REFRIGERANT COMPOSITIONS FOR REFRIGERANT COMPRESSOR SYSTEMS

1 . A refrigeration system, comprising:

a hermetic compressor;

and a refrigerant composition;

wherein the refrigerant composition comprises:

difluoromethane (R-32) present in an amount of 16 to 18 weight percent, 2,3,3,3-tetrafluoropropene (R-1234yf) present in an amount of 79 to 83 weight percent, and propane (R-290) present in an amount of 1.0 to 4.0 weight percent passed on the weight of the refrigerant composition.

2 . The refrigeration system of claim 1 , wherein said hermetic compressor is a rotary, scroll, or reciprocating compressor.

3 . The refrigeration system of claim 1 , wherein said hermetic compressor is a medium back pressure (MBP) or a low back pressure compressor (LBP).

4 . (canceled)

5 . (canceled)

6 . (canceled)

7 . The refrigeration system of claim 1 , wherein the propane is present in an amount of 0.5 to 1.0 weight percent based on the weight of the refrigerant composition.

8 . The refrigeration system of claim 1 , further comprising a non-refrigerant compound in an amount of 0.01 to 49 weight percent based on the weight of the refrigerant composition.

9 . The refrigeration system of claim 7 , wherein the non-refrigerant compound includes a lubricant selected from the group consisting of mineral oil, alkylbenzene, polyol esters, polyalkylene glycols, polyvinyl ethers, polycarbonates, perfluoropolyethers, silicones, silicate esters, phosphate esters, paraffins, naphthenes, polyalpha-olefins, and combinations thereof.

10 . The refrigeration system of claim 1 :

further comprising an evaporator;

wherein the average evaporator temperature is below −5° C.

11 . The refrigeration system of claim 1 :

wherein the compressor discharge temperature is below the compressor discharge temperature of R-457A at the same operating conditions.

12 . The refrigeration system of claim 1 :

wherein the compressor discharge temperature is below the compressor discharge temperature of R-454C at the same operating conditions.

13 . The refrigeration system of claim 1 :

wherein the refrigerant composition has burning velocity less than 10 cm/s.

14 . A method of replacing a first refrigerant composition comprising R-404A, R-457A, R-290, or R-454C with a second refrigerant composition comprising 79 to 83 weight percent 2,3,3,3-tetrafluoropropene, 16 to 18 weight percent difluoromethane, and 1.0 to 4.0 weight percent propane, wherein the replacing is performed in a refrigeration system including a hermetic compressor.

15 . The method of claim 14 , wherein the second refrigerant composition further comprises a non-refrigerant compound in an amount of 0.01 to 50 weight percent based on the weight of the refrigerant composition.

16 . The method of claim 15 , wherein the non-refrigerant compound includes a lubricant selected from the group consisting of mineral oil, alkylbenzene, polyol esters, polyalkylene glycols, polyvinyl ethers, polycarbonates, perfluoropolyethers, silicones, silicate esters, phosphate esters, paraffins, naphthenes, polyalpha-olefins, and combinations thereof.

17 . The method of claim 14 , wherein the compressor discharge temperature is below the compressor discharge temperature of R-457A.

18 . A method of operating a hermetic compressor as part of a refrigeration system, comprising the steps of:

receiving by a hermetic compressor a refrigerant composition including difluoromethane, 2,3,3,3-tetrafluoropropene, and propane;

compressing by a hermetic compressor the refrigerant composition;

wherein the discharge temperature of the compressor is between 80.0° C. and 100.0° C.

19 . The method of claim 18 , wherein the hermetic compressor receives the refrigerant composition from an evaporator having an average evaporator temperature between −40° C. and −5° C.

20 . The method of claim 18 , wherein the hermetic compressor receives the refrigerant composition from an evaporator having an average evaporator temperature between −40° C. and −18° C.

21 . The method of claim 18 , wherein the difluoromethane is present in an amount of 15 to 20 weight percent based on the weight of the refrigerant composition, the 2,3,3,3-tetrafluoropropene is present in an amount of 72 to 83 weight percent based on the weight of the refrigerant composition, and the propane is present in an amount of 1.0 to 10 weight percent based on the weight of the refrigerant composition.

22 . The method of claim 18 , wherein the discharge temperature of the compressor is between 81.0° C. and 99.0° C.

23 . The method of claim 18 , wherein the discharge temperature of the compressor is between 90° C. and 100.0° C.

24 . The method of claim 18 :

further comprising the step of receiving by the hermetic compressor the refrigerant composition from an evaporator;

wherein the average evaporator temperature is below −5° C.

25 . The method of claim 24 , wherein the average evaporator temperature is between −40° C. and −5° C.

26 . (canceled)

27 . (canceled)

28 . (canceled)