Use of (2E)-1,1,1,4,5,5,5-heptafluoro-4-(trifluoromethyl)pent-2-ene in power cycles
View Patent ↗A method is provided for converting heat from a heat source to mechanical energy. The method comprises heating a working fluid using heat supplied from the heat source; and expanding the heated working fluid to lower pressure of the working fluid and generating mechanical energy as the pressure of the working fluid is lowered. The method is characterized by using a working fluid comprising (2E)-1,1,1,4,5,5,5-heptafluoro-4-(trifluoromethyl)pent-2-ene (HFO-153-10mzzy). Also provided is a power cycle apparatus. The apparatus is characterized by containing a working fluid comprising HFO-153-10mzzy.
1. A method for converting heat from a heat source to mechanical energy, comprising: heating a working fluid consisting of (2E)-1,1,1,4,5,5,5-heptafluoro-4-(trifluoromethyl)pent-2-ene (HFO-153-10mzzy) using heat supplied from the heat source; and expanding the heated working fluid to lower the pressure of the working fluid and generate mechanical energy as the pressure of the working fluid is lowered.
2. The method of claim 1 , wherein the working fluid is compressed prior to heating; and the expanded working fluid is cooled and compressed for repeated cycles.
3. The method of claim 2 wherein heat from a heat source is converted to mechanical energy using a sub-critical cycle comprising: (a) compressing a liquid working fluid to a pressure below its critical pressure; (b) heating the compressed liquid working fluid from (a) using heat supplied by the heat source to form vapor working fluid; (c) expanding the vapor working fluid from (b) to lower the pressure of the working fluid and generate mechanical energy; (d) cooling the expanded working fluid from (c) to form a cooled liquid working fluid; and (e) cycling the cooled liquid working fluid from (d) to (a) for compression.
4. The method of claim 2 wherein heat from a heat source is converted to mechanical energy using a trans-critical cycle comprising: (a) compressing a liquid working fluid above said working fluid's critical pressure; (b) heating the compressed working fluid from (a) using heat supplied by the heat source; (c) expanding the heated working fluid from (b) to lower the pressure of the working fluid below its critical pressure and generate mechanical energy; (d) cooling the expanded working fluid from (c) to form a cooled liquid working fluid; and (e) cycling the cooled liquid working fluid from (d) to (a) for compression.
5. The method of claim 2 wherein heat from a heat source is converted to mechanical energy using a super-critical cycle comprising: (a) compressing a working fluid from a pressure above its critical pressure to a higher pressure; (b) heating the compressed working fluid from (a) using heat supplied by the heat source; (c) expanding the heated working fluid from (b) to lower the pressure of the working fluid to a pressure above its critical pressure and generate mechanical energy; (d) cooling the expanded working fluid from (c) to form a cooled working fluid above its critical pressure; and (e) cycling the cooled liquid working fluid from (d) to (a) for compression.
6. The method of claim 1 wherein the heat source is selected from the group consisting of: low pressure steam, industrial waste heat, solar energy, geothermal hot water, low-pressure geothermal steam, low-pressure geothermal steam, and distributed power generation equipment utilizing fuel cells or prime movers.
7. The method of claim 1 wherein the maximum operating pressure for the repeated cycles does not exceed 4 MPa.
8. A power cycle apparatus containing a working fluid to convert heat to mechanical energy, characterized by: said apparatus containing a working fluid consisting of (2E)-1,1,1,4,5,5,5-heptafluoro-4-(trifluoromethyl)pent-2-ene (HFO-153-10mzzy).
9. The power cycle apparatus of claim 8 comprising (a) a heat exchange unit; (b) an expander in fluid communication with the heat exchange unit; (c) a working fluid cooling unit in fluid communication with the expander; and (d) a compressor in fluid communication with the working fluid cooling unit, the compressor further being in fluid communication with the heat exchange unit such that the working fluid then repeats flow through components (a), (b), (c) and (d) in a repeating cycle.
10. The power cycle apparatus of claim 8 wherein the working fluid converts heat to mechanical energy by using heat from a heat source.
11. The power cycle apparatus of claim 10 wherein the heat source is selected from the group consisting of: low pressure steam, industrial waste heat, solar energy, geothermal hot water, low-pressure geothermal steam, low-pressure geothermal steam, and distributed power generation equipment utilizing fuel cells or prime movers.
12. The power cycle apparatus of claim 8 wherein the maximum operating pressure for the power cycle apparatus does not exceed 4 MPa.
13. The power cycle apparatus of claim 8 wherein the power cycle is a sub-critical cycle and the temperature to which the working fluid is heated by the heat source is in the range of from about 50° C. to about 165° C.
14. The power cycle apparatus of claim 8 wherein the power cycle is a trans-critical cycle or a super-critical cycle and the temperature to which the working fluid is heated by the heat source is in the range of from about 171° C. to about 400° C.
15. The power cycle apparatus of claim 8 , wherein the power cycle is a Rankine cycle.
16. A method for raising the maximum feasible evaporating temperature of an existing power cycle system containing a first working fluid comprising: replacing the first working fluid with a second working fluid consisting of (2E)-1,1,1,4,5,5,5-heptafluoro-4-(trifluoromethyl)pent-2-ene.
17. The method of claim 16 , wherein the power cycle system is a Rankine cycle system.