Power generation and LNG production

Patent metadata

Field	Value
Publication number	US-9618261-B2
Application number	US-201414182048-A
Country	US
Kind code	B2
Filing date	Feb 17, 2014
Priority date	Mar 8, 2013
Publication date	Apr 11, 2017
Grant date	Apr 11, 2017

Abstract

The present techniques are directed to a system and method for generating power and producing liquefied natural gas (LNG). The system includes a power plant configured to generate power, wherein an exhaust gas from the power plant provides a gas mixture including nitrogen and carbon dioxide. The system also includes a dehydration system configured to dehydrate the gas mixture to generate a nitrogen refrigerant stream and a refrigeration system configured to produce LNG from a natural gas stream using the nitrogen refrigerant stream.

First claim

What is claimed is:

1. A system for generating power and producing liquefied natural gas (LNG), comprising:
a power plant configured to generate power, wherein an exhaust gas from the power plant provides a gas mixture comprising nitrogen and carbon dioxide;
a dehydration system configured to dehydrate the gas mixture to generate a nitrogen refrigerant stream; and
a refrigeration system configured to produce LNG from a natural gas stream using the nitrogen refrigerant stream.

2. The system of claim 1 , comprising a carbon dioxide separation system configured to separate the carbon dioxide from the gas mixture.

3. The system of claim 2 , wherein the carbon dioxide separation system separates the carbon dioxide from the gas mixture via an amine separation process.

4. The system of claim 2 , wherein the carbon dioxide separation system separates the carbon dioxide from the gas mixture via a potassium carbonate separation process.

5. The system of claim 1 , wherein the power plant comprises:
an expander turbine configured to provide mechanical energy by extracting energy from the gas mixture after combustion of the gas mixture in a combustor; and
a generator configured to generate electricity from the mechanical energy provided by the expander turbine.

6. The system of claim 1 , wherein the power plant comprises a combined cycle power plant.

7. The system of claim 6 , wherein the combined cycle power plant comprises:
an expander turbine configured to provide mechanical energy by extracting energy from the gas mixture after combustion of the gas mixture in a combustor;
a heat recovery steam generator (HRSG) configured to generate steam by heating a boiler with an exhaust stream from the expander turbine;
a steam turbine configured to provide mechanical energy by extracting energy from the steam generated by the HRSG; and
a generator configured to generate electricity from the mechanical energy provided by the expander turbine and the steam turbine.

8. The system of claim 6 , wherein the combined cycle power plant comprises:
an expander turbine configured to provide mechanical energy by extracting energy from the gas mixture after combustion of the gas mixture in a combustor;
a first generator configured to generate electricity from the mechanical energy provided by the expander turbine;
a heat recovery steam generator (HRSG) configured to generate steam by heating a boiler with an exhaust stream from the expander turbine;
a steam turbine configured to provide mechanical energy by extracting energy from the steam generated by the HRSG; and
a second generator configured to generate electricity from the mechanical energy provided by the steam turbine.

9. The system of claim 1 , wherein a portion of the gas mixture is recycled to the power plant.

10. The system of claim 1 , wherein the refrigeration system comprises a plurality of heat exchangers configured to chill the natural gas stream to produce the LNG via indirect heat exchange with the nitrogen refrigerant stream.

11. The system of claim 1 , wherein the refrigeration system comprises a nitrogen refrigeration loop.

12. The system of claim 11 , wherein the nitrogen refrigeration loop comprises:
a first heat exchanger configured to cool the nitrogen refrigerant stream;
an expander configured to reduce a temperature and a pressure of the nitrogen refrigerant stream;
a second heat exchanger configured to produce the LNG via indirect heat exchange between the nitrogen refrigerant stream and the natural gas stream; and
a compressor configured to compress the nitrogen refrigerant stream and pass the nitrogen refrigerant stream back to the first heat exchanger.

13. The system of claim 12 , wherein a first portion of the nitrogen refrigerant stream from the dehydration system is used as the nitrogen refrigerant stream for the nitrogen refrigeration loop, and wherein a second portion of the nitrogen refrigerant stream from the dehydration system is used to cool the first portion of the nitrogen refrigerant stream in the first heat exchanger.

14. The system of claim 13 , wherein the first portion of the nitrogen refrigerant stream is flowed from the dehydration system to a water and carbon dioxide removal system prior to being flowed to the nitrogen refrigeration loop.

15. The system of claim 13 , wherein the second portion of the nitrogen refrigerant stream is flowed from the dehydration system to a third heat exchanger and a second expander prior to being flowed to the first heat exchanger.

16. The system of claim 1 , wherein the power plant is configured to operate at a substantially stoichiometrically balanced condition, and wherein at least a portion of the exhaust gas is recirculated to the power plant.

17. A method for generating power and producing liquefied natural gas (LNG), comprising:
producing power via a power plant, wherein an exhaust gas from the power plant provides a gas mixture comprising nitrogen and carbon dioxide;
generating a nitrogen refrigerant stream from the gas mixture; and
producing LNG from a natural gas stream using the nitrogen refrigerant stream.

18. The method of claim 17 , comprising generating the nitrogen refrigerant stream by dehydrating the gas mixture.

19. The method of claim 17 , comprising generating the nitrogen refrigerant stream by removing the carbon dioxide from the gas mixture.

20. The method of claim 17 , comprising generating the nitrogen refrigerant stream by removing argon from the gas mixture.

21. The method of claim 17 , comprising generating the nitrogen refrigerant stream by cooling the gas mixture.

22. The method of claim 17 , wherein producing the power via the power plant comprises:
providing mechanical energy via an expander turbine using energy extracted from the gas mixture after combustion of the gas mixture in a combustor; and
generating electricity via a generator using the mechanical energy provided by the expander turbine.

23. The method of claim 17 , wherein producing the power via the power plant comprises:
providing mechanical energy via an expander turbine using energy extracted from the gas mixture after combustion of the gas mixture in a combustor;
generating steam via a heat recovery steam generator (HRSG) by heating a boiler with an exhaust stream from the expander turbine;
providing mechanical energy via a steam turbine using energy extracted from the steam generated by the HRSG; and
generating electricity via a generator using the mechanical energy provided by the expander turbine and the steam turbine.

24. The method of claim 17 , comprising producing the LNG from the natural gas stream by cooling the natural gas stream via heat exchange with the nitrogen refrigerant stream.

25. A system for producing liquefied natural gas (LNG) using nitrogen recovered from a combined cycle power plant, comprising:
an expander turbine configured to provide mechanical energy by extracting energy from a gas mixture exiting a combustor, wherein the gas mixture comprises nitrogen and carbon dioxide;
a heat recovery steam generator (HRSG) configured to generate steam by heating a boiler with the gas mixture from the expander turbine;
a steam turbine configured to provide mechanical energy by extracting energy from the steam generated by the HRSG;
a generator configured to generate electricity from the mechanical energy provided by the expander turbine and the steam turbine;
a de

Assignees

• Huntington Richard A
• Uptigrove Stanley O
• Oelfke Russell H
• Sites O Angus
• Exxonmobil Upstream Res Co

Inventors

• Huntington Richard A
• Uptigrove Stanley O
• Oelfke Russell H
• Sites O Angus

Classifications

• F01K23/10

  with exhaust fluid of one cycle heating the fluid in another cycle (F01K17/025 takes precedence) · CPC title

• F25J2270/904

  by liquid or gaseous cryogen in an open loop · CPC title

• F25J1/0221

  using the cold stored in an external cryogenic component in an open refrigeration loop · CPC title

• F01K5/02

  used in regenerative installation · CPC title

• F25J2240/44

  the fluid being nitrogen · CPC title