Electrothermal energy storage system and an associated method thereof

Patent metadata

Field	Value
Publication number	US-9695715-B2
Application number	US-201414554081-A
Country	US
Kind code	B2
Filing date	Nov 26, 2014
Priority date	Nov 26, 2014
Publication date	Jul 4, 2017
Grant date	Jul 4, 2017

Abstract

An electrothermal energy storage and discharge system is provided including a charging cycle and a discharging cycle. The charging cycle includes a refrigeration unit and a thermal unit, and the discharging cycle includes a power unit. The refrigeration unit is driven by an excess electric power and is configured to generate a cold energy storage having a solid carbon dioxide. The thermal unit is driven by a thermal energy and is configured to generate a hot energy storage and/or provide a hot source. The power unit operates between the cold energy storage and at least one of the hot energy storage and hot source so as to retrieve the energy by producing a high pressure carbon dioxide and a hot supercritical carbon dioxide, and generating an electric energy using the hot supercritical carbon dioxide.

First claim

The invention claimed is:

1. An electrothermal energy storage system having a charging cycle and a discharging cycle, the system comprising:
a refrigeration unit configured to generate a cold energy storage comprising a solid carbon dioxide, wherein the refrigeration unit is driven by an electric power, and wherein the refrigeration unit comprises a liquid pump configured to increase pressure of a liquid carbon dioxide, an expansion device configured to expand the liquid carbon dioxide to produce the solid carbon dioxide and a vaporized carbon dioxide, a compressor configured to increase pressure of the vaporized carbon dioxide, and a cooling unit configured to convert the vaporized carbon dioxide into the liquid carbon dioxide by exchanging heat with an ambient environment;
a thermal unit configured to provide at least one of a hot energy storage and a hot source; and
a power unit configured to operate between the cold energy storage and at least one of the hot energy storage, and the hot source to retrieve energy,
wherein the power unit is configured to produce a high pressure carbon dioxide and a supercritical carbon dioxide, and to generate an electric energy using the supercritical carbon dioxide.

2. The system of claim 1 , wherein the refrigeration unit further comprises a storage tank configured to store the liquid carbon dioxide, and the solid carbon dioxide at a triple point of a carbon dioxide to generate the cold energy storage.

3. The system of claim 1 , wherein the refrigeration unit further comprises a storage tank including a first insulated tank configured to store the liquid carbon dioxide, and a second insulated tank configured to store the solid carbon dioxide to generate the cold energy storage.

4. The system of claim 1 , wherein the thermal unit is driven by a thermal energy to generate the hot energy storage comprising a hot molten salt, wherein the thermal energy comprises at least one of a waste heat and a solar energy.

5. The system of claim 1 , wherein the hot source is produced by a thermal energy comprising at least one of a waste heat and a solar energy.

6. The system of claim 1 , wherein the power unit comprises a liquid pump configured to increase pressure of a liquid carbon dioxide received from at least one of a storage tank and a mixing chamber to produce the high pressure carbon dioxide.

7. The system of claim 6 , wherein the power unit further comprises a first heat exchanger configured to heat the liquid carbon dioxide by exchanging heat with a vaporized carbon dioxide received from a turbine exhaust to produce the supercritical carbon dioxide.

8. The system of claim 7 , wherein the power unit further comprises a second heat exchanger configured to further heat the supercritical carbon dioxide by exchanging heat with at least one of the hot energy storage and the hot source.

9. The system of claim 8 , wherein the power unit further comprises a turbine configured to expand the supercritical carbon dioxide, and a generator coupled to the turbine and configured to be driven by the turbine to generate the electric energy.

10. The system of claim 1 , wherein the power unit further comprises a posimetric pump configured to increase pressure of the solid carbon dioxide received from a storage tank comprising a first insulated tank, to produce a pressurized solid carbon dioxide, and a mixing chamber configured to directly mix the pressurized solid carbon dioxide with a vaporized carbon dioxide received from a turbine exhaust to produce a liquid carbon dioxide.

11. The system of claim 1 , wherein the charging and discharging cycles operate transcritically to store and retrieve energy directly through a carbon dioxide.

12. A method for storing and retrieving energy in an electrothermal energy storage system, the method comprising:
generating a cold energy storage by converting a liquid carbon dioxide into a solid carbon dioxide through a refrigeration unit driven by an electric power, wherein the refrigeration unit is configured to increase pressure of the liquid carbon dioxide using a liquid pump, expand the liquid carbon dioxide to produce the solid carbon dioxide and a vaporized carbon dioxide using an expansion device, compress the vaporized carbon dioxide to increase pressure of the vaporized carbon dioxide using a compressor, and convert the vaporized carbon dioxide into the liquid carbon dioxide by exchanging heat with an ambient environment using a cooling unit;
providing at least one of a hot energy storage, and a hot source through a thermal unit driven by a thermal energy comprising at least one of a waste heat and a solar energy; and
retrieving the energy in the solid carbon dioxide by operating a power unit between the cold energy storage and at least one of the hot energy storage, and the hot source,
wherein the power unit is configured to produce a high pressure carbon dioxide, a supercritical carbon dioxide, and to generate an electric energy using the supercritical carbon dioxide.

13. The method of claim 12 , further comprising storing the solid carbon dioxide, and the liquid carbon dioxide at a triple point of a carbon dioxide in a storage tank to generate the cold energy storage.

14. The method of claim 12 , further comprising storing the solid carbon dioxide in a storage tank comprising an insulated tank to generate the cold energy storage.

15. The method of claim 12 , wherein the providing comprises generating the hot energy storage by adding heat to a molten salt via the thermal unit.

16. The method of claim 12 , wherein the retrieving comprises increasing pressure of the liquid carbon dioxide received from at least one of a storage tank and a mixing chamber to produce the high pressure carbon dioxide.

17. The method of claim 16 , wherein the retrieving further comprises heating the high pressure carbon dioxide to produce the supercritical carbon dioxide by exchanging heat with a vaporized carbon dioxide received from a turbine exhaust via a first heat exchanger.

18. The method of claim 17 , wherein the retrieving further comprises further heating the supercritical carbon dioxide by exchanging heat with at least one of the hot energy storage, and the hot source via a second heat exchanger.

19. The method of claim 18 , wherein the retrieving further comprises expanding the supercritical carbon dioxide via a turbine, and generating the electric energy via a generator coupled to the turbine and configured to be driven by the turbine.

20. The method of claim 12 , further comprising increasing pressure of the solid carbon dioxide received from a storage tank comprising an insulated tank to produce a pressurized solid carbon dioxide, and directly mixing the pressurized solid carbon dioxide with a vaporized carbon dioxide received from a turbine exhaust to produce the liquid carbon dioxide.

Assignees

• Gen Electric

Inventors

• Kalra Chiranjeev Singh
• Peter Andrew Maxwell
• Shisler Roger Allen

Classifications

• F03G6/066

  of the Organic Rankine Cycle [ORC] type or the Kalina Cycle type · CPC title

• F28D20/00

  Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 · CPC title

• F28D2020/0047

  using molten salts or liquid metals · CPC title

• Y02E10/46

  Conversion of thermal power into mechanical power, e.g. Rankine, Stirling or solar thermal engines · CPC title

• F01K25/103 Primary

  Carbon dioxide (F01K25/065 takes precedence) · CPC title