Cascading closed loop cycle power generation

• US 20040011038A1
• Filed: 03/03/2003
• Published: 01/22/2004
• Est. Priority Date: 07/22/2002
• Status: Active Grant

• Current Assignee: Universal Technologies Incorporated
• Original Assignee: Universal Technologies Incorporated
• Inventors: Mian, Farouk Aslam, Stinger, Daniel H.
• Granted Patent: US 7,096,665 B2
• Time in Patent Office: Days
• US Class Current: 60/651
• CPC Class Codes: F01K 25/08 using special vapours
• CPC Class Codes: Y02P 80/15 On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply

Abstract

Cascading Closed Loop Cycle (CCLC) and Super Cascading Closed Loop Cycle (Super-CCLC) systems are described for recovering power in the form of mechanical or electrical energy from the waste heat of a steam turbine system. The waste heat from the boiler and steam condenser is recovered by vaporizing propane or other light hydrocarbon fluids in multiple indirect heat exchangers; expanding the vaporized propane in multiple cascading expansion turbines to generate useful power; and condensing to a liquid using a cooling system. The liquid propane is then pressurized with pumps and returned to the indirect heat exchangers to repeat the vaporization, expansion, liquefaction and pressurization cycle in a closed, hermetic process.

Claims

1. A method for generating energy, the method comprising:

providing a working fluid;

increasing the pressure of the working fluid;

dividing the working fluid into multiple streams, including at least a first stream and a second stream;

transferring a first amount of heat energy from an energy source to the first stream and subsequently transferring a second amount of heat energy from the first stream to the second stream;

extracting a first amount of useful energy from the first stream;

extracting a second amount of useful energy from the second stream;

merging the first stream with the second stream; and

reducing the first stream and the second stream to a minimum pressure, the minimum pressure being approximately equal to or below the vapor pressure of the working fluid at an ambient temperature.

2. The method of claim 1, wherein the working fluid is selected from the group consisting of propane, propylene, light hydrocarbons and combinations thereof.

3. The method of claim 1, wherein the minimum pressure is about 25 psia to about 300 psia.

4. The method of claim 1, wherein the ambient temperature is about −

50 degrees Fahrenheit to about 160 degrees Fahrenheit.

5. The method of claim 1, wherein the energy source is selected from the group consisting of fossil fuel energy, nuclear energy, solar energy, geothermal energy, waste heat, hydrogen and combinations thereof.

6. The method of claim 1, wherein the step of transferring a second amount of heat energy from the first stream to the second stream comprises:

transferring a first portion of the second amount of heat energy from the first stream to the second stream before the step of merging the first stream with the second stream; and

transferring a second portion of the second amount of heat energy from the first stream to the second stream after the step of merging the first stream with the second stream.

7. The method of claim 6, wherein the step of transferring a first portion of the second amount of heat energy from the first stream to the second stream is performed after the step of extracting a first amount of useful energy from the first stream.

8. The method of claim 1, wherein the sum of the first amount of useful energy and the second amount of useful energy is equal to at least about 20% of the first amount of heat energy.

9. The method of claim 1, wherein the step of increasing the pressure of the working fluid comprises increasing the pressure of the working fluid to about 300 psia to about 1000 psia.

10. An apparatus for generating energy, the apparatus comprising:

multiple fluid conduits, including at least a first fluid conduit, a second fluid conduit, and a combined fluid conduit, the multiple fluid conduits being adapted to contain a working fluid;

a pump operatively attached to the multiple fluid conduits and adapted to pressurize the working fluid;

an energy source;

a first heat exchanger operatively attached to the first fluid conduit and adapted to allow a first amount of heat energy to transfer from the energy source to the working fluid in the first fluid conduit;

a second heat exchanger operatively attached to the first fluid conduit and the second fluid conduit and adapted to allow a second amount of heat energy to transfer from the working fluid in the first fluid conduit to the working fluid in the second fluid conduit, the second heat exchanger being positioned, with respect to the first fluid conduit, downstream of the first heat exchanger;

a first fluid expander operatively attached to the first fluid conduit and adapted to extract a first amount of useful energy from the working fluid in the first fluid conduit;

a second fluid expander operatively attached to the second fluid conduit and adapted to extract a second amount of useful energy from the working fluid in the second fluid conduit;

a cooling device operatively attached to at least one of the multiple fluid conduits and adapted to reduce the working fluid to a minimum pressure, the minimum pressure being approximately equal to or below the vapor pressure of the fluid at an ambient temperature; and

wherein the first fluid conduit and the second fluid conduit join at a merge point to form the combined fluid conduit.

11. The apparatus of claim 10, wherein the working fluid is selected from the group consisting of propane, propylene, light hydrocarbons and combinations thereof.

12. The apparatus of claim 10, wherein the minimum pressure is about 25 psia to about 300 psia.

13. The apparatus of claim 10, wherein the ambient temperature is about −

50 degrees Fahrenheit to about 160 degrees Fahrenheit.

14. The apparatus of claim 10, wherein the energy source is selected from the group consisting a fossil fuel burner, a nuclear reactor, a solar collector, a geothermal source, a waste heat source, hydrogen and combinations thereof.

15. The apparatus of claim 10, wherein the second heat exchanger comprises:

a primary second heat exchanger operatively attached to the primary fluid conduit and the secondary fluid conduit, and being located, with respect to the first fluid conduit, between the first fluid expander and the merge point, and being adapted to transfer a first portion of the second amount of heat energy from the working fluid in the first fluid conduit to the working fluid in the second fluid conduit; and

a secondary second heat exchanger operatively attached to the second fluid conduit and the combined fluid conduit, and being positioned, with respect to the combined fluid conduit, between the merge point and the pump, and being adapted to transfer a second portion of the second amount of heat energy from the working fluid in the combined fluid conduit to the working fluid in the second fluid conduit.

16. The apparatus of claim 15, wherein the second heat exchanger is positioned, with respect to the first fluid conduit, after the first fluid expander.

17. The apparatus of claim 10, wherein the sum of the first amount of useful energy and the second amount of useful energy is equal to at least about 20% of the first amount of heat energy.

18. The apparatus of claim 10, wherein the pump is adapted to pressurize the working fluid to about 300 psia to about 1000 psia.

19. A method for converting heat to useful energy, the method comprising:

providing a combined fluid stream in a liquid state;

pressurizing the combined fluid stream;

dividing the combined fluid stream into a primary fluid stream and a secondary fluid stream;

applying thermal energy from a heat source to vaporize the primary fluid stream;

expanding the vaporized primary fluid stream to produce a first amount of useful energy;

transferring heat from the vaporized and expanded primary fluid stream to superheat the vaporized secondary fluid stream;

expanding the vaporized second fluid stream to produce a second amount of useful energy;

mixing the vaporized and expanded primary fluid stream with the vaporized and expanded secondary fluid stream to form a combined fluid stream;

transferring heat from the combined fluid stream to vaporize the secondary fluid stream; and

condensing the combined fluid stream to a liquid state.

20. The method of claim 19, wherein the fluid is selected from the group consisting of propane, propylene, light hydrocarbons and combinations thereof.

21. The method of claim 19, wherein the step of transferring heat from the combined fluid stream to vaporize the secondary fluid stream further comprises maintaining the pressure of the combined fluid stream above the vapor pressure of the fluid.

22. An apparatus for converting heat to useful energy, the apparatus comprising:

a combined fluid conduit adapted to convey a fluid stream;

a pump operatively attached to the combined fluid conduit;

a stream separator operatively attached to the combined fluid conduit downstream of the pump, the stream separator further being operatively attached to a primary fluid conduit and a secondary fluid conduit;

a first heat exchanger operatively attached to the primary fluid conduit downstream of the stream separator, the first heat exchanger further being operatively attached to a heat source;

a first expander operatively attached to the primary fluid conduit downstream of the first heat exchanger;

a second heat exchanger operatively attached to the primary fluid conduit downstream of the first expander, the second heat exchanger further being operatively attached to the secondary fluid conduit;

a third heat exchanger operatively attached to the secondary fluid conduit downstream of the fluid separator;

the third heat exchanger further being operatively attached to the combined fluid conduit;

a second expander operatively attached to the secondary fluid conduit downstream of the second heat exchanger;

a stream mixer operatively attached to the combined fluid conduit, to the primary fluid conduit downstream of the second heat exchanger, and to the secondary fluid conduit downstream of the second expander;

a cooler operatively attached to the combined fluid conduit between the stream mixer and the pump;

wherein the third heat exchanger is positioned, with respect to the combined fluid conduit, between the stream mixer and the cooler; and

wherein the second heat exchanger is positioned, with respect to the secondary fluid conduit, between the third heat exchanger and the second expander.

23. The apparatus of claim 22, wherein the fluid stream is selected from the group consisting of propane, propylene, light hydrocarbons and combinations thereof.

24. The apparatus of claim 22, wherein the energy source is selected from the group consisting a fossil fuel burner, a nuclear reactor, a solar collector, a geothermal source, a waste heat source, hydrogen and combinations thereof.

25. A method for improving the efficiency of a power system having an energy source and a cooling system, the method comprising:

transferring a first amount of heat energy from the cooling system to a first loop of a cascading closed loop cycle system;

extracting a first amount of useful energy from the first loop;

transferring a second amount of heat energy from the energy source to a second loop of a cascading closed loop cycle system; and

extracting a second amount of useful energy from the second loop.

26. The method of claim 25, wherein the cascading closed loop cycle system comprises a working fluid selected from the group consisting of propane, propylene, light hydrocarbons and combinations thereof.

27. The method of claim 25, further comprising:

transferring a third amount of heat energy from the second loop to a third loop of a cascading closed loop cycle system; and

extracting a third amount of useful energy from the third loop.

28. The method of claim 27, wherein the power system receives a fourth amount of heat energy from the energy source and generates a fourth amount of useful energy, and wherein the sum of the first amount of useful energy, the second amount of useful energy, the third amount of useful energy and the fourth amount of useful energy is equal to at least about 30% of the fourth amount of heat energy.

29. A method for improving the efficiency of a power system having an energy source and a cooling system, the method comprising:

providing a working fluid;

increasing the pressure of the working fluid;

dividing the working fluid into multiple streams, including at least a first stream and a second stream;

transferring a first amount of heat energy from the cooling system to the first stream;

extracting a first amount of useful energy from the first stream;

transferring a second amount of heat energy from the energy source to the second stream;

extracting a second amount of useful energy from the second stream; and

cooling the working fluid to a minimum pressure, the minimum pressure being approximately equal to or below the vapor pressure of the working fluid at an ambient air temperature.

30. The method of claim 29, wherein:

the second stream comprises a primary second stream and a secondary second stream; and

the step of transferring a second amount of heat energy from the energy source to the second stream comprises;

transferring the second amount of heat energy from the energy source to the primary second stream; and

transferring a portion of the second amount of heat energy from the primary second stream to the secondary second stream.

31. The method of claim 30, wherein the step of extracting a second amount of useful energy from the second stream comprises:

extracting a first portion of the second amount of useful energy from the primary second stream; and

extracting a second portion of the second amount of useful energy from the secondary second stream.

32. The method of claim 29, wherein the working fluid is selected from the group consisting of propane, propylene, light hydrocarbons and combinations thereof.

33. The method of claim 29, wherein the minimum pressure is about 25 psia to about 300 psia.

34. The method of claim 29, wherein the ambient temperature is about −

50 degrees Fahrenheit to about 160 degrees Fahrenheit.

35. The method of claim 29, wherein the energy source is selected from the group consisting of fossil fuel energy, nuclear energy, solar energy, geothermal energy, waste heat, hydrogen and combinations thereof.

36. The method of claim 29, wherein the power system is a steam power generation system.

37. The method of claim 29, wherein the step of increasing the pressure of the working fluid comprises increasing the pressure of the working fluid to about 300 psia to about 1000 psia.

38. A method for generating energy, the method comprising:

providing a first working fluid;

increasing the pressure of the first working fluid;

transferring a first amount of heat energy from an energy source to the first working fluid;

extracting a first amount of useful energy from the first working fluid;

providing a second working fluid;

increasing the pressure of the second working fluid;

dividing the second working fluid into multiple streams, including at least a first stream and a second stream;

transferring a second amount of heat energy from the first working fluid to the first stream;

extracting a second amount of useful energy from the first stream;

transferring a third amount of heat energy from the energy source to the second stream;

extracting a third amount of useful energy from the second stream; and

cooling the second working fluid to a minimum pressure, the minimum pressure being approximately equal to or below the vapor pressure of the second working fluid at an ambient air temperature.

39. The method of claim 38, wherein:

the second stream comprises a primary second stream and a secondary second stream; and

the step of transferring a third amount of heat energy from the energy source to the second stream comprises;

transferring the third amount of heat energy from the energy source to the primary second stream; and

transferring a portion of the third amount of heat energy from the primary second stream to the secondary second stream.

40. The method of claim 39, wherein the step of extracting a third amount of useful energy from the second stream comprises:

extracting a first portion of the third amount of useful energy from the primary second stream; and

extracting a second portion of the third amount of useful energy from the secondary second stream.

41. The method of claim 38, wherein the first working fluid is water.

42. The method of claim 38, wherein the second working fluid is selected from the group consisting of propane, propylene, light hydrocarbons and combinations thereof.

43. The method of claim 38, wherein the minimum pressure is about 25 psia to about 300 psia.

44. The method of claim 38, wherein the ambient temperature is about −

50 degrees Fahrenheit to about 160 degrees Fahrenheit.

45. The method of claim 38, wherein the energy source is selected from the group consisting of fossil fuel energy, nuclear energy, solar energy, geothermal energy, waste heat and combinations thereof.

46. A method for improving the efficiency of a power system having an energy source and a cooling system, the method comprising:

providing a working fluid;

increasing the pressure of the working fluid;

dividing the working fluid into a first stream a second stream and a third stream;

transferring a first amount of heat energy from the cooling system to the first stream;

extracting a first amount of useful energy from the first stream;

transferring a second amount of heat energy from the energy source to the second stream;

extracting a second amount of useful energy from the second stream;

transferring a third amount of heat energy from the second stream to the third stream;

extracting a third amount of useful energy from the third stream; and

cooling the working fluid to a minimum pressure, the minimum pressure being approximately equal to or below the vapor pressure of the working fluid at an ambient air temperature.

47. The method of claim 46, wherein the step of transferring a second amount of heat energy from the energy source to the second stream comprises:

transferring a first portion of the second amount of heat energy from the energy source to the second stream in a first heat exchanger; and

transferring a second portion of the second amount of heat energy from the energy source to the second stream in a second heat exchanger.

48. The method of claim 46, wherein:

the step of extracting a first amount of useful energy from the first stream comprises expanding the first stream in a first expander;

the step of extracting a second amount of useful energy from the second stream comprises expanding the second stream in a second expander; and

the step of extracting a third amount of useful energy from the third stream comprises expanding the third stream in a third expander.

49. The method of claim 46, wherein the working fluid is selected from the group consisting of propane, propylene, light hydrocarbons and combinations thereof.

50. The method of claim 46, wherein the minimum pressure is about 25 psia to about 300 psia.

51. The method of claim 46, wherein the ambient temperature is about −

50 degrees Fahrenheit to about 160 degrees Fahrenheit.

52. The method of claim 46, wherein the energy source is selected from the group consisting of fossil fuel energy, nuclear energy, solar energy, geothermal energy, waste heat, hydrogen and combinations thereof.

53. The method of claim 46, wherein the power system is a steam power generation system.

54. An apparatus for generating supplemental energy from a power system having an energy source and a cooling system, the apparatus comprising:

multiple fluid conduits, including at least a first fluid conduit, a second fluid conduit, and a combined fluid conduit, the multiple fluid conduits being adapted to contain a working fluid;

one or more pumps operatively attached to the multiple fluid conduits and adapted to pressurize the working fluid;

a first heat exchanger operatively attached to the first fluid conduit and adapted to allow a first amount of heat energy to transfer from the cooling system to the working fluid in the first fluid conduit;

a first fluid expander operatively attached to the first fluid conduit and adapted to extract a first amount of useful energy from the working fluid in the first fluid conduit;

a second heat exchanger operatively attached to the second fluid conduit and adapted to allow a second amount of heat energy to transfer from the energy source to the working fluid in the second fluid conduit;

a second fluid expander operatively attached to the second fluid conduit and adapted to extract a second amount of useful energy from the working fluid in the second fluid conduit;

a cooling device operatively attached to at least one of the multiple fluid conduits and adapted to reduce the working fluid to a minimum pressure, the minimum pressure being approximately equal to or below the vapor pressure of the fluid at an ambient temperature; and

wherein the first fluid conduit and the second fluid conduit join at one or more merge points to form the combined fluid conduit.

55. The apparatus of claim 54, wherein the multiple fluid conduits further include a third fluid conduit, and the apparatus further comprises:

a third heat exchanger operatively attached to the second fluid conduit and the third fluid conduit and adapted to transfer a third amount of heat energy from the working fluid in the second fluid conduit to the working fluid in the third fluid conduit;

a third fluid expander operatively attached to the third fluid conduit and adapted to extract a third amount of useful energy from the working fluid in the third fluid conduit; and

wherein the third heat exchanger is located, relative the second fluid conduit, after the second fluid expander.

56. The apparatus of claim 54, wherein the second heat exchanger comprises two or more heat exchangers.

57. The apparatus of claim 54, wherein the working fluid is selected from the group consisting of propane, propylene, light hydrocarbons and combinations thereof.

58. The apparatus of claim 54, wherein the minimum pressure is about 25 psia to about 300 psia.

59. The apparatus of claim 54, wherein the ambient temperature is about −

50 degrees Fahrenheit to about 160 degrees Fahrenheit.

60. The apparatus of claim 54, wherein the energy source is selected from the group consisting a fossil fuel burner, a nuclear reactor, a solar collector, a geothermal source, a waste heat source, hydrogen and combinations thereof.

61. The apparatus of claim 54, wherein the power system receives a fourth amount of heat energy from the energy source and generates a fourth amount of useful energy, and wherein the sum of the first amount of useful energy, the second amount of useful energy, the third amount of useful energy and the fourth amount of useful energy is equal to at least about 30% of the fourth amount of heat energy.

62. An apparatus for converting heat energy to useful energy, the apparatus comprising:

a primary power system comprising;

an energy source;

a primary fluid conduit adapted to contain a primary working fluid;

a primary fluid pump operatively attached to the primary fluid conduit and adapted to pressurize the primary working fluid;

a primary fluid heat exchanger operatively attached to the primary fluid conduit and adapted to allow a first amount of heat energy to transfer from the energy source to the primary fluid contained in the primary fluid conduit;

a primary fluid expander operatively attached to the primary fluid conduit and adapted to extract a first amount of useful energy from the primary working fluid in the primary fluid conduit;

a secondary power system comprising;

a secondary fluid conduit system comprising a first fluid loop, a second fluid loop, and a third fluid loop, the secondary fluid conduit system being adapted to contain a secondary working fluid;

one or more secondary fluid pumps operatively attached to the secondary fluid conduit system and adapted to pressurize the secondary working fluid;

a first heat exchanger operatively attached to the first fluid loop and the primary fluid conduit and being positioned, relative to the primary fluid conduit, between the primary fluid expander and the primary fluid pump, the first heat exchanger being adapted to allow a second amount of heat energy to transfer from the primary fluid in the primary working fluid conduit to the secondary working fluid in the first fluid loop;

a first fluid expander operatively attached to the first fluid loop and adapted to extract a second amount of useful energy from the secondary working fluid in the first fluid loop;

a second heat exchanger operatively attached to the second fluid loop and adapted to allow a third amount of heat energy to transfer from the energy source to the secondary working fluid in the second fluid loop;

a second fluid expander operatively attached to the second fluid loop and adapted to extract a third amount of useful energy from the secondary working fluid in the second fluid loop;

a third heat exchanger operatively attached to the second fluid loop and the third fluid loop and being located, relative the second fluid loop, after the second fluid expander, the third heat exchanger being adapted to allow a fourth amount of heat energy to transfer from the secondary working fluid in the second fluid loop to the secondary working fluid in the third fluid loop;

a third fluid expander operatively attached to the third fluid loop and adapted to extract a fourth amount of useful energy from the secondary working fluid in the second fluid loop; and

a cooling device operatively attached to the secondary fluid conduit system and adapted to reduce the secondary working fluid to a minimum pressure, the minimum pressure being approximately equal to or below the vapor pressure of the secondary working fluid at an ambient temperature.

63. The apparatus of claim 62, wherein the primary working fluid is water.

64. The apparatus of claim 62, wherein the secondary working fluid is selected from the group consisting of propane, propylene, light hydrocarbons and combinations thereof.

65. The apparatus of claim 62, wherein the minimum pressure is about 25 psia to about 300 psia.

66. The apparatus of claim 62, wherein the ambient temperature is about −

50 degrees Fahrenheit to about 160 degrees Fahrenheit.

67. The apparatus of claim 62, wherein the energy source is selected from the group consisting a fossil fuel burner, a nuclear reactor, a solar collector, a geothermal source, a waste heat source, hydrogen and combinations thereof.

68. The apparatus of claim 62, wherein the sum of the first amount of useful energy, the second amount of useful energy, the third amount of useful energy and the fourth amount of useful energy is equal to at least about 30% of the first amount of heat energy.

69. The apparatus of claim 62, wherein the one or more secondary fluid pumps are adapted to pressurize the secondary working fluid to about 300 psia to about 1000 psia.