Power plant using CO.sub.2 as a working fluid

• US 4,765,143 A
• Filed: 02/04/1987
• Issued: 08/23/1988
• Est. Priority Date: 02/04/1987
• Status: Expired due to Term

• Current Assignee: CBI Research Corporation Plainfield IL
• Original Assignee: CBI Research Corporation
• Inventors: Fischer, Harry C., Crawford, John T., Tyree, Lewis Jr., Coers, Don H.
• Primary Examiner(s): Ostrager, Allen M.
• Application Number:
  US07/010,685
• Time in Patent Office: 566 Days
• Field of Search: 60/651, 60/671, 60/692
• US Class Current: 60/671
• CPC Class Codes: F01K 25/103 Carbon dioxide F01K25/065 takes precedence
• 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: Y02E 20/16 Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]

Abstract

A system for storing electrical energy in the form of triple-point CO₂ and then using such stored energy plus heat to generate electrical power. A reservoir of carbon dioxide liquid at about the triple point is created in an insulated vessel. Liquid carbon dioxide is withdrawn and pumped to a high pressure, which high pressure carbon dioxide is heated and expanded to create rotary power which generates electrical power. The discharge stream from the expander is cooled and returned to the vessel where carbon dioxide vapor is condensed by melting solid carbon dioxide. A fuel-fired gas turbine connected to an electrical power generator can be used to heat the high pressure carbon dioxide, and an ambient air stream flowing toward the gas turbine can be cooled by giving up heat to the high pressure carbon dioxide stream. The returning expanded carbon dioxide stream can be returned to a separate auxiliary vessel, and liquid carbon dioxide pumped from such auxiliary vessel to a main vessel wherein solid carbon dioxide is formed and then transferred to the auxiliary vessel.

Claims

1. A system for storing energy and then using such stored energy plus heat to generate power, which system comprises

insulated vessel means for storing liquid carbon dioxide at its triple point,

means for creating a reservoir of carbon dioxide liquid at about the triple point thereof in said vessel means, which reservoir contains a substantial amount of solid carbon dioxide,

means for withdrawing liquid carbon dioxide from said vessel means and very substantially increasing the pressure of said withdrawn liquid,

means for heating said higher pressure carbon dioxide,

means connected to an outlet from said heating means for expanding said heated carbon dioxide to dry vapor or to vapor containing some entrained liquid to create rotary power, and

means for returning the discharge stream from said expanding means to said vessel means where carbon dioxide vapor is condensed by melting solid carbon dioxide therein.

2. A system in accordance with claim 1 wherein said withdrawing means comprises pump means capable of increasing said carbon dioxide pressure to at least about 1000 psia.

3. A system in accordance with claim 1 wherein said heating means is connected to a source of heat above ambient.

4. A system in accordance with claim 1 wherein a first heat-exchanger is provided which forms a part of said heating means and which is arranged to cool said returning lower pressure carbon dioxide stream, said high pressure carbon dioxide being passed therethrough in heat exchange with said discharge stream from said expanding means.

5. A system in accordance with claim 4 wherein said heating means includes a fuel-fired gas turbine connected to rotary electrical power generation means, and wherein rotary electrical power generating means is linked to said expanding means.

6. A system in accordance with claim 5 wherein said heating means also includes a second heat-exchanger connected for heat exchange between hot exhaust gases from said gas turbine and said high pressure carbon dioxide from said first heat-exchanger.

7. A system in accordance with claim 6 wherein said heating means also includes a third heat-exchanger connected for heat exchange between said high pressure carbon dioxide and an air stream flowing toward said gas turbine.

8. A system in accordance with claim 7 wherein a fourth heat-exchanger is connected between said reservoir and said pressure-increasing means so that heat from said returning lower pressure carbon dioxide stream is given up to said liquid stream flowing toward said pressure-increasing means.

9. A system in accordance with claim 1 wherein said vessel means includes a main vessel and a separate auxiliary vessel, wherein said returning carbon dioxide stream is returned to said auxiliary vessel, wherein pump means is provided for transferring liquid carbon dioxide from said auxiliary vessel to said main vessel, and wherein means is provided for transferring solid carbon dioxide from said main vessel to said auxiliary vessel.

10. A method for storing energy and then using such stored energy plus heat to generate electrical power, which method comprises the following steps

creating a reservoir of carbon dioxide at about the triple point thereof, which reservoir contains a substantial percentage of solid carbon dioxide,

withdrawing a stream of liquid carbon dioxide from said reservoir and very substantially increasing the pressure of said stream of withdrawn liquid,

heating said higher pressure carbon dioxide,

expanding said heated carbon dioxide to dry vapor or to vapor containing some entrained liquid to create rotary power,

using said rotary power to generate electrical power, and

returning the lower pressure stream to said reservoir where carbon dioxide vapor is condensed by melting solid carbon dioxide therein.

11. A method in accordance with claim 10 wherein the pressure of said withdrawn carbon dioxide is increased to at least about 1000 psia.

12. A method in accordance with claim 11 wherein said high pressure carbon dioxide is heated to at least about 500°

F. prior to said expanding step.

13. A method in accordance with claim 12 wherein said lower pressure discharge stream from said expanding step is cooled to about -50°

F. or lower before being returned to said reservoir.

14. Apparatus for utilizing carbon dioxide slush in combination with the generation of power, which apparatus comprises:

vessel means including a main vessel for holding carbon dioxide slush to an internal depth of at least about 15 feet,

refrigeration means associated with said vessel means for creating a reservoir of carbon dioxide slush at the triple point,

means for withdrawing liquid carbon dioxide from said vessel means, increasing the pressure of said withdrawn carbon dioxide, heating said pressurized carbon dioxide and expanding said heated carbon dioxide in a manner to perform useful work used in the generation of power and to create carbon dioxide vapor,

said vessel means also including an auxiliary vessel,

means for transferring carbon dioxide slush from said main vessel to said auxiliary vessel,

means for returning said carbon dioxide vapor to said auxiliary vessel where it is condensed to liquid by melting solid carbon dioxide, and

means for transferring liquid carbon dioxide from said auxiliary vessel to said main vessel.

15. Apparatus according to claim 14 wherein said auxiliary vessel is located at a lower vertical level than said main vessel and said transfer of slush is assisted by gravity.

16. Apparatus according to claim 14 wherein separation means through which liquid CO₂ but not solid CO₂ will pass divides said auxiliary vessel into an upper portion and a lower portion from which liquid CO₂ is transferred to said main vessel.

17. Apparatus according to claim 14 wherein high pressure positive displacement pump means is provided for pressurizing said withdrawn liquid carbon dioxide and rotary expander means is provided for expanding said heated carbon dioxide.

18. Apparatus according to claim 17 wherein effluent from a combustion unit for generating electric power is provided for heating said pressurized carbon dioxide and wherein electrical generator means is linked to said carbon dioxide rotary expander means to utilize the power generated.

19. A method for utilizing carbon dioxide slush in combination with the generation of electric power, which method comprises:

establishing a reservoir zone containing carbon dioxide slush at the triple point to a depth of at least about 15 feet,

withdrawing liquid carbon dioxide from said reservoir zone, increasing the pressure of said withdrawn carbon dioxide, heating said pressurized carbon dioxide and expanding said heated carbon dioxide to create carbon dioxide vapor in a manner to perform useful work in connection with the ultimate generation of electric power,

transferring a portion of said carbon dioxide slush from a main section of said reservoir zone to a separate auxiliary section thereof,

returning said carbon dioxide vapor to said auxiliary reservoir section in a manner so that it is condensed to liquid by melting solid carbon dioxide, and

transferring liquid carbon dioxide from said auxiliary reservoir section to said main reservoir section.

20. A method according to claim 19 wherein said transfer of slush is by gravity flow.

21. A method according to claim 19 wherein said withdrawn carbon dioxide is heated by heat exchanger with returning CO₂ vapor, is thereafter pressurized to as least about 1000 psia and heated to at least about 500°

F.