Page 457 - Mechanical Engineers' Handbook (Volume 4)
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446   Refrigeration

                          piston compressors are usually found in household refrigerators and small air conditioners
                          up to inputs of 2 kW. For a fixed-vane, rolling piston rotary compressor, the shaft is located
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                          in the center of the housing while the roller is mounted on an eccentric. Suction gas enters
                          directly into the suction port. As the roller rotates, the refrigerant vapor is compressed and
                          is discharged into the compressor housing through the discharge valve.
                             One difference between a rotary and a reciprocating compressor is that the rotary is able
                          to obtain a better vacuum during suction. 18  It has low reexpansion losses because there is
                          no high-pressure discharge vapor present during suction as with a reciprocating compressor.
                             Because rotary vane compressors have a light weight for their displacement, they are
                          ideal for transportation applications. Rotary vane compressors can be used in applications
                          where temperatures drop down to  40 to  51 C, depending whether it is in a single- or
                          two-stage system. Refrigerants R-22, R-404a, and R-717 are currently used with rotary vane
                          compressors. 18

                          Scroll Compressors
                          The principle of the scroll compressor was first patented in 1905. However, the first com-
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                          mercial units were not built until the early 1980s. Scroll compressors are used in building
                          air-conditioning, heat pump, refrigeration, and automotive air-conditioning applications. They
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                          range in capacity from 3 to 50 kW. Scroll compressors have two spiral-shaped scroll mem-
                          bers that are assembled 180  out of phase (Fig. 10). One scroll is fixed while the other
                          ‘‘orbits’’ the first. Vapor is compressed by sealing vapor off at the edge of the scrolls and
                          reducing the volume of the gas as it moves inward toward the discharge port. Figure 10a
                          shows the two scrolls at the instant that vapor enters the compressor and compression begins.
                          The orbiting motion of the second scroll forces the pocket of vapor toward the discharge
                          port while decreasing its volume (Fig. 10b–10h). In Fig. 10c and f, the two scrolls open at
                          the ends and allow new pockets of vapor to be admitted into the scrolls for compression.
                          Compression is a nearly continuous process in a scroll compressor.
                             Scroll compressors offer several advantages over reciprocating compressors. First, rel-
                          atively large suction and discharge ports can be used to reduce pressure losses. Second, the
                          separation of the suction and discharge processes reduces the heat transfer between the
                          discharge and suction processes. Third, with no valves and reexpansion losses, they have
                          higher volumetric efficiencies. Capacities of systems with scroll compressors can be varied
                          by using variable speed motors or by use of multiple suction ports at different locations
                          within the two spiral members. Fourth, with a smaller number of moving parts, they have
                          the potential to be more reliable and quieter than reciprocating compressors.

                          Screw Compressors
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                          Screw compressors were first introduced in 1958. These are positive displacement machines
                          available in the capacity range from 15 to 1100 kW, overlapping reciprocating compressors
                          for lower capacities and centrifugal compressors for higher capacities. Both twin-screw and
                          single-screw compressors are used for refrigeration applications.
                             Fixed suction and discharge ports, used instead of valves in reciprocating compressors,
                          set the ‘‘built-in volume ratio’’ of the screw compressor. This is the ratio of the volume of
                          fluid space in the meshing rotors at the beginning of the compression process to the volume
                          in the rotors as the discharge port is first exposed. Associated with the built-in volume ratio
                          is a pressure ratio that depends on the properties of the refrigerant being compressed. Peak
                          efficiency is obtained if the discharge pressure imposed by the system matches the pressure
                          developed by the rotors when the discharge port is exposed. If the interlobe pressure is
                          greater or less than discharge pressure, energy losses occur but no harm is done to the
                          compressor.
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