Multi-fluid, earth battery energy systems and methods

Patent metadata

Field	Value
Publication number	US-11873740-B2
Application number	US-202117397515-A
Country	US
Kind code	B2
Filing date	Aug 9, 2021
Priority date	Mar 16, 2018
Publication date	Jan 16, 2024
Grant date	Jan 16, 2024

Abstract

The present disclosure relates to a system for storing and time shifting at least one of excess electrical power from an electrical power grid, excess electrical power from the power plant itself, or heat from a heat generating source, in the form of pressure and heat, for future use in assisting with a production of electricity. An oxy-combustion furnace is powered by a combustible fuel source, plus excess electricity, during a charge operation to heat a reservoir system containing a quantity of a thermal storage medium. During a discharge operation, a discharge subsystem has a heat exchanger which receives heated CO 2 from the reservoir system and uses this to heat a quantity of high-pressure, supercritical CO 2 (sCO 2 ) to form very-high-temperature, high-pressure sCO 2 at a first output thereof. The very-high-temperature, high-pressure sCO 2 is used to drive a Brayton-cycle turbine, which generates electricity at a first output thereof for transmission to a power grid. The Brayton-cycle turbine also outputs a quantity of sCO 2 which is reduced in temperature and pressure to a heat recuperator subsystem. The heat recuperator subsystem circulates the sCO 2 and re-heats and re-pressurizes the sCO 2 before feeding it back to the heat exchanger to be even further reheated, and then output to the Brayton-cycle turbine as a new quantity of very-high-temperature, high-pressure sCO 2 , to assist in powering the Brayton-cycle turbine.

First claim

What is claimed is:

1. A system for storing and time-shifting at least one of excess electrical power from an electrical power grid, excess electrical power from a power plant, or heat from a heat generating source, in the form of pressure and heat, for future use in assisting with a production of electricity, the system comprising:
a reservoir system containing a quantity of a thermal storage medium, the thermal storage medium including at least one of sand, rocks, manufactured granular material including at least one of ceramic pebbles, or a mixture of manufactured granular material, sand, and rocks, and being configured to be heated using a combustible fuel source;
an oxy-combustion furnace for heating the thermal storage medium during a charge operation using O 2 , and at least one of natural gas, coal, coke, petroleum, petroleum coke, tires, solid waste, biomass, or electricity supplied from the electrical power grid or the power plant;
a discharge subsystem including:
a heat exchanger having a first input configured to receive heated CO 2 from the reservoir system during a discharge operation of the system and to generate a first quantity of supercritical CO 2 (sCO 2 ) at a first temperature and a first pressure, at a first output thereof;
a power generating component for receiving the first quantity of sCO 2 from the first output of the heat exchanger and generating electricity therefrom at a first output thereof for transmission to the power grid, the power generating component also configured to produce a second quantity of sCO 2 having a second temperature and a second pressure at a second output thereof, the second temperature and the second pressure each being lower than the first temperature and the first pressure; and
a recuperator subsystem for circulating the second quantity of sCO 2 to reheat and re-pressurize the second quantity of sCO 2 to create a third quantity of sCO 2 , for reapplication to the heat exchanger, to be further reheated by the heat exchanger to create a quantity of sCO 2 which is output to the power generating component to further assist in powering the power generating component.

2. The system of claim 1 , wherein the third quantity of sCO 2 has a third temperature and a third pressure; and
the heat exchanger having a second input for receiving the third quantity of sCO 2 from the recuperator subsystem and using the third quantity of sCO 2 to help produce the re-heated third quantity of sCO 2 with a temperature and pressure similar to that of the first quantity of sCO 2 .

3. The system of claim 2 , wherein the recuperator subsystem comprises:
a plurality of recuperators for sequentially extracting heat from the second quantity of sCO 2 in a plurality of stages.

4. The system of claim 3 , wherein the plurality of recuperators comprise:
a first recuperator configured to receive the second quantity of sCO 2 and to output the second quantity of sCO2 as the third quantity of sCO2 with a reduced temperature and having a reduced pressure;
a second recuperator configured to receive an additional quantity of sCO2 and to reduce at least one of a pressure or a temperature of the additional quantity of sCO2 to create a first output therefrom for further use by the system.

5. The system of claim 4 , further comprising a third recuperator configured to receive the first output of the sCO 2 from the second recuperator and to generate a quantity of cool sCO 2 .

6. The system of claim 5 , wherein the recuperator subsystem includes a cooler for receiving and cooling the quantity of cool sCO 2 from the third recuperator to produce a quantity of cold CO 2 .

7. The system of claim 6 , further comprising a low-pressure compressor for receiving the quantity of cold CO 2 and generating a fifth output of sCO 2 with a fourth pressure between the second and third pressures.

8. The system of claim 7 , wherein the recuperator subsystem includes a flow splitter for receiving and splitting the fifth output of sCO 2 from the low-pressure compressor into first and second subquantities of sCO 2 and providing the first and second subquantities of sCO 2 to different ones of the second and third recuperators.

9. The system of claim 8 , further comprising a first high-pressure compressor for receiving one of the first and second subquantities of sCO 2 from the flow splitter, further pressurizing the received one of the first and second subquantities of sCO 2 and providing a sixth quantity of sCO 2 back to the second recuperator.

10. The system of claim 9 , further comprising an intercooler interposed between the flow splitter and the first high-pressure compressor for cooling the one of the first and second subquantities of sCO 2 from the flow splitter before passing the one of the first and second subquantities of sCO 2 to the first high-pressure compressor.

11. The system of claim 10 , further comprising a second high-pressure compressor for receiving a quantity of sCO 2 from the third recuperator and generating a pressurized quantity of sCO 2 .

12. The system of claim 11 , further comprising a flow mixer for receiving the pressurized quantity of sCO 2 from the second high-pressure compressor and providing a quantity of highly pressurized sCO 2 to the first recuperator.

13. The system of claim 1 , further comprising:
a dryer subsystem for receiving a mixture of gaseous CO 2 and water vapor from the reservoir system and generating therefrom CO 2 during the charging operation;
a compressor for receiving the CO 2 and pressurizing the CO 2 for transmission to a CO 2 storage reservoir.

14. The system of claim 1 , wherein the recuperator subsystem comprises a closed loop subsystem.

15. A system for storing and time-shifting at least one of excess electrical power from an electrical power grid, excess electrical power from a power plant itself, or heat from a heat generating source, in a form of pressure and heat, for future use in assisting with a production of electricity, the system comprising:
a reservoir system containing a quantity of a thermal storage medium, the thermal storage medium including at least one of sand, rocks, manufactured granular material including at least one of ceramic pebbles, or a mixture of manufactured granular material, sand, and rocks, and being configured to be heated;
an oxy-combustion furnace for heating the thermal storage medium during a charge operation using O 2 and at least one of natural gas, coal, coke, petroleum, petroleum coke, tires, solid waste, or biomass, or electricity supplied from the power grid or the power plant;
a dryer subsystem for receiving a mixture of gaseous CO 2 and water vapor from the reservoir system and generating therefrom CO 2 during a charging operation;
a compressor for receiving the CO 2 and pressurizing the CO 2 for transmission to a CO 2 storage reservoir;
a discharge subsystem including:
a heat exchanger having a first input configured to receive heated CO 2 from the oxy-combustion furnace during a discharge operation of the system and to generate a first quantity of supercritical CO 2 (sCO 2 ) at a first temperature and a first pressure, at a first output thereof;
a Brayton-cycle turbine for receiving the first quantity of sCO 2 from the first output of the heat exchanger and generating electricity therefrom at a first output thereof for transmission to the power grid, the Brayton-cycle turbine also configured to produce a second quantity of sCO 2 having a second temperature and a second pressure at a second output thereof, the second temperature and the second pressure each being lower than the f

Assignees

• L Livermore Nat Security Llc

Inventors

• Buscheck Thomas A
• Upadhye Ravindra Shrikrishna

Classifications

• F03G4/063

  with energy storage devices · CPC title

• F01K25/103 Primary

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

• F24T10/20 Primary

  using underground water as working fluid; using working fluid injected directly into the ground, e.g. using injection wells and recovery wells · CPC title

• F01K27/00

  Plants for converting heat or fluid energy into mechanical energy, not otherwise provided for · CPC title

• F03G7/04

  using pressure differences or thermal differences occurring in nature (F03G7/06 takes precedence) · CPC title