SYSTEMS AND METHODS FOR ENERGY STORAGE AND RETRIEVAL

• US 20150260463A1
• Filed: 03/25/2015
• Published: 09/17/2015
• Est. Priority Date: 09/27/2012
• Status: Active Grant

• Current Assignee: Malta, Inc.
• Original Assignee: Gigawatt Day Storage Systems, Inc.
• Inventors: Laughlin, Robert B., Larochelle, Philippe, Cizek, Nicholas
• Granted Patent: US 10,012,448 B2
• Time in Patent Office: Days
• US Class Current: 1/1
• CPC Class Codes: F01K 13/02 Controlling, e.g. stopping or starting
• CPC Class Codes: F01K 3/00 Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein regenerating exhaust steam F01K19/00
• CPC Class Codes: F01K 3/12 having two or more accumulators
• CPC Class Codes: F01K 3/185 using waste heat from outside the plant F02G5/00 takes precedence
• CPC Class Codes: F01K 3/20 with heating by combustion gases of main boiler
• CPC Class Codes: F02C 1/10 Closed cycles
• CPC Class Codes: F02C 6/14 Gas-turbine plants having means for storing energy, e.g. for meeting peak loads
• CPC Class Codes: F05D 2250/90 Variable geometry
• CPC Class Codes: F24S 60/10 using latent heat
• CPC Class Codes: F28D 15/00 Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies F28D17/00, F28D19/00, F28D20/00 take precedence
• CPC Class Codes: F28D 20/00 Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
• CPC Class Codes: F28D 2020/0047 using molten salts or liquid metals
• CPC Class Codes: Y02E 10/40 Solar thermal energy, e.g. solar towers
• CPC Class Codes: Y02E 20/14 Combined heat and power generation [CHP]
• CPC Class Codes: Y02E 20/16 Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
• CPC Class Codes: Y02E 60/14 Thermal energy storage
• CPC Class Codes: Y02E 60/16 Mechanical energy storage, e.g. flywheels or pressurised fluids

Abstract

The present disclosure provides pumped thermal energy storage systems that can be used to store electrical energy. A pumped thermal energy storage system of the present disclosure can store energy by operating as a heat pump or refrigerator, whereby net work input can be used to transfer heat from the cold side to the hot side. A working fluid of the system is capable of efficient heat exchange with heat storage fluids on a hot side of the system and on a cold side of the system. The system can extract energy by operating as a heat engine transferring heat from the hot side to the cold side, which can result in net work output. Systems of the present disclosure can employ solar heating for improved storage efficiency.

Claims

1. An energy storage and retrieval system, comprising:

a compressor;

a first heat storage unit;

a turbine;

a second heat storage unit;

a working fluid that flows along a fluid flow path in a closed cycle including, in sequence, the compressor, the first heat storage unit, the turbine, and the second heat storage unit; and

an auxiliary tank comprising the working fluid, wherein the auxiliary tank is in fluid communication with the fluid flow path of the closed cycle; and

wherein the system alternately operates as both (i) a heat engine to provide mechanical work from heat and (ii) as a heat pump to use mechanical work to store heat.

3. The system of claim 1, wherein the mechanical work provided in (i) or used in (ii) varies with an absolute pressure of the working fluid in the closed cycle.

4. The system of claim 1, wherein the absolute pressure of the working fluid in the closed cycle varies with an amount of working fluid transferred between the auxiliary tank and the closed cycle.

5. The system of claim 1, wherein the first heat storage unit and the second heat storage unit are both capable of exchanging heat with the working fluid, and wherein the first heat storage unit or the second heat storage unit comprises:

a first thermal storage tank;

a second thermal storage tank;

a heat storage fluid capable of flowing between the first and second thermal storage tanks to store or release heat; and

a counter-flow heat exchanger, wherein the heat storage fluid and the working fluid flow in opposite directions.

11. The system of claim 1, further comprising a radiator operatively coupled to the apparatus to dissipate waste heat generated during operation of the apparatus.

19. The system of claim 1, wherein the first and/or second heat storage unit comprises a storage fluid held at about ambient pressure.

20. The system of claim 1, wherein the auxiliary tank is in fluid communication with the closed cycle at a high pressure side of the closed cycle, which high pressure side is after the compressor and before the turbine, and wherein the auxiliary tank is in fluid communication with the closed cycle at a low pressure side of the closed cycle, which low pressure side is after the turbine and before the compressor.

23. The system of claim 20, wherein the fluid communication is regulated by a valve.

24. The system of claim 1, wherein the auxiliary tank contains the working fluid at a pressure that is between a maximum and a minimum pressure of the working fluid in the closed cycle.

25. The system of claim 5, wherein the system further comprises (i) a solar heater for heating the heat storage fluid of the first heat storage unit or the working fluid, (ii) a combustion heat source for heating the heat storage fluid of the first heat storage unit or the working fluid, or (iii) a waste heat source for heating the heat storage fluid of the first heat storage unit or the working fluid.

64. The system of claim 5, further comprising a controller that is programmed to regulate (i) a temperature difference between any two thermally coupled fluid elements of the counter-flow heat exchanger, and/or (ii) one or more fluid properties of the fluid elements of the counter-flow heat exchanger such that entropy generation in the counter-flow heat exchanger is minimized during operation of the system.

67. The system of claim 64, wherein the controller is programmed to regulate (i) and/or (ii) such that, during use, a rate of entropy generation associated with the counter-flow heat exchanger is less than 20% of a rate of entropy generation within the system.

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30. A method for storing and releasing energy, the method comprising:

(a) providing a system comprising a closed cycle comprising, in sequence, a compressor, a first heat storage unit, a turbine and a second heat storage unit configured to circulate a working fluid, wherein the system further comprises an auxiliary tank for the working fluid, and wherein the first and second heat storage units exchange heat with the working fluid flowing through the closed cycle; and

(b) alternately and sequentially operating the system in a refrigerator mode and a heat engine mode, wherein in the refrigerator mode, mechanical work is used to transfer thermal energy from the second heat storage unit to the first heat storage unit, and wherein, in the heat engine mode, thermal energy transferred from the first heat storage unit to the second heat storage unit is used to provide mechanical work.

36. The method of claim 30, further comprising (i) transferring more thermal energy between the second heat storage unit and the first heat storage unit by increasing an absolute pressure of the working fluid, or (ii) transferring less thermal energy between the second heat storage unit and the first heat storage unit by decreasing an absolute pressure of the working fluid.

83. The method of claim 30, further comprising (i) in the refrigerator mode, storing energy at a rate of at least about 10 megawatt, or (ii) in the heat engine mode, extracting energy at a rate of at least about 10 megawatt.

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40. A method for storing and releasing energy, the method comprising:

(a) increasing the pressure of a working fluid, operating in a closed cycle comprising a fluid flow path configured to circulate the working fluid, from a first pressure to a second pressure with the aid of a compressor, thereby increasing the temperature of the working fluid;

(b) using a first heat storage unit downstream of the compressor and in thermal communication with the working fluid for (i) in a storing mode, removing-heat from the working fluid and decreasing the temperature of the working fluid, which decrease in temperature is at substantially the second pressure, or (ii) in a releasing mode, supplying heat to the working fluid and increasing the temperature of the working fluid, which increase in temperature is at substantially the second pressure;

(c) decreasing the pressure of the working fluid from the second pressure to the first pressure with the aid of a turbine, thereby decreasing the temperature of the working fluid;

(d) using a second heat storage unit downstream of the turbine and in thermal communication with the working fluid for (i) in a storing mode, supplying heat to the working fluid and increasing the temperature of the working fluid, which decrease in temperature is at substantially the first pressure, or (ii) in a releasing mode, removing heat from the working fluid and decreasing the temperature of the working fluid, which decrease in temperature is at substantially the first pressure; and

(e) with the aid of a recuperator in fluid communication with the fluid flow path, supplying heat to the working fluid or removing heat from the working fluid, wherein the working fluid does not undergo a phase change.

43. The method of claim 40, wherein the first heat storage unit is capable of exchanging heat with the working fluid between a first low temperature and a first high temperature, which first low temperature is lower than the first high temperature, wherein the second heat storage unit is capable of exchanging heat with the working fluid between a second low temperature and a second high temperature, which second low temperature is lower than the second high temperature, and wherein the first low temperature is higher than the second high temperature.

48. The method of claim 43, wherein (e) comprises exchanging heat with the working fluid between the first low temperature and the second high temperature using the recuperator.

49. The method of claim 48, wherein (e) further comprises transferring heat between a portion of the working fluid flowing along a high pressure portion of the closed cycle and a portion of the working fluid flowing along a low pressure portion of the closed cycle.

54. The system of claim 43, wherein the working fluid is capable of (i) exchanging heat between the second low temperature and the first low temperature in a low pressure portion of the closed cycle, or (ii) exchanging heat between the second high temperature and the first high temperature in a high pressure portion of the closed cycle.

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