Page 34 - Reciprocating Compressors Operation Maintenance
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Reciprocating  Compressors and Their Applications  21


         PISTON RING  LEAKAGE


           This  leakage  allows gas from  the compression  chamber  to escape  past
         the piston into the other end of the cylinder, which is taking suction with
         the  inlet valve open.  Capacity  is  reduced  because  this  hot  leakage  gas
         heats up the incoming gas in that end of the cylinder.
           Naturally,  maximum piston  leakage  occurs  as  the  piston  approaches
         the end of its stroke because differential  pressure  across  the rings and the
         time  element  are  the  greatest  at this  point. This  leakage  causes  both  a
         volumetric  and  a  horsepower  loss  as  evidenced  by  an  increase  in dis-
         charge temperatures.

         VALVE  SLIP


           Valve  slip  means  reversed  gas  flow  through  the  valves  before they
         have had time to seat at the end of the piston  stroke.  Obviously, this vol-
         ume  loss  can occur through both  intake and discharge  valves. Minimum
         slippage  occurs  in  a  responsive  valve; one  that has  minimum inertia so
         that the moving element can easily be controlled  by air flow.
            Slippage  is usually much less through intake  valves than through  dis-
         charge valves. In the latter, differential pressure  across  the valve  increas-
         es rapidly as the piston reaches  dead  center,  so that if the valve does  not
         respond  instantaneously, high  pressure  gas  naturally returns through the
         valve before it seats.

         EFFECTS OF MULTISTAGING


            Multistaging  has  a  marked  effect  on  volumetric  efficiency. Here,  the
         low  pressure cylinder largely determines  the entire  machine's  volumetric
         efficiency  because  whatever volume this cylinder  delivers  to  succeeding
         stages  must be  discharged,  with the  exception  of  slight  leakage  that
         occurs through packing boxes.
            In  other  words,  volumetric efficiency  of  a  two-stage  machine  is  the
         same  as  if  the  low  pressure  cylinder  were  a  single-stage  compressor
         delivering gas at intercooler pressure.
            Figure  1-12 shows the  pV combined  diagram  of a two-stage  100 psig
         air  compressor. Further stages  are  added  in the  same manner. In a  recip-
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