Page 27 - Reciprocating Compressors Operation Maintenance
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1 4  Reciprocating  Compressors:  Operation and Maintenance
















                                              FIGURE  1-7. Multistage,
                                              double-acting reciprocating
                                              compressor in V-arrangement
                                              (Source:  Sulzer-Burkhardt,
                                              Winterthur,  Switzerland).


           Rotary  motion provided at the compressor  shaft  is converted  to  recip-
         rocating (linear) motion by use of a crankshaft, crosshead,  and a connect-
         ing rod between the two.
           One end of the connecting rod is secured by the crankpin to the crank-
         shaft,  and  the  other  by  crosshead  pin  to  the  crosshead  which,  as  the
         crankshaft  turns, reciprocates  in a linear  motion.
           Intake  (suction)  and  discharge  valves  are  located  in the  top  and bot-
         tom of the cylinder.  (Sometimes  they may be located  in the cylinder  bar-
         rel.)  These  are  basically  check  valves,  permitting  gas  to  flow  in  one
         direction only.
           The  movement of  (he piston  to the  top  of  the  cylinder  creates  a partial
         vacuum  in the lower end of the cylinder; the pressure  differential between
         intake  pressure  and  this  vacuum across  the  intake  valve  then  causes  the
         valves to open, allowing air to flow into the cylinder from the intake line.
           On the return  stroke, when the pressure in the cylinder exceeds the  pres-
         sure  in the  discharge  line, the  discharge  valve opens,  permitting air  at that
         pressure to be discharged from  the cylinder into the discharge or system line.
           This action,  when on one side  of the piston  only, is called "single-act-
         ing" compression; when on both  sides  of the piston, it is called "double-
         acting" compression.




           Determining  compressor  capacity  would be relatively  simple  if  a  non-
         compressible, non-expandable fluid were handled. The quantity into the dis-
         charge line would be practically equal to the volume swept by the piston.
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