SUPERCRITICAL CO2 TURBINE FOR USE IN SOLAR POWER PLANTS

• US 20100024421A1
• Filed: 12/08/2006
• Published: 02/04/2010
• Est. Priority Date: 12/08/2006
• Status: Active Grant

• Current Assignee: SolarReserve Technology, LLC
• Original Assignee: United Technologies Corporation (Raytheon Technologies Corporation d/b/a RTX)
• Inventors: Hoffman, Nathan J., Litwin, Robert Z., Wait, David, von Arx, Alan V., Zillmer, Andrew J.
• Granted Patent: US 7,685,820 B2
• Time in Patent Office: Days
• US Class Current: 60/641.800
• CPC Class Codes: F02C 1/05 characterised by the type or source of heat, e.g. using nuclear or solar energy
• CPC Class Codes: F03G 6/067 Binary cycle plants where the fluid from the solar collector heats the working fluid via a heat exchanger
• CPC Class Codes: Y02E 10/46 Conversion of thermal power into mechanical power, e.g. Rankine, Stirling or solar thermal engines
• CPC Class Codes: Y02P 80/10 Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
• CPC Class Codes: Y02P 80/20 using renewable energy

Abstract

A solar-powered supercritical carbon dioxide turbine system includes a supercritical carbon dioxide turbine system and a solar heating system. The solar heating system has a molten salt heat transfer fluid for providing thermal energy to the supercritical carbon dioxide turbine system.

Claims

1. A turbine system comprising:

a supercritical carbon dioxide turbine having an outlet;

a high temperature recuperator having a first inlet connected to the outlet of the supercritical carbon dioxide turbine and a first outlet;

a low temperature recuperator having a first inlet connected to the first outlet of the high temperature recuperator and a first outlet;

a first valve having an inlet, a first outlet and a second outlet, wherein the first inlet of the first valve is connected to the first outlet of the low temperature recuperator;

a compressor connected to the first outlet of the first valve;

a precooler connected to the second outlet of the first valve; and

a solar heating system having a molten salt heat transfer fluid for providing thermal energy to the supercritical carbon dioxide turbine.

2. The turbine system of claim 1, wherein the supercritical carbon dioxide turbine operates at a temperature of at least about 1022 degrees Fahrenheit.

3. The turbine system of claim 1, wherein the molten salt heat transfer fluid comprises between about 50% sodium nitrate and about 70% sodium nitrate and between about 30% potassium nitrate and about 50% potassium nitrate by weight.

4. The turbine system of claim 1, wherein the solar heating system heats the molten salt heat transfer fluid to a temperature of at least about 1065 degrees Fahrenheit.

5. The turbine system of claim 1, wherein the supercritical carbon dioxide turbine comprises a supercritical carbon dioxide Brayton power conversion cycle.

6. The turbine system of claim 1, and further comprising a heat exchanger, wherein the thermal energy is transferred from the molten salt heat transfer fluid to a carbon dioxide Brayton cycle working fluid.

7. A system for providing energy for a supercritical carbon dioxide turbine, the system comprising:

a Brayton cycle working fluid for providing energy to the supercritical carbon dioxide turbine;

a high temperature recuperator that receives the Brayton working fluid from the supercritical carbon dioxide turbine and cools it;

a low temperature recuperator that receives the Brayton working fluid from the high temperature recuperator and cools it;

a precooler;

a first valve that divides the Brayton cycle working fluid cooled by the low temperature recuperator into a first portion that flows through the precooler and a second portion that does not flow through the precooler;

a second valve that combines the first portion of the Brayton cycle working fluid that is cooled by the precooler and the second portion of the Brayton cycle working fluid that is not cooled by the precooler; and

a solar receiver for heating a heat transfer fluid to a temperature of at least about 1065 degrees Fahrenheit, wherein the heat transfer fluid is in communication with the Brayton cycle working fluid.

8. The system of claim 7, wherein the supercritical carbon dioxide turbine operates at an inlet temperature of about 1022 degrees Fahrenheit.

9. The system of claim 7, wherein the heat transfer fluid comprises molten salt.

10. The system of claim 9, wherein the molten salt heat transfer fluid comprises between about 50% sodium nitrate and about 70% sodium nitrate and between about 30% potassium nitrate and about 50% potassium nitrate by weight.

11. The system of claim 9, wherein the heat transfer fluid provides thermal energy to the supercritical carbon dioxide turbine.

12. The system of claim 11, and further comprising a heat exchanger, wherein the thermal energy is transferred from the molten salt to carbon dioxide.

13. The system of claim 7, wherein the system is a solar heating system.

14. A method of generating electricity with a supercritical carbon dioxide turbine, the method comprising:

capturing solar energy from sunlight;

heating a heat transfer fluid to a temperature of at least about 1065 degrees Fahrenheit with the solar energy;

transporting energy from the heat transfer fluid to heat a Brayton cycle working fluid of the supercritical carbon dioxide turbine;

passing the heated Brayton cycle working fluid through the supercritical carbon dioxide turbine;

cooling the Brayton cycle working fluid from the supercritical carbon dioxide turbine with a high temperature recuperator;

cooling the Brayton cycle working fluid from the high temperature recuperator with a low temperature recuperator;

dividing the cooled Brayton cycle working fluid from the low temperature recuperator into a first portion and a second portion;

cooling the first portion of the Brayton cycle working fluid;

not cooling the second portion of the Brayton cycle working fluid; and

combining the first portion of the Brayton cycle working fluid and the second portion of the Brayton cycle working fluid that is not cooled after the step of cooling the first portion of the Brayton cycle working fluid.

15. The method of claim 14, wherein capturing solar energy comprises using a solar heating system.

16. The method of claim 14, wherein the heat transfer fluid comprises molten salt.

17. The method of claim 16, wherein the molten salt heat transfer fluid comprises between about 50% sodium nitrate and about 70% sodium nitrate and between about 30% potassium nitrate and about 50% potassium nitrate by weight.

18. The method of claim 14, wherein transporting the energy of the heat transfer fluid to heat the Brayton cycle working fluid of the supercritical carbon dioxide turbine comprises using a heat exchanger.

19. The method of claim 14, wherein the heat transfer fluid provides thermal energy to the supercritical carbon dioxide turbine.

20. The method of claim 14, wherein the supercritical carbon dioxide turbine comprises a supercritical carbon dioxide Brayton power conversion cycle.