Hfo-1234ze, hfo-1225zc and hfo-1234yf containing compositions and processes for producing and using the compositions
US-2024352296-A1 · Oct 24, 2024 · US
US9267066B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9267066-B2 |
| Application number | US-201113989437-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 8, 2011 |
| Priority date | Nov 25, 2010 |
| Publication date | Feb 23, 2016 |
| Grant date | Feb 23, 2016 |
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The invention relates to a composition comprising (E)-1,1,1,4,4,4-hexafluorobat-2-ene as a mixture with at least one hydrocarbon, hydrofinorocarbon or fluoroolefin compound having a boiling point less than or equal to −12° C., and also to the use of this composition as a heat transfer fluid.
Opening claim text (preview).
The invention claimed is: 1. A composition comprising (E)-1,1,1,4,4,4-hexafluorobut-2-ene with at least one compound having a boiling point less than or equal to −12° C. at a pressure of 101.325 KPa selected from the group consisting of 1,3,3,3-tetrafluoropropene, 2,3,3,3-tetrafluoropropene, 3,3,3-trifluoropropene, 1,1,1,2-tetrafluoroethane, 1,1-difluoroethane, difluoromethane, pentafluoroethane, propane and dimethyl ether, and mixtures thereof, wherein the difference between the liquid saturation pressure and the vapor saturation pressure at a temperature of −5° C. is less than or equal to 10% of the liquid saturation pressure. 2. The composition as claimed in claim 1 , consisting of a mixture of: (E)-1,1,1,4,4,4-hexafluorobut-2-ene and a compound selected from the group consisting of 1,3,3,3-tetrafluoropropene, 2,3,3,3-tetrafluoropropene, 3,3,3-trifluoropropene, 1,1,1,2-tetrafluoroethane, 1,1-difluoroethane, difluoromethane, pentafluoroethane and propane and mixtures thereof. 3. The composition as claimed in claim 1 , comprising: from 10 to 50 weight % of (E)-1,1,1,4,4,4-hexafluorobut-2-ene and from 50 to 90 weight % of 1,3,3,3-tetrafluoropropene. 4. A heat-transfer composition comprising the composition as claimed in claim 1 further comprising one or more additives selected from the group consisting of lubricants, stabilizers, surfactants, tracers, fluorescent agents, odorous agents and solubilizing agents, and mixtures thereof. 5. Heat-transfer equipment comprising a vapor compression circuit containing a composition as claimed in claim 1 . 6. The heat-transfer equipment as claimed in claim 5 , selected from mobile heat-pump heating, or stationary heat-pump heating, air conditioning, refrigeration equipment, and freezing equipment and Rankine cycles. 7. A process for heating or cooling a fluid or a body by means of a vapor compression circuit containing a heat-transfer fluid, said process successively comprising evaporation of the heat-transfer fluid, compression of the heat-transfer fluid, condensation of the heat-transfer fluid and expansion of the heat-transfer fluid, wherein the heat-transfer fluid is a composition as claimed in claim 1 . 8. The process as claimed in claim 7 , comprising a process for cooling a fluid or a body, wherein the temperature of the fluid or of the body cooled is from −15° C. to 15° C. 9. A process for reducing the environmental impact of heat-transfer equipment comprising a vapor compression circuit containing an initial heat-transfer fluid, said process comprising a step replacing the initial heat-transfer fluid in the vapor compression circuit with a final heat-transfer fluid, the final heat-transfer fluid having a GWP which is lower than the initial heat-transfer fluid, wherein the final heat-transfer fluid is a composition as claimed in claim 1 . 10. A composition consisting of a mixture of (E)-1,1,1,4,4,4-hexafluorobut-2-ene and two compounds selected from the group consisting of 1,3,3,3-tetrafluoropropene, 2,3,3,3-tetrafluoropropene, 3,3,3-trifluoropropene, 1,1,1,2-tetrafluoroethane, 1,1-difluoroethane, difluoromethane, pentafluoroethane, propane and isobutane, wherein the difference between the liquid saturation pressure and the vapor saturation pressure at a temperature of −5° C. is less than or equal to 10% of the liquid saturation pressure. 11. The composition as claimed in claim 1 , comprising from 1% to 98% of (E)-1,1,1,4,4,4-hexafluorobut-2-ene, from 1% to 98% of 2,3,3,3-tetrafluoropropene and from 1% to 50% of 1,1,1,2-tetrafluoroethane. 12. The composition as claimed in claim 1 , comprising from 1% to 98% of (E)-1,1,1,44,4-hexafluorobut-2-ene, from 1% to 98% of 1,3,3,3-tetrafluoropropene and from 1% to 40% of 1,1,1,2-tetrafluoroethane. 13. The process as claimed in claim 7 , comprising a process for heating a fluid or a body, wherein the temperature of the fluid or of the body heated is from 30° C. to 90° C. 14. The composition as claimed in claim 1 , wherein the difference between the liquid saturation pressure and the vapor saturation pressure at a temperature of −5° C. is less than or equal to 5% of the liquid saturation pressure. 15. The composition as claimed in claim 1 , comprising: from 1 to 12 weight % of (E)-1,1,1,4,4,4-hexafluorobut-2-ene and from 88 to 99 weight % of 1,3,3,3-tetrafluoropropene.
Compression machines, plants or systems with non-reversible cycle (F25B3/00, F25B5/00, F25B6/00, F25B7/00, F25B9/00 take precedence) · CPC title
Ethers · CPC title
Hydrocarbons · CPC title
All components of a mixture being fluoro compounds · CPC title
Unsaturated fluorinated hydrocarbons · CPC title
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