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Chapter 4: Compressors    4-9
                               The main advantage of the multistage reciprocating piston compressor is the positive
                               control of both the volumetric flow rate, which can be put  through the machine, and
                               the pressure of the  output.    Many  reciprocating  piston  compressors  allow  for  the
                               rotation to be adjusted, thus, changing the throughput of air or gas.   Also,  provided
                               there  is  adequate  input  power  from  the  prime  mover,  reciprocating  piston
                               compressors can adjust to  any back pressure  changes  and  maintain  proper  rotation
                               speed (which in turn maintains a given volumetric flow rate).
                                    The main advantage of this  subclass  of  compressor  is  their  extremely  high
                               pressure output capability and reliable volumetric flow rates (see Figures 4-2 and 4-
                               3).   The main disadvantage to  multistage  reciprocating  piston  compressors  is  that
                               they can not be practically constructed in  machines capable of volumetric flow rates
                               much beyond 1,000  actual  cfm.    Also,  the  higher-capacity  compressors  are  rather
                               large and bulky and generally require more maintenance than similar capacity rotary
                               compressors.    In  any  positive  displacement  compressor,  like  a  liquid  positive
                               displacement pump, the real volume flow rate is slightly smaller than the mechanical
                               displacement volume.  This is due to the following factors:
                                   • Pressure drop on the suction side
                                   • Heating up of the intake air
                                   • Internal and external leakage
                                   • Expansion of the gas trapped in the clearance volume (reciprocating piston
                                    compressors only)
                                   Reciprocating  compressors  can  be  designed  with  multiple  stages.    Such
                               multistage compressors are designed with  nearly equal compression ratios  for  each
                               stage (it can be  shown  that  equal  stages  of  compression  lead  to  minimum  input
                               power requirements).  Thus, since the volumetric flow rate (in actual cfm) is  reduced
                               from one stage to  the next,  the volume  displacement  of  each  stage  (its  geometric
                               size) is progressively smaller.

                                 4.4.2 Rotary Compressors
                                   Another important positive displacement compressor is  the  rotary  compressor.
                               This  type of compressor is  usually of rather simple  construction, having no valves
                               and being lightweight.  These compressors are constructed to handle volumetric flow
                               rates up to around 2,000 actual cfm and pressure ratios up to  around 15 (see Figure
                               4-2). Rotary compressors are available in  a  variety  of  designs.    The  most  widely
                               used rotary compressors are the sliding vane, helical lobe (screw), and liquid piston.
                                   The most  important characteristic of this  type of compressor is  that all have  a
                               fixed, built-in, compression  ratio for each stage of compression (as well as a fixed,
                               built-in  volume displacement) [1].   Thus,  at a given rotational speed  (provided  by
                               the prime mover), there will  be  a  predetermined  volumetric  flow  rate  through  the
                               compressor (the geometry of the compressor inlet is  fixed), and the pressure at  the
                               outlet will be equal to the built-in design pressure ratio of the machine multiplied by
                               the inlet pressure.
                                   The upper pressure versus volume plot in Figure 4-9 shows the typical situation
                               when the back pressure on the outlet side of the compressor is  equal to  the built-in
                               design output pressure.  Under these conditions, there  is  no  expansion  of  the  output
                               gas as it exits the compressor  and  passes through  the expansion tank and continues
                               into the initial portion of the pipeline [1].
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