have  been
         maintained  during this shutdown, precisely  110 HP was required  to over-
         come the leaks).
           The plant required at least  160 HP of compression  to maintain 100 psig
         during  plant operation.  Without leaks,  however,  this  plant required  only
         40 HP, or about 200 CFM.
           The cost of this wasted energy is easy to calculate.
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