Compound closed-loop heat cycle system for recovering waste heat and method thereof

• US 8,490,397 B2
• Filed: 11/16/2009
• Issued: 07/23/2013
• Est. Priority Date: 11/16/2009
• Status: Active Grant

• Current Assignee: Nuovo Pignone Tecnologie SRL (Nuovo Pignone International SRL)
• Original Assignee: General Electric Company
• Inventors: Lehar, Matthew Alexander
• Primary Examiner(s): Bomberg, Kenneth
• Assistant Examiner(s): Wan, Deming
• Application Number:
  US12/618,958
• Publication Number:
  US 20110113780A1
• Time in Patent Office: 1,345 Days
• Field of Search: 606/51, 606/73, 606/53, 606/41, 606/94, 603/78
• US Class Current: 60/651
• CPC Class Codes: F02C 1/007 combination of cycles
• CPC Class Codes: F02C 1/10 Closed cycles
• CPC Class Codes: F02C 6/18 using the waste heat of gas-turbine plants outside the plants themselves, e.g. gas-turbine power heat plants using waste heat as source of energy for refrigeration plants F25B27/02; using the waste heat of a gasturbine for steam generation or in a steam cycle see F01K23/10

Abstract

A waste heat recovery system includes a Brayton cycle system having an heater configured to circulate carbon dioxide vapor in heat exchange relationship with a hot fluid to heat carbon dioxide vapor. A Rankine cycle system is coupled to the Brayton cycle system and configured to circulate a working fluid in heat exchange relationship with the carbon dioxide vapor to heat the working fluid.

Claims

1. A waste heat recovery system, comprising:

a Brayton cycle system comprising;

a heater configured to circulate carbon dioxide vapor in heat exchange relationship with a hot fluid to heat the carbon dioxide vapor;

a first turbine coupled to the heater and configured to expand the carbon dioxide vapor;

a cooler; and

a compressor configured to compress the carbon dioxide vapor fed through the cooler; and

a Rankine cycle system coupled to the Brayton cycle system;

wherein the Rankine system comprises;

a first heat exchanger, a second heat exchanger, and a third heat exchanger, wherein the carbon dioxide vapor from the first turbine is circulated in heat exchange relationship with a vaporized working fluid sequentially via the first heat exchanger, the second heat exchanger, and the third heat exchanger to heat the working fluid;

wherein the cooler is configured to cool the carbon dioxide vapor fed through the first heat exchanger, the second heat exchanger, and the third heat exchanger;

a fourth heat exchanger configured to circulate the vaporized working fluid in heat exchange relationship with the carbon dioxide vapor fed from the compressor so as to heat the working fluid

a second turbine configured to expand the vaporized working fluid fed from the fourth heat exchanger via the first heat exchanger; and

a condenser configured to condense the vaporized working fluid fed from the second turbine via the third heat exchanger.

2. The system of claim 1, wherein the Brayton cycle system comprises a first generator coupled to the first turbine and configured to generate power.

3. The system of claim 1, wherein the Rankine cycle system comprises a second generator coupled to the second turbine and configured to generate power.

4. The system of claim 1, wherein the Rankine cycle system comprises a pump configured to pressurize and feed the condensed working fluid from the condenser to the third heat exchanger to vaporize the condensed working fluid.

5. The system of claim 4, wherein a Rankine cycle system comprises a flow splitter device configured to feed one portion of the vaporized working fluid from the third heat exchanger to the fourth heat exchanger and another portion of the vaporized working fluid from the third heat exchanger to a point upstream of the first heat exchanger;

wherein the other portion of the vaporized working fluid from the third heat exchanger is mixed with the vaporized working fluid fed from the fourth heat exchanger to the first heat exchanger.

6. The system of the claim 1, wherein the working fluid comprises a hydrocarbon.

7. A method comprising:

circulating carbon dioxide vapor in heat exchange relationship with a hot fluid to heat the carbon dioxide vapor via an heater of a Brayton cycle system;

expanding the carbon dioxide vapor via a first turbine coupled to the heater of the Brayton cycle system;

circulating the carbon dioxide vapor from the first turbine in heat exchange relationship with a vaporized working fluid sequentially via a first heat exchanger, a second heat exchanger, and a third heat exchanger of the Rankine cycle system to heat the vaporized working fluid;

cooling the carbon dioxide vapor fed through the first heat exchanger, the second heat exchanger, and the third heat exchanger via a cooler of the Brayton cycle system;

compressing the carbon dioxide vapor fed through the cooler via a compressor of the Brayton cycle system;

circulating the vaporized working fluid in heat exchange relationship with the carbon dioxide vapor fed from the compressor so as to heat the vaporized working fluid via a fourth heat exchanger of the Rankine cycle system

expanding the vaporized working fluid fed through the fourth heat exchanger, the first heat exchanger via a second turbine of the Rankine cycle system; and

condensing the vaporized working fluid fed from the second turbine via the third heat exchanger, using a condenser of the Rankine cycle system.

8. The method of claim 7, further comprising generating power via a first generator coupled to the first turbine of the Brayton cycle system.

9. The method of claim 7, further comprising generating power via a second generator coupled to the second turbine of the Rankine cycle system.

10. The method of claim 7, further comprising pressurizing and feeding the condensed working fluid from the condenser to the third heat exchange via a pump of the Rankine cycle system.

11. The method of claim 10, further comprising feeding one portion of the vaporized working fluid from the third heat exchanger to the fourth heat exchanger and another portion of the vaporized working fluid from the third heat exchanger to a point upstream of the first heat exchanger via a flow splitter device of the Rankine cycle system.

12. The method of claim 11, further comprising mixing the other portion of the vaporized working fluid from the third heat exchanger with the vaporized working fluid fed from the fourth heat exchanger to the first heat exchanger.