Binary refrigerating apparatus
A binary refrigerating apparatus employs a refrigerant composition that has a small global-warming potential (GWP) and can be used as a refrigerant capable of achieving a low temperature of −80° C. A refrigerant composition used as a low-temperature-side refrigerant is a refrigerant mixture including a non-azeotropic mixture in which 20% by mass or less of carbon dioxide (R744) is mixed to difluoroethylene (R1132a). A refrigerant composition used as a high-temperature-side refrigerant is a combination of: a non-azeotropic mixture comprising the refrigerant group of difluoromethane (R32), pentafluoroethane (R125), 1,1,1,2-tetrafluoroethane (R134a) and 1,1,3-trifluoro ethane (R143a); and 1,1,1,2,3-pentafluoropentene (HFO-1234ze), having a global-warming potential (GWP) of 1500 or less.
1. A binary refrigerating apparatus comprising:
a high-temperature-side refrigeration circuit; and
a low-temperature-side refrigeration circuit that achieves a refrigerating capacity of −80° C. or lower by condensing a refrigerant in the low-temperature-side refrigeration circuit with a refrigerant passing through a cascade condenser in the high-temperature-side refrigeration circuit,
wherein the refrigerant in the low-temperature-side refrigeration circuit contains a first amount of difluoroethylene (R1132a) and a second amount of hexafluoroethane (R116), and
wherein the first amount of difluoroethylene (R1132a) and the second amount of hexafluoroethane (R116) contained in the refrigerant allow an evaporation temperature of the refrigerant in the low-temperature-side refrigeration circuit to be lower than a boiling point of difluoroethylene (R1132a) and a boiling point of hexafluoroethane (R116).
2. A binary refrigerating apparatus comprising:
a high-temperature-side refrigeration circuit; and
a low-temperature-side refrigeration circuit that achieves a refrigerating capacity of −80° C. or lower by condensing a refrigerant in the low-temperature-side refrigeration circuit with a refrigerant passing through a cascade condenser in the high-temperature-side refrigeration circuit,
wherein the refrigerant in the low-temperature-side refrigeration circuit contains a first amount of difluoroethylene (R1132a) and more than 0% by mass and 20% by mass or less of carbon dioxide (R744), and
wherein the first amount of difluoroethylene (R1132a) and more than 0% by mass and 20% by mass or less of carbon dioxide (R744) contained in the refrigerant allow an evaporation temperature of the refrigerant in the low-temperature-side refrigeration circuit to be lower than a boiling point of difluoroethylene (R1132a) and a boiling point of carbon dioxide (R744).
3. The binary refrigerating apparatus according to claim 1 , wherein the refrigerant in the low-temperature-side refrigeration circuit further contains a third amount of carbon dioxide (R744), and
wherein the first amount of difluoroethylene (R1132a), the second amount of hexafluoroethane (R116), and the third amount of carbon dioxide contained in the refrigerant allow the evaporation temperature of the refrigerant in the low-temperature-side refrigeration circuit to be lower than any boiling points of difluoroethylene (R1132a), hexafluoroethane (R116), and carbon dioxide (R744).
4. The binary refrigerating apparatus according to claim 2 , wherein the refrigerant in the low-temperature-side refrigeration circuit further contains hexafluoroethane (R116).
5. The binary refrigerating apparatus according to claim 4 , wherein the refrigerant in the low-temperature-side refrigeration circuit contains which difluoroethylene (R1132a)/hexafluoroethane (R116)/carbon dioxide (R744)=27.6 to 29.2% by mass/56.8 to 68.4% by mass/4.0 to 14.0% by mass to allow the evaporation temperature of the refrigerant in the low-temperature-side refrigeration circuit to be lower than any of the boiling point of difluoroethylene (R1132a), a boiling point of hexafluoroethane (R116), and the boiling point of carbon dioxide (R744).
6. The binary refrigerating apparatus according to claim 4 , wherein the refrigerant in the low-temperature-side refrigeration circuit contains difluoroethylene (R1132a)/hexafluoroethane (R116)/carbon dioxide (R744)=54.8 to 58.3% by mass/25.2 to 35.7% by mass/8.0 to 18.0% by mass to allow the evaporation temperature of the refrigerant in the low-temperature-side refrigeration circuit to be lower than any of the boiling point of difluoroethylene (R1132a), a boiling point of hexafluoroethane (R116), and the boiling point of carbon dioxide (R744).
7. The binary refrigerating apparatus according to claim 1 , wherein the refrigerant in the low-temperature-side refrigeration circuit contains a ratio of 14% by mass or less of n-pentane with respect to a total mass of the refrigerant in the low-temperature-side refrigeration circuit.
8. The binary refrigerating apparatus according to claim 1 , wherein the refrigerant in the low-temperature-side refrigeration circuit contains a ratio of 14% by mass or less of propane (R290) with respect to a total mass of the refrigerant in the low-temperature-side refrigeration circuit.
9. The binary refrigerating apparatus according to claim 1 , wherein the refrigerant in the low-temperature-side refrigeration circuit contains a non-azeotropic mixture comprising a refrigerant group of difluoromethane (R32), pentafluoroethane (R125), 1,1,1,2-tetrafluoroethane (R134a), and 1,1,3-trifluoroethane (R143a), and 1,1,1,2,3-pentafluoropentene (HFO-1234ze), and having a Global-warming potential (GWP) of 1500 or less.
10. The binary refrigerating apparatus according to claim 1 , wherein the refrigerant in the low-temperature-side refrigeration circuit contains a non-azeotropic mixture comprising a refrigerant group of difluoromethane (R32), pentafluoroethane (R125), 1,1,1,2-tetrafluoroethane (R134a), and 1,1,3-trifluoroethane (R143a), and 1,1,1,2-tetrafluoropentene (HFO-1234yf), and having a Global-warming potential (GWP) of 1500 or less.
11. The binary refrigerating apparatus according to claim 2 , wherein the refrigerant in the low-temperature-side refrigeration circuit contains n-pentane that is mixed in a ratio of 14% by mass or less with respect to a total mass of the refrigerant in the low-temperature-side refrigeration circuit.
12. The binary refrigerating apparatus according to claim 2 , wherein the refrigerant in the low-temperature-side refrigeration circuit contains a ratio of 14% by mass or less of propane (R290) with respect to a total mass of the refrigerant in the low-temperature-side refrigeration circuit.
13. The binary refrigerating apparatus according to claim 2 , wherein the refrigerant in the low-temperature-side refrigeration circuit contains a non-azeotropic mixture comprising a refrigerant group of difluoromethane (R32), pentafluoroethane (R125), 1,1,1,2-tetrafluoroethane (R134a), and 1,1,3-trifluoroethane (R143a), and 1,1,1,2,3-pentafluoropentene (HFO-1234ze), and having a Global-warming potential (GWP) of 1500 or less.
14. The binary refrigerating apparatus according to claim 2 , wherein the refrigerant in the low-temperature-side refrigeration circuit contains a non-azeotropic mixture comprising a refrigerant group of difluoromethane (R32), pentafluoroethane (R125), 1,1,1,2-tetrafluoroethane (R134a), and 1,1,3-trifluoroethane (R143a), and 1,1,1,2-tetrafluoropentene (HFO-1234yf), and having a Global-warming potential (GWP) of 1500 or less.
15. The binary refrigerating apparatus according to claim 2 , wherein the low-temperature-side refrigeration circuit comprises an evaporator having an entrance pipe for the refrigerant, and a temperature of the entrance pipe to the evaporator is about −90.0 C° in operation.