Working fluid composition for refrigerator
US-10414962-B2 · Sep 17, 2019 · US
US12410351B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12410351-B2 |
| Application number | US-202118030625-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 7, 2021 |
| Priority date | Oct 8, 2020 |
| Publication date | Sep 9, 2025 |
| Grant date | Sep 9, 2025 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Disclosed is a composition comprising difluoromethane (R-32), 2,3,3,3-tetrafluoropropene (R-1234yf), and isobutane (R-600a). A refrigeration system, including a hermetic compressor and a refrigerant composition. The refrigerant composition includes difluoromethane (R-32), 2,3,3,3-tetrafluoropropene (R-1234yf), and isobutane (R-600a).
Opening claim text (preview).
What is claimed is: 1. A composition comprising a refrigerant consisting essentially of 15 to 22 weight percent difluoromethane, 70 to 84 weight percent 2,3,3,3-tetrafluoropropene, and 1.0 to 10 weight percent isobutane. 2. The composition of claim 1 , wherein the refrigerant consists essentially of 15 to 19 weight percent difluoromethane, 76 to 84 weight percent 2,3,3,3-tetrafluoropropene, and 1.0 to 6.0 weight percent isobutane. 3. The composition of claim 1 , wherein the refrigerant consists essentially of 20 to 22 weight percent difluoromethane, 73 to 76 weight percent 2,3,3,3-tetrafluoropropene, and 4.0 to 5.0 weight percent isobutane. 4. The composition 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. 5. The composition of claim 4 , 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. 6. A refrigeration system, comprising: a hermetic compressor; and the composition of claim 1 . 7. The refrigeration system of claim 6 , wherein said hermetic compressor is a rotary, scroll, or reciprocating compressor. 8. The refrigeration system of claim 6 , 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 8 , 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 6 : wherein the compressor discharge temperature is below the compressor discharge temperature of R-457A or R-454C. 11. A method of operating a hermetic compressor as part of a refrigeration system, comprising the steps of: receiving by the hermetic compressor the composition of claim 1 ; compressing by the hermetic compressor the composition; wherein the discharge temperature of the hermetic compressor is between 80.0° C. and 100.0° C. 12. The method of claim 11 , wherein the hermetic compressor is a low back pressure hermetic reciprocating compressor and the low back pressure hermetic reciprocating compressor receives the composition of claim 1 from an evaporator having an average evaporator temperature between −40° C. and −5° C. 13. The method of claim 11 , wherein the discharge temperature of the compressor is between 81.0° C. and 99.0° C. 14. The method of claim 11 , wherein: the hermetic compressor is a low back pressure hermetic reciprocating compressor; and the method further comprises a step of receiving by the low back pressure hermetic reciprocating compressor the refrigerant composition from an evaporator; wherein the average evaporator temperature is below −5° C. 15. A method of replacing a first refrigerant composition comprising R-404A, R-457A, R-290, or R-454C with a second refrigerant composition comprising 70 to 84 weight percent 2,3,3,3-tetrafluoropropene, 15 to 22 weight percent difluoromethane, and 1.0 to 10 weight percent isobutane, wherein the replacing is performed in a refrigeration system including a hermetic compressor. 16. The method of claim 15 , 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. 17. The method of claim 16 , 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. 18. The method of claim 15 , wherein the compressor discharge temperature is below the compressor discharge temperature of R- 457 A.
Replacement mixtures · CPC title
Unsaturated fluorinated hydrocarbons · CPC title
Halogenated hydrocarbons · CPC title
Hydrocarbons · CPC title
characterised by the use of a special lubricant · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.