Integrated micro combined heat and power system

• US 6,598,397 B2
• Filed: 11/30/2001
• Issued: 07/29/2003
• Est. Priority Date: 08/10/2001
• Status: Expired due to Term

• Current Assignee: Energetix Genlec Limited
• Original Assignee: Energetix Micropower Limited
• Inventors: Anson, Donald, Stickford, George Henry Jr., Hanna, William Thompson, Coll, John Gordon
• Primary Examiner(s): NGUYEN, HOANG M
• Application Number:
  US09/998,705
• Publication Number:
  US 20030029169A1
• Time in Patent Office: 606 Days
• Field of Search: 606/51, 606/71, 606/16, 606/18
• US Class Current: 60/651
• CPC Class Codes: F01K 17/02 for heating purposes, e.g. industrial, domestic F01K17/06 takes precedence; domestic- or space-heating systems, e.g. central-heating systems, in general F24D1/00, F24D3/00, F24D9/00
• CPC Class Codes: F01K 25/08 using special vapours
• CPC Class Codes: F24D 18/00 Small-scale combined heat and power [CHP] generation systems specially adapted for domestic heating, space heating or domestic hot-water supply
• CPC Class Codes: F24D 2101/10 Gas turbines; Steam engines or steam turbines; Water turbines, e.g. located in water pipes
• CPC Class Codes: F24D 2103/13 characterised by their heat exchangers
• CPC Class Codes: Y02E 20/14 Combined heat and power generation [CHP]

Abstract

An integrated system to provide both heat and electric power. The integrated, or cogeneration, system operates with an organic working fluid that circulates in a Rankine-type cycle, where the organic working fluid is superheated by a heat source, expanded through an involute spiral wrap (scroll) expander such that the organic working fluid remains superheated through the expander, cooled in a condenser, and pressurized by a pump. Heat exchange loops within the system define hot water production capability for use in space heating and domestic hot water, while the generator is coupled to the scroll expander to generate electricity.

Claims

1. A cogeneration system configured to operate with an organic working fluid, said system comprising:

a heat source;

a first circuit configured to transport said organic working fluid, said first circuit in thermal communication with said heat source such that heat transferred therefrom superheats said organic working fluid, said first circuit comprising;

a scroll expander configured to receive said organic working fluid such that said organic working fluid remains superheated after passage through said scroll expander;

a condenser in fluid communication with said scroll expander; and

a pump configured to circulate said organic working fluid through said first circuit; and

a generator operatively coupled to said scroll expander to produce electricity.

2. A cogeneration system comprising:

an organic working fluid;

a heat source capable of superheating said organic working fluid;

a first circuit configured to transport said organic working fluid, at least a portion of said first circuit in thermal communication with said heat source, said first circuit comprising;

a scroll expander configured to receive said organic working fluid such that said organic working fluid remains superheated after passage through said scroll expander;

a condenser in fluid communication with said scroll expander; and

a pump configured to circulate said organic working fluid through said first circuit; and

a generator operatively coupled to said scroll expander to produce electricity.

3. A cogeneration system according to claim 2, wherein said heat source is a burner in thermal communication with an evaporator.

4. A cogeneration system according to claim 3, wherein said burner and said evaporator are enclosed within a common container, said container including an exhaust duct.

5. A cogeneration system according to claim 4, further comprising a heat exchanger adjacent to said exhaust duct.

6. A cogeneration system according to claim 5, wherein said heat exchanger further comprises an exhaust gas recirculation device.

7. A cogeneration system according to claim 5, wherein a portion of the heat removed from said exhaust duct by said heat exchanger is placed in thermal communication with at least one circulating fluid, thereby increasing the temperature of said fluid.

8. A cogeneration system according to claim 3, wherein said thermal communication between said burner and said first circuit is through an interloop heat exchanger disposed between said pump and said scroll expander.

9. A cogeneration system according to claim 8, further comprising a second circuit disposed adjacent said burner, said second circuit including at least one piping loop adapted to convey a heat exchange fluid therethrough.

10. A cogeneration system according to claim 9, wherein said burner is contained within a combustion chamber that is in thermal communication with said second circuit, said combustion chamber including an exhaust duct in combustion communication with said burner.

11. A cogeneration system according to claim 10, further comprising an exhaust fan coupled to said exhaust duct to facilitate the removal of exhaust gas from said combustion chamber.

12. A cogeneration system according to claim 10, wherein said exhaust duct further comprises an exhaust gas recirculation device such that at least a portion of residual heat extant in said exhaust gas is transferred to said heat exchange fluid.

13. A cogeneration system according to claim 8, wherein said heat exchange fluid in said second circuit comprises a mixture of water and a freeze-inhibiting additive.

14. A cogeneration system according to claim 8, wherein said heat exchange fluid in said second circuit comprises an organic heat transfer fluid.

15. A cogeneration system according to claim 2, wherein said heat source and said first circuit are configured such that the maximum operating pressure of said organic working fluid within said first circuit is approximately 200 to 450 pounds per square inch, and the maximum operating temperature is approximately 250 to 350 degrees Fahrenheit.

16. A cogeneration system according to claim 2, wherein said organic working fluid comprises a halocarbon refrigerant.

17. A cogeneration system according to claim 16, wherein said halocarbon refrigerant comprises R-245fa.

18. A cogeneration system according to claim 2, wherein said working fluid comprises at least one naturally occurring hydrocarbon.

19. A cogeneration system according to claim 18, wherein said at least one naturally occurring hydrocarbon comprises the general formula C_nH_2n+2.

20. A cogeneration system according to claim 19, wherein said at least one naturally occurring hydrocarbon of the general formula C_nH_2n+2 comprises isopentane.

21. A cogeneration system according to claim 2, wherein said condenser is configured to be in heat exchange communication with a space heating loop.

22. A cogeneration system according to claim 21, further comprising a space heating loop preheat device placed in heat exchange communication with a second circuit adapted to convey a heat exchange fluid therethrough.

23. A cogeneration system according to claim 2, wherein said first circuit is configured such that electricity produced by said generator is up to 10 kilowatts.

24. A cogeneration system according to claim 2, wherein said system is configured such that a portion of said electricity produced by said generator is used to operate said pump.

25. A cogeneration system according to claim 2, wherein said condenser is capable of transferring up to 60 kilowatts of thermal energy.

26. A cogeneration system according to claim 2, further including a controller configured to monitor and selectively vary the extent to which said organic working fluid is superheated.

27. A cogeneration system according to claim 26, wherein said controller is configured to compare temperature signals in said evaporator and said scroll expander to determine the extent to which said organic working fluid is superheated.

28. A cogeneration system according to claim 27, further comprising at least one switch responsive to a level of said organic working fluid at the exit of said condenser, said at least one switch coupled to said controller.

29. A cogeneration system according to claim 26, further comprising a set of valves configured to permit said organic working fluid to bypass said scroll expander upon a preset condition.

30. A cogeneration system according to claim 29, wherein said preset condition is a grid outage.

31. A cogeneration system according to claim 29, wherein said preset condition is a startup transient.

32. A cogeneration system according to claim 29, wherein said preset condition is a shutdown transient.

33. A cogeneration system according to claim 2, wherein said cogeneration system is configured to be in heat exchange communication with a domestic hot water loop.

34. A cogeneration system according to claim 33, wherein said heat exchange communication between said cogeneration system and said domestic hot water loop occurs in a storage tank disposed within a second circuit, and wherein said second circuit is adapted to convey a heat exchange fluid therethrough.

35. A cogeneration system according to claim 34, further comprising a heating element disposed in said water storage tank, said heating element is heated by electricity provided by said generator.

36. A cogeneration system according to claim 33, wherein said heat exchange communication between said cogeneration system and said domestic hot water loop occurs in said condenser.

37. A directly-fired micro combined heat and power system comprising:

an organic working fluid;

a piping loop that defines an organic working fluid flow path;

an evaporator disposed in said organic working fluid flow path;

a burner in thermal communication with said evaporator such that heat transferred thereto superheats said organic working fluid;

a scroll expander disposed in said organic working fluid flow path such that said superheated organic working fluid passing through said scroll expander remains superheated upon discharge from said scroll expander;

a generator operatively responsive to said scroll expander to generate electricity;

a condenser comprising;

a primary loop disposed in said organic working fluid flow path such that said primary loop is in fluid communication with said scroll expander; and

a secondary loop in heat exchange relationship with said primary loop, said secondary loop configured to transfer at least a portion of the heat contained in said organic working fluid passing through said primary loop to a space heating device; and

a pump disposed in said organic working fluid flow path between said condenser and said evaporator.

38. A directly-fired micro combined heat and power system according to claim 37, further including a controller configured to monitor and selectively vary the extent to which said organic working fluid is superheated.

39. A directly-fired micro combined heat and power system according to claim 38, further comprising at least one switch responsive to a level of said organic working fluid at the exit of said condenser, said at least one switch coupled to said controller.

40. A directly-fired micro combined heat and power system according to claim 38, further comprising a set of valves configured to permit said organic working fluid bypass said scroll expander if said controller detects a grid outage.

41. A directly-fired micro combined heat and power system according to claim 37, wherein said burner and said evaporator are enclosed within a common container, said container including an exhaust duct.

42. A directly-fired micro combined heat and power system according to claim 41, wherein said secondary loop is bifurcated such that one path is configured to connect to a space heating loop, while the other path is configured to connect to a domestic hot water loop.

43. A directly-fired micro combined heat and power system according to claim 42, wherein at least one place in said secondary loop is in thermal communication with said heat exchanger disposed adjacent said exhaust duct.

44. A directly-fired micro combined heat and power system according to claim 37, further comprising a heat exchanger disposed in said exhaust duct.

45. A directly-fired micro combined heat and power system according to claim 37, wherein said heat exchanger further comprises an exhaust gas recirculation device.

46. A directly-fired micro combined heat and power system according to claim 37, wherein said burner is sized to provide additional heat to said secondary loop.

47. A directly-fired micro combined heat and power system according to claim 37, wherein said secondary loop of said condenser is further configured to couple to a water storage tank.

48. A directly-fired micro combined heat and power system according to claim 47, further comprising a connection in electrical communication with said generator, said connection adapted to connect to a heating element in said water storage tank.

49. A directly-fired micro combined heat and power system according to claim 47, wherein said condenser is configured to convey up to 60 kilowatts of heat to said secondary loop.

50. A directly-fired micro combined heat and power system according to claim 47, wherein said secondary loop is configured to circulate a hydronic fluid.

51. A directly-fired micro combined heat and power system according to claim 37, wherein said organic working fluid comprises a halocarbon refrigerant.

52. A directly-fired micro combined heat and power system according to claim 51, wherein said halocarbon refrigerant comprises R-245fa.

53. A directly-fired micro combined heat and power system according to claim 37, wherein said working fluid comprises at least one naturally-occurring hydrocarbon.

54. A directly-fired micro combined heat and power system according to claim 53, wherein said at least one naturally occurring hydrocarbon comprises the general formula C_nH_2n+2.

55. A directly-fired micro combined heat and power system according to claim 54, wherein said at least one naturally occurring hydrocarbon of the general formula C_nH_2n+2 comprises isopentane.

56. A micro combined heat and power system comprising:

an electricity generating loop comprising;

an organic working fluid;

a burner for superheating said organic working fluid;

a scroll expander to receive said organic working fluid, said scroll expander configured to leave said organic working fluid in a superheated state after passing therethrough;

a generator operatively coupled to said scroll expander to produce electricity;

a condenser disposed in fluid communication with said scroll expander; and

a pump to circulate said organic working fluid through said electricity generating loop; and

a connection in said condenser, said connection configured to couple to an external heating loop.

57. A micro combined heat and power system according to claim 56, wherein said external heating loop is a space heating loop.

58. A micro combined heat and power system according to claim 56, wherein said external heating loop a domestic hot water loop.

59. A micro combined heat and power system according to claim 56, wherein said external heating loop comprises a domestic hot water loop and a space heating loop.

60. A micro combined heat and power system according to claim 56, further comprising a second circuit in thermal communication with said burner.

61. A micro combined heat and power system according to claim 60, wherein said second circuit is adapted to convey a heat exchange fluid therethrough.

62. A micro combined heat and power system according to claim 61, further comprising a preheat coil coupled to said condenser and in thermal communication with said burner such that a fluid flowing through said preheat coil can be preheated prior to entry into said condenser.

63. A micro combined heat and power system according to claim 61, further comprising a controller in signal communication with said electricity generating loop to monitor and selectively vary the energy content of said organic working fluid.

64. A micro combined heat and power system according to claim 56, wherein said burner is disposed in a combustion chamber, said combustion chamber disposed in a second circuit to circulate a secondary fluid therethrough, said combustion chamber comprising:

an exhaust duct in combustion communication with said burner;

a secondary fluid flow path disposed adjacent said burner; and

an exhaust gas recirculation duct in fluid communication with said burner.

65. A micro combined heat and power system according to claim 64, further comprising an exhaust fan coupled to said exhaust duct to facilitate the removal of exhaust gas from said combustion chamber.

66. A micro combined heat and power system according to claim 58, further comprising a coupling loop to facilitate thermal communication between said electricity generating loop and said domestic hot water loop, said coupling loop comprising:

a circulating fluid flow path;

a combustion chamber disposed in said working fluid flow path, said combustion chamber comprising;

a burner in thermal communication with said heat source such that the temperature of said organic working fluid in said organic working fluid flow path is raised;

an exhaust duct in combustion communication with said burner;

an exhaust fan coupled to said exhaust duct to facilitate the removal of exhaust gas from said combustion chamber; and

an exhaust gas recirculation duct in fluid communication with said burner; and

a thermal interface with said at least one heat exchanger disposed in said domestic hot water loop such that a least a portion of the heat extant in working fluid flowing through said working fluid flow path is transferred to domestic hot water flowing through said domestic hot water loop.

67. A system for the production of domestic hot water, space heat and electricity from a Rankine-based cycle, said system comprising:

an organic working fluid;

a substantially closed circuit fluid path configured to transport said organic working fluid therethrough, said substantially closed circuit fluid path at least partially defined by conduit configured to act as a heat transfer element for said organic working fluid, said substantially closed circuit fluid path comprising;

a scroll expander configured to accept said organic working fluid such that said organic working fluid remains superheated after passage through said scroll expander;

a generator operatively coupled to said scroll expander to generate electricity;

a condenser configured to extract at least a portion of the heat remaining in said organic working fluid after said organic working fluid passes through said scroll expander; and

a pump capable of circulating said organic working fluid through said substantially closed circuit fluid path;

a burner in thermal communication with said conduit, said burner configured to provide sufficient heat to superheat said organic working fluid; and

a controller to regulate the operation of said system.

68. A system according to claim 67, wherein said condenser is configured such that an external heating fluid path could be placed in thermal communication therewith.

69. A system according to claim 68, wherein said condenser is configured to extract up to 60 kilowatts of thermal energy from said organic working fluid.

70. A system according to claim 67, wherein said pump is powered by a portion of said electricity produced in said generator.

71. A system according to claim 67, wherein said electrical output of said generator is up to 10 kilowatts.

72. A system according to claim 67, wherein a preferred heat to power ratio extracted from said system during normal operation is between about 7:

1 and 11;

1.

76. A method according to claim 69, wherein said organic working fluid is superheated to about 10 to 30 degrees Fahrenheit above its boiling point in said superheating step.

77. A method according to claim 69, wherein said returning step pressurizes said organic working fluid to a maximum pressure of about 200 to 450 pounds per square inch.

73. A method of producing heat and electrical power from a cogeneration device, the method comprising the steps of:

configuring a first circuit to transport an organic working fluid;

superheating said organic working fluid with a heat source that is in thermal communication with said first circuit;

expanding said superheated organic working fluid in a scroll expander;

maintaining said organic working fluid in a superheated state through said expanding step;

turning a generator that is coupled to said scroll expander to generate electricity;

cooling said organic working fluid in a condenser such that at least a portion of the heat in said organic working fluid passing through said condenser is transferred to an external heating loop;

using at least a portion of said heat that has been transferred to said external heating loop heat to provide space heat; and

returning said organic working fluid exiting said condenser to a position in said first circuit such that it can receive additional heat input from said heat source.

74. A method according to claim 73, comprising the additional step of selectively using at least a portion of said heat that has been transferred to said external heating loop to heat a domestic hot water loop.

75. A method according to claim 74, comprising the additional steps of:

configuring a second circuit to transport a heat exchange fluid, said second circuit defined by a piping loop in thermal communication with said heat source and heat exchange communication with at least one domestic hot water loop;

heating said heat exchange fluid with said heat source; and

using at least a portion of said heat that has been transferred to said heating exchange fluid to heat a fluid in said domestic hot water loop.

78. A method according to claim 73, wherein said superheating step produces a maximum temperature of said organic working fluid between about 250 to 350 degrees Fahrenheit.

79. A method according to claim 73, wherein said expanding step is conducted such that the electrical output of said generator is up to 10 kilowatts.

80. A method according to claim 73, wherein said cooling step is conducted such that the thermal output transferred to said external heating loop is up to 60 kilowatts.

81. A method according to claim 73, wherein said superheating step is conducted such that said organic working fluid is directly fired with said heat source.

82. A method according to claim 73, wherein said superheating step is conducted such that said organic working fluid is indirectly fired with said heat source.

83. A method according to claim 73, comprising the additional step of operating a set of valves configured to permit said organic working fluid to bypass said scroll expander upon a preset condition.

84. A method according to claim 83, wherein said preset condition is a grid outage.

85. A method according to claim 83, wherein said preset condition is a startup transient.

86. A method according to claim 83, wherein said preset condition is a shutdown transient.

87. A system for the production of electricity and space heat, said system comprising:

an organic working fluid;

a flow path configured to transport said organic working fluid;

a combustion chamber disposed in said flow path, said combustion chamber comprising;

a burner;

a heat transfer element adapted to convey said organic working fluid adjacent said burner such that upon operation of said burner, said organic working fluid becomes superheated; and

an exhaust duct to convey combustion products produced by said burner to the atmosphere;

a scroll expander disposed in said flow path to receive and discharge said organic working fluid such that said organic working fluid remains superheated after passage through said scroll expander;

a generator operatively coupled to said scroll expander to produce electricity;

a condenser in fluid communication with said scroll expander; and

a pump to circulate said organic working fluid through said flow path.

88. A system according to claim 87, further comprising at least one connection in said condenser, said connection configured to place a space heating loop in thermal communication with said organic working fluid.

89. A system according to claim 88, further comprising:

a controller configured to monitor and selectively vary the extent to which said organic working fluid is superheated;

at least one switch responsive to a level of said organic working fluid at the exit of said condenser, said at least one switch coupled to said controller; and

a set of valves configured to permit said organic working fluid to bypass said scroll expander upon a preset condition.

90. A system according to claim 88, further comprising a heat exchanger adjacent said exhaust duct.

91. A system according to claim 90, wherein said heat exchanger further comprises an exhaust gas recirculation device.

92. A system according to claim 90, further comprising a supplemental heat device placed in heat exchange communication with said heat exchanger, said supplemental heat device configured to increase the fluid temperature in at least one of said organic working fluid flow path or said space heating loop.