Heat transfer compositions, methods, and systems
The present invention relates to a refrigerant composition, including trifluoroiodomethane (CF 3 I); 1,3,3,3-tetrafluoropropene (HFO-1234ze); difluoromethane (HFC-32), and pentafluoroethane (HFC-125) for use in a heat exchange system, including refrigeration applications and in particular aspects to the use of such compositions as a replacement of the refrigerant R-22 or R-404A for heating and cooling applications and to retrofitting heat exchange systems, including systems designed for use with R-22 or R-404A.
1. A refrigerant comprising at least about 97% by weight of the following four compounds, with each compound being present in the following relative percentages: 36.8 to 72% by weight trifluoroiodomethane (CF 3 I);
2 to 36% by weight of tetrafluoropropene selected from trans-1,3,3,3-tetrafluoropropene (HFO-1234ze(E), 2,3,3,3-tetrafluoropropene (HFO-1234yf) and combinations of these;
15 to 31% by weight difluoromethane (HFC-32); and
1 to 4.5% by weight pentafluoroethane (HFC-125).
2. The refrigerant of claim 1 consisting essentially of the following four compounds, with each compound being present in the following relative percentages:
36.8 to 64.8% by weight trifluoroiodomethane (CF 3 I);
8 to 36% by weight trans-1,3,3,3-tetrafluoropropene (HFO-1234ze(E));
17 to 23% by weight difluoromethane (HFC-32); and
1 to 4.2% by weight pentafluoroethane (HFC-125).
3. The refrigerant of claim 1 consisting essentially of the following four compounds, with each compound being present in the following relative percentages:
about 58% by weight trifluoroiodomethane (CF 3 I);
about 16% by weight trans-1,3,3,3-tetrafluoropropene (HFO-1234ze(E));
22±1% by weight difluoromethane (HFC-32); and
4±0.5% by weight pentafluoroethane (HFC-125).
4. The refrigerant of claim 1 consisting of the following four compounds, with each compound being present in the following relative percentages:
about 58% by weight trifluoroiodomethane (CF 3 I);
about 16% by weight trans-1,3,3,3-tetrafluoropropene (HFO-1234ze(E));
22±1% by weight difluoromethane (HFC-32); and
4±0.5% by weight pentafluoroethane (HFC-125).
5. The refrigerant of claim 1 consisting essentially of the following four compounds, with each compound being present in the following relative percentages:
about 42 to about 60% by weight trifluoroiodomethane (CF 3 I);
about 12 to about 30% by weight trans-1,3,3,3-tetrafluoropropene (HFO-1234ze(E));
about 18 to about 20% by weight difluoromethane (HFC-32); and
2 to 4.2% by weight pentafluoroethane (HFC-125), wherein said refrigerant is non-flammable and has a GWP of 400 or less.
6. The refrigerant of claim 1 consisting of the following four compounds, with each compound being present in the following relative percentages:
about 42 to about 60% by weight trifluoroiodomethane (CF 3 I);
about 12 to about 30% by weight trans-1,3,3,3-tetrafluoropropene (HFO-1234ze(E));
about 18 to about 20% by weight difluoromethane (HFC-32); and
2 to 4.2% by weight pentafluoroethane (HFC-125), wherein said refrigerant is non-flammable and has a GWP of 400 or less.
7. The refrigerant of claim 1 comprising at least about 98.5% by weight of the following four compounds, with each compound being present in the following relative percentages:
46 to 72% by weight trifluoroiodomethane (CF 3 I);
2 to 28% by weight 1,1,1,2-tetrafluoropropene (HFO-1234yf);
15 to 21.5% by weight difluoromethane (HFC-32); and
1 to 4.5% by weight pentafluoroethane (HFC-125).
8. The refrigerant of claim 1 comprising at least about 98.5% by weight of the following four compounds, with each compound being present in the following relative percentages:
about 50 to about 68% by weight trifluoroiodomethane (CF 3 I);
about 6 to about 24% by weight 1,1,1,2-tetrafluoropropene (HFO-1234yf);
about 18 to about 21% by weight difluoromethane (HFC-32); and
2 to 4.5% by weight pentafluoroethane (HFC-125).
9. The refrigerant of claim 1 comprising at least about 98.5% by weight of the following four compounds, with each compound being present in the following relative percentages:
about 53% by weight trifluoroiodomethane (CF 3 I);
about 23% by weight 1,1,1,2-tetrafluoropropene (HFO-1234yf);
20±1% by weight difluoromethane (HFC-32); and
4±0.5% by weight pentafluoroethane (HFC-125).
10. The refrigerant of claim 1 consisting essentially of the following four compounds, with each compound being present in the following relative percentages:
about 53% by weight trifluoroiodomethane (CF 3 I);
about 23% by weight 1,1,1,2-tetrafluoropropene (HFO-1234yf);
20±1% by weight difluoromethane (HFC-32); and
4±0.5% by weight pentafluoroethane (HFC-125).
11. The refrigerant of claim 1 consisting essentially of the following four compounds, with each compound being present in the following relative percentages:
about 50 to about 68% by weight trifluoroiodomethane (CF 3 I);
about 6 to about 24% by weight 1,1,1,2-tetrafluoropropene (HFO-1234yf);
about 18 to about 21% by weight difluoromethane (HFC-32); and
2 to 4.5% by weight pentafluoroethane (HFC-125), wherein said refrigerant is non-flammable and has a GWP of 400 or less.
12. A heat transfer composition comprising the refrigerant of claim 1 .
13. The heat transfer composition of claim 12 , wherein the refrigerant comprises greater than 40% by weight of the heat transfer composition.
14. The heat transfer composition of claim 13 further comprising a stabilizer selected from an alkylated naphthalene, a diene-based compound, a phenol compound and combinations of two or more of these and further comprising a lubricant selected from the group consisting of polyol esters (POEs), mineral oil, alkylbenzenes (ABs) and polyvinyl ethers (PVE).
15. A method for transferring heat of the type comprising evaporating refrigerant liquid to produce a refrigerant vapor, compressing in a compressor at least a portion of the refrigerant vapor and condensing refrigerant vapor, said method comprising:
(a) providing a refrigerant comprising at least about 97% by weight of the following four compounds, with each compound being present in the following relative percentages:
36.8 to 72% by weight trifluoroiodomethane (CF 3 I);
2 to 36% by weight of tetrafluoropropene selected from trans-1,3,3,3-tetrafluoropropene (HFO-1234ze(E), 2,3,3,3-tetrafluoropropene (HFO-1234yf) and combinations of these;
15 to 31% by weight difluoromethane (HFC-32); and
1 to 4.5% by weight pentafluoroethane (HFC-125);
(b) evaporating said refrigerant at a temperature of from about −40° C. to about +10° C.
16. The method of claim 15 further comprising exposing at least a portion of said refrigerant and/or at least a portion of said lubricant to a sequestration material comprising:
i. activated alumina, or
ii. a zeolite molecular sieve comprising copper, silver, lead or a combination thereof, or
iii. an anion exchange resin, or
iv. a moisture-removing material, preferably a moisture-removing molecular sieve, or
v. a combination of two or more of the above.
17. The method of claim 15 wherein said evaporating step occurs in a heat transfer system comprising a low temperature refrigeration system, a medium temperature refrigeration system, and/or transport refrigeration system.
18. A heat transfer system the type comprising an evaporator, a compressor, and a refrigerant in the system, said system comprising:
(a) said refrigerant comprising at least about 97% by weight of the following four compounds, with each compound being present in the following relative percentages:
36.8 to 72% by weight trifluoroiodomethane (CF 3 I);
2 to 36% by weight of tetrafluoropropene selected from trans-1,3,3,3-tetrafluoropropene (HFO-1234ze(E), 2,3,3,3-tetrafluoropropene (HFO-1234yf) and combinations of these;
15 to 31% by weight difluoromethane (HFC-32); and
1 to 4.5% by weight pentafluoroethane (HFC-125); and
(b) a sequestration material comprising:
i. activated alumina, and
ii. a zeolite molecular sieve comprising copper, silver, lead or a combination thereof, and
iii. an anion exchange resin, and
iv. a moisture-removing material, preferably a moisture-removing molecular sieve.
19. The heat transfer system of claim 18 wherein said system further comprises an oil separator and wherein said sequestration material is located in said oil separator.
20. The heat transfer system of claim 18 wherein said heat transfer system comprises a low temperature refrigeration system, a medium temperature refrigeration system, and/or transport refrigeration system.