Systems and methods for combined thermal and compressed gas energy conversion systems

• US 7,958,731 B2
• Filed: 01/20/2010
• Issued: 06/14/2011
• Est. Priority Date: 01/20/2009
• Status: Active Grant

• Current Assignee: Hydrostor Inc.
• Original Assignee: SustainX, Inc. (General Compression, Inc.)
• Inventors: McBride, Troy O., Bollinger, Benjamin R., Cameron, Benjamin, Magari, Patrick, Chen, Weibo, Izenson, Michael
• Primary Examiner(s): Nguyen; Hoang M
• Application Number:
  US12/690,513
• Publication Number:
  US 20100205960A1
• Time in Patent Office: 510 Days
• Field of Search: 60413-418, 606/43, 606/45, 606/412, 91/4.R, 91/4.A
• US Class Current: 60/613
• CPC Class Codes: F02C 6/16 for storing compressed air
• CPC Class Codes: F03G 4/001 Binary cycle plants where the source fluid from the geothermal collector heats the working fluid via a heat exchanger
• CPC Class Codes: F03G 6/00 Devices for producing mechanical power from solar energy solar boilers F24
• CPC Class Codes: F03G 6/071 with energy storage devices
• CPC Class Codes: F03G 7/04 using pressure differences or thermal differences occurring in nature F03G7/06 takes precedence
• CPC Class Codes: Y02E 10/46 Conversion of thermal power into mechanical power, e.g. Rankine, Stirling or solar thermal engines
• CPC Class Codes: Y02E 60/16 Mechanical energy storage, e.g. flywheels or pressurised fluids
• CPC Class Codes: Y02T 10/12 Improving ICE efficiencies

Abstract

The invention relates to systems and methods including an energy conversion system for storage and recovery of energy using compressed gas, a source of recovered thermal energy, and a heat-exchange subsystem in fluid communication with the energy conversion system and the source of recovered thermal energy.

Claims

1. A combined thermal and compressed-gas energy conversion system (i) suitable for the efficient use and conservation of energy resources and (ii) for use with a source of recovered thermal energy, the system comprising:

an open-air compressed-gas energy conversion system configured for substantially isothermal storage and recovery of energy and comprising;

at least one cylinder assembly for the storage and recovery of energy via compression and expansion of gas therewithin,

selectively fluidly connected to the at least one cylinder assembly, means for storage of compressed gas after compression and supply of compressed gas for expansion thereof, and

selectively fluidly connected to the at least one cylinder assembly, a vent for exhausting expanded gas to atmosphere after expansion and supply of gas for compression thereof; and

a heat-exchange subsystem (i) configured for fluid communication with the compressed-gas energy conversion system and the source of recovered thermal energy, and (ii) comprising, disposed in at least one said cylinder assembly, a spray mechanism for introducing a heat-exchange fluid therein.

2. The system of claim 1, wherein the heat-exchange subsystem utilizes the recovered thermal energy to heat the compressed gas prior to and/or during expansion thereof.

3. The system of claim 1, wherein the heat-exchange subsystem utilizes the recovered thermal energy to cool the compressed gas during and/or after compression thereof.

4. The system of claim 1, wherein the source of recovered thermal energy comprises at least one of a fossil fuel power plant, a heat engine power plant, a solar thermal source, a geothermal source, an industrial process with waste heat, a heat pump, a heat source, a heat sink, or a source of environmentally chilled water.

5. The system of claim 1, wherein the source of recovered thermal energy comprises a thermal well.

6. The system of claim 1, wherein the heat-exchange subsystem comprises:

a circulation apparatus in fluid communication with the energy conversion system for circulating the heat-exchange fluid through the heat-exchange subsystem; and

a heat exchanger comprising;

a first side in fluid communication with the circulation apparatus and the energy conversion system, the circulation apparatus circulating the heat-exchange fluid from the energy conversion system, through the heat exchanger, and back to the energy conversion system, and

a second side configured for fluid communication with the source of recovered thermal energy.

7. The system of claim 6, wherein the heat-exchange fluid transfers at least a portion of the recovered thermal energy for use as at least one of process heat, cooling, or building conditioning.

8. The system of claim 1, wherein the at least one cylinder assembly comprises a first cylinder assembly including a staged pneumatic side and a hydraulic side, the sides being separated by a mechanical boundary mechanism that transfers energy therebetween, and the heat exchange subsystem is in fluid communication with the pneumatic side of the first cylinder assembly.

9. The system of claim 1, wherein the spray mechanism comprises at least one of a spray head disposed at an end of at least one said cylinder assembly or a spray rod running through at least a portion of at least one said cylinder assembly.

10. The system of claim 8, further comprising, in fluid communication with the first cylinder assembly, a second cylinder assembly including a staged pneumatic side and a hydraulic side separated by a boundary mechanism that transfers mechanical energy therebetween.

11. The system of claim 10, wherein the first cylinder assembly is an accumulator that transfers the mechanical energy at a first pressure ratio and the second cylinder assembly is an intensifier that transfers the mechanical energy at a second pressure ratio greater than the first pressure ratio.

12. The system of claim 1, wherein the means for storage of compressed gas after compression and supply of compressed gas for expansion thereof comprises a pressure vessel, and the heat-exchange subsystem is in fluid communication with the pressure vessel.

13. The system of claim 12, wherein the heat-exchange subsystem comprises:

a circulation apparatus in fluid communication with the pressure vessel for circulating a fluid through the heat-exchange subsystem; and

a heat exchanger comprising;

a first side in fluid communication with the circulation apparatus and the pressure vessel, the circulation apparatus circulating the fluid from the pressure vessel, through the heat exchanger, and back to the pressure vessel, and

a second side configured for fluid communication with the source of recovered thermal energy.

14. The system of claim 13, wherein the fluid comprises a gas being stored in the pressure vessel.

15. A combined thermal and compressed-gas energy conversion system (i) suitable for the efficient use and conservation of energy resources and (ii) for use with a source of recovered thermal energy, the system comprising:

a compressed-gas energy conversion system (i) configured for substantially isothermal storage and recovery of energy, and (ii) comprising a cylinder assembly including a staged pneumatic side and a hydraulic side, the sides being separated by a mechanical boundary mechanism that transfers energy therebetween; and

a heat-exchange subsystem configured for fluid communication with the pneumatic side of the cylinder assembly and the source of recovered thermal energy,

wherein the heat-exchange subsystem comprises;

a circulation apparatus in fluid communication with the pneumatic side of the cylinder assembly for circulating a fluid through the heat-exchange subsystem; and

a heat exchanger comprising;

a first side in fluid communication with the circulation apparatus and the pneumatic side of the cylinder assembly, the circulation apparatus circulating the fluid from the pneumatic side of the cylinder assembly, through the heat exchanger, and back to the pneumatic side of the cylinder assembly, and

a second side configured for fluid communication with the source of recovered thermal energy.

16. The system of claim 15, wherein the fluid comprises a gas being compressed or expanded in the pneumatic side of the cylinder assembly.

17. The system of claim 15, further comprising a spray mechanism disposed in the pneumatic side of the cylinder assembly, wherein the fluid comprises a heat-exchange fluid introduced into the cylinder assembly through the spray mechanism.

18. The system of claim 17, wherein the spray mechanism comprises at least one of a spray head disposed at an end of the cylinder assembly or a spray rod running through at least a portion of the cylinder assembly.

19. The system of claim 15, further comprising, in fluid communication with the cylinder assembly, a second cylinder assembly including a staged pneumatic side and a hydraulic side separated by a boundary mechanism that transfers mechanical energy therebetween.

20. The system of claim 19, wherein the cylinder assembly is an accumulator that transfers the mechanical energy at a first pressure ratio and the second cylinder assembly is an intensifier that transfers the mechanical energy at a second pressure ratio greater than the first pressure ratio.

21. The system of claim 15, wherein the heat-exchange subsystem utilizes the recovered thermal energy to heat the compressed gas prior to and/or during expansion thereof.

22. The system of claim 15, wherein the heat-exchange subsystem utilizes the recovered thermal energy to cool the compressed gas during and/or after compression thereof.

23. The system of claim 15, wherein the source of recovered thermal energy comprises at least one of a fossil fuel power plant, a heat engine power plant, a solar thermal source, a geothermal source, an industrial process with waste heat, a heat pump, a heat source, a heat sink, or a source of environmentally chilled water.

24. The system of claim 15, wherein the source of recovered thermal energy comprises a thermal well.

25. The system of claim 15, wherein the fluid transfers at least a portion of the recovered thermal energy for use as at least one of process heat, cooling, or building conditioning.

26. A combined thermal and compressed-gas energy conversion system (i) suitable for the efficient use and conservation of energy resources and (ii) for use with a source of recovered thermal energy, the system comprising:

a compressed-gas energy conversion system (i) configured for substantially isothermal storage and recovery of energy, and (ii) comprising a pressure vessel for storage of the compressed gas;

a spray mechanism disposed in the pressure vessel; and

a heat-exchange subsystem configured for fluid communication with the pressure vessel and the source of recovered thermal energy, the heat-exchange subsystem comprising;

a circulation apparatus in fluid communication with the pressure vessel for circulating a fluid through the heat-exchange subsystem, and

a heat exchanger comprising;

a first side in fluid communication with the circulation apparatus and the pressure vessel, the circulation apparatus circulating the fluid from the pressure vessel, through the heat exchanger, and back to the pressure vessel, and

a second side configured for fluid communication with the source of recovered thermal energy,

wherein the fluid comprises a heat-exchange fluid introduced into the pressure vessel through the spray mechanism.

27. The system of claim 26, wherein the heat-exchange subsystem utilizes the recovered thermal energy to heat the compressed gas prior to and/or during expansion thereof.

28. The system of claim 26, wherein the heat-exchange subsystem utilizes the recovered thermal energy to cool the compressed gas during and/or after compression thereof.

29. The system of claim 26, wherein the source of recovered thermal energy comprises at least one of a fossil fuel power plant, a heat engine power plant, a solar thermal source, a geothermal source, an industrial process with waste heat, a heat pump, a heat source, a heat sink, or a source of environmentally chilled water.

30. The system of claim 26, wherein the source of recovered thermal energy comprises a thermal well.

31. The system of claim 26, wherein the fluid transfers at least a portion of the recovered thermal energy for use as at least one of process heat, cooling, or building conditioning.