Page 446 - Mechanical Engineers' Handbook (Volume 4)
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4 Refrigerants  435

                           Table 4 Ozone Depletion Potential and Halocarbon Global Warming Potential of Popular
                           Refrigerants and Mixtures a
                                                                           Ozone
                                                                          Depletion    100-yr Global
                                                                          Potential   Warming Potential
                           Refrigerant Number      Chemical Formula        (ODP)          (GWP)
                           Chlorofluorocarbons
                             11               CCl 3 F                      1.0             4,600
                             12               CCl 2 F 2                    1.0            10,600
                             113              CCl 2 FCClF 2                0.80           14,000
                             114              CClF 2 CClF 2                1.0             9,800
                             115              CClF 2 CF 3                  0.6             7,200
                           Hydrochlorofluorocarbons
                             22               CHClF 2                      0.055           1,700
                             123              CHCl 2 CF 3                  0.020            120
                             124              CHClFCF 3                    0.020            620
                             141b             CH 3 CCl 2 F                 0.11             700
                            142b              CH 3 CClF 2                  0.065           2,400
                           Hydrofluorocarbons
                             32               CH 2 F 2                     0                550
                             125              CHF 2 CF 3                   0               3,400
                             134a             CH 2 FCF 3                   0               1,100
                             143a             CH 3 CF 3                    0                750
                             152a             CH 3 CHF 2                   0                 43
                           Hydrocarbons
                             50               CH 4                         0                  0
                             290              CH 3 CH 2 CH 3               0                  0
                           Zeotropes
                             407C             R-32/125/134a (23/25/52%wt)  0               1,700
                             410A             R-32/125 (50/50%wt)          0               2,000
                           Azeotropes
                             500              R-12/152a (73.8/26.2 wt%)    0.74            6,310
                             502              R-22/115 (48.8/51.2 wt%)     0.31            5,494
                           a Compiled from Refs. 4, 15, and 16.


                              Critical temperature and pressure should be well above the operating level. As the
                           critical pressure is approached, less heat is rejected as latent heat compared to the sensible
                           heat from desuperheating the compressor discharge gas, and cycle efficiency is reduced.
                           Methane (R-50) and chlorotrifluoromethane (R-13) are usually cascaded with other refrig-
                           erants because of their low critical points.
                              Suction volume sets the size of the compressor. High suction volumes require centrifugal
                           or screw compressors, and low suction volumes dictate the use of reciprocating compressors.
                           Suction volumes also may influence evaporator design, particularly at low temperatures, since
                           they must include adequate space for gas-liquid separation.
                              Freezing point should be lower than minimum operating temperature. This generally is
                           no problem unless the refrigerant is used as a brine.
                              Theoretical power required for adiabatic compression of the gas is slightly less with
                           some refrigerants than others. However, this is usually a secondary consideration offset by
                           the effects of particular equipment selections, for example, line-pressure drops, etc., on sys-
                           tem power consumption.
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