Configurations and methods for thermal integration of LNG regasification and power plants

• US 8,196,413 B2
• Filed: 03/21/2006
• Issued: 06/12/2012
• Est. Priority Date: 03/30/2005
• Status: Expired due to Fees

• Current Assignee: Fluor Technologies Corporation (Fluor Corporation)
• Original Assignee: Fluor Technologies Corporation (Fluor Corporation)
• Inventors: Mak, John
• Primary Examiner(s): CASAREGOLA, LOUIS J
• Application Number:
  US11/908,770
• Publication Number:
  US 20080276617A1
• Time in Patent Office: 2,275 Days
• Field of Search: 60/391.82, 60/394.65, 60/395.3, 60/395.9, 607/28, 607/75
• US Class Current: 60/775
• CPC Class Codes: F02C 3/22 the fuel or oxidant being gaseous at standard temperature and pressure F02C3/28 takes precedence
• CPC Class Codes: F02C 7/22 Fuel supply systems
• CPC Class Codes: Y02E 20/16 Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
• CPC Class Codes: Y02E 20/18 Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]

Abstract

Contemplated plants integrate regeneration of a freeze point depressant with LNG regasification and a power cycle. Most preferably, the plant is a combined cycle plant in which heat for reboiling the regenerator is provided by the steam cycle, and in which LNG refrigeration content is used to condense steam from the regenerator and to further subcool intake air for a combustion turbine.

Claims

1. A thermally integrated regenerator configuration comprising:

a regenerator configured to receive a rich freeze point depressant solution and further configured to form steam and a lean freeze point depressant solution from the rich solution;

wherein the regenerator is thermally coupled to an LNG-cooled heat transfer fluid circuit such that heat from the steam can be transferred to the heat transfer fluid; and

wherein the regenerator is further thermally coupled to a steam cycle such that heat from the steam cycle can be transferred to the rich freeze point depressant solution in the regenerator.

2. The regenerator configuration of claim 1 further comprising an air intake chiller thermally coupled to the LNG-cooled heat transfer fluid circuit, and further fluidly coupled to a mixing device, wherein the mixing device is configured to receive the lean freeze point depressant solution and to allow mixing of the lean freeze point depressant solution with air.

3. The regenerator configuration of claim 2 wherein the air intake chiller is configured to chill the air-lean freeze point depressant solution mixture to a temperature of less than 32°

F.

4. The regenerator configuration of claim 3 further comprising a separator that is fluidly coupled to the air intake chiller and that is configured to allow removal the rich freeze point depressant solution from the chilled mixture.

5. The regenerator configuration of claim 2 further comprising a second air intake chiller thermally coupled to the LNG-cooled heat transfer fluid circuit, and further upstream and fluidly coupled the air intake chiller.

6. The regenerator configuration of claim 1 further comprising a heat exchanger that is configured to allow cooling of the lean freeze point depressant solution using refrigeration content of the rich freeze point depressant solution.

7. The regenerator configuration of claim 1 wherein thermal coupling of the regenerator to the steam cycle comprises a circuit that is configured to receive at least partially expanded steam from a steam turbine of the steam cycle, to provide the at least partially expanded steam to a reboiler of the regenerator, and to return the at least partially expanded steam from the regenerator to the steam cycle.

8. The regenerator configuration of claim 1 wherein thermal coupling of the regenerator to the LNG-cooled heat transfer fluid circuit comprises a heat exchanger that is configured to provide heat from the steam to the LNG-cooled heat transfer fluid.

9. The regenerator configuration of claim 1 wherein the LNG-cooled heat transfer fluid comprises a glycol, or a solution with water absorption capacity at a temperature of 32°

F. or below.

10. The regenerator configuration of claim 1 wherein the lean freeze point depressant solution comprises a glycol.

11. A method of chilling intake air for a combustion turbine of a combined cycle power plant, comprising:

combining a cooled air stream with a lean freeze point depressant solution to thereby form a mixture, and subcooling the mixture to a temperature of below 32°

F.;

removing rich freeze point depressant solution from the subcooled mixture, and regenerating the lean freeze point depressant solution in a regenerator using heat from a working fluid of a steam power cycle of the combined cycle power plant, thereby forming steam as overhead product of the regenerator; and

condensing the steam using a LNG-cooled heat transfer fluid.

12. The method of claim 11 wherein the cooled air stream is formed by an upstream air chiller that cools ambient air to a temperature of between 35°

F. and 45°

F.

13. The method of claim 11 wherein the step of combining is performed using spraying the lean freeze point depressant solution into the cooled air stream.

14. The method of claim 11 wherein the subcooled mixture has a temperature of between 20°

F. and −

40°

F.

15. The method of claim 11 wherein the step of removing the rich freeze point depressant solution is performed in a separator that provides a cooled rich freeze point depressant solution.

16. The method of claim 15 wherein the cooled rich freeze point depressant solution is heat exchanged with heated lean freeze point depressant solution from the regenerator.

17. The method of claim 11 wherein the step of regenerating includes a step of providing at least partially expanded steam from a steam cycle to the regenerator to thereby form the steam and heated lean freeze point depressant solution.

18. The method of claim 17 wherein the at least partially expanded steam is returned from the regenerator to the steam cycle.

19. The method of claim 11 wherein at least one of the cooled air stream and the subcooled mixture is cooled using refrigeration content from the LNG-cooled heat transfer fluid.

20. The method of claim 11 wherein the LNG-cooled heat transfer fluid is heated using heat content from the steam from the regenerator.