Systems and methods for LNG refrigeration and liquefaction

Patent metadata

Field	Value
Publication number	US-12313337-B2
Application number	US-201916297000-A
Country	US
Kind code	B2
Filing date	Mar 8, 2019
Priority date	Nov 6, 2015
Publication date	May 27, 2025
Grant date	May 27, 2025

Abstract

A LNG liquefaction plant system includes concurrent power production, wherein the refrigeration content of the refrigerant or SMR is used to liquefy and sub-cool a natural gas stream in a cold box or cryogenic exchanger. For concurrent power production, the system uses waste heat from refrigerant compression to vaporize and superheat a waste heat working fluid that in turn drives a compressor for refrigerant compression. The refrigerant may be an external SMR or an internal LNG refrigerant working fluid expanded and compressed by a twin compander arrangement.

First claim

What is claimed is:

1. A method for LNG liquefaction, the method comprising:
providing a natural gas feed stream;
providing, in a heat exchanger, heat exchange between the natural gas feed stream and a compressed and cooled refrigerant stream, wherein the heat exchange heats the compressed and cooled refrigerant stream;
after the heat exchange in the heat exchanger, splitting the compressed and cooled refrigerant stream into a first refrigerant portion and a second refrigerant portion;
expanding, in a first expander, the first refrigerant portion to produce an expanded first refrigerant stream portion;
using the expanded first refrigerant stream portion in the heat exchanger to cool the natural gas feed stream, where the expanded first refrigerant stream portion is heated in the heat exchanger to produce a first warm LNG vapor stream;
compressing the first warm LNG vapor stream with a first refrigerant compressor;
using the second refrigerant portion in the heat exchanger to cool the natural gas feed stream, wherein the second refrigerant portion is heated in the heat exchanger to produce a warmed refrigerant stream;
expanding, in a second expander, the warmed refrigerant stream to produce an expanded second refrigerant stream portion; and
using the expanded second refrigerant stream portion in the heat exchanger, wherein the expanded second refrigerant stream portion is heated in the heat exchanger to produce a second warm LNG vapor stream.

2. The method of claim 1 , where a volumetric flow ratio of the first refrigerant portion to the second refrigerant portion is 3:1.

3. The method of claim 1 , further comprising:
compressing the second warm LNG vapor stream in a first compressor to produce a compressed second LNG vapor stream.

4. The method of claim 3 , wherein the first compressor is mechanically coupled to the second expander.

5. The method of claim 3 , further comprising:
compressing the compressed second LNG vapor stream in a second compressor to form a second LNG vapor stream.

6. The method of claim 5 , wherein the second compressor is mechanically coupled to the first expander.

7. The method of claim 5 , further comprising:
cooling the compressed second LNG vapor stream prior to compressing the compressed second LNG vapor stream in the second compressor.

8. The method of claim 5 , further comprising:
compressing the second LNG vapor stream with a second refrigerant compressor.

9. The method of claim 8 , where the second refrigerant compressor forms a first stage in a refrigerant compressor system.

10. The method of claim 9 , wherein the first refrigerant compressor forms a second stage or third stage of the refrigerant compressor system.

11. The method of claim 1 , further comprising:
directing a gas stream from the produced LNG; and
using the gas stream in the heat exchanger for heat exchange with the natural gas feed stream.

12. The method of claim 1 , further comprising:
liquefying the natural gas feed stream in the heat exchanger to produce LNG.

13. The method of claim 12 , further comprising:
storing the LNG in a storage tank downstream of the heat exchanger,
directing a gas stream from the storage tank to the heat exchanger;
passing the gas stream from the heat exchanger to a third compressor;
compressing the gas stream in the third compressor into a fuel gas stream, wherein the fuel gas stream is used in a compressor driver to drive the first refrigerant compressor.

14. The method of claim 1 , wherein the heat exchanger is a cold box.

15. The method of claim 1 , further comprising:
treating the natural gas feed stream to remove one or more components in a natural gas treatment system before the providing the heat exchange between the natural gas feed stream and the compressed and cooled refrigerant stream.

Assignees

• Fluor Tech Corp

Inventors

• Mak John
• Thomas Jacob

Classifications

• F25J2240/70

  Steam turbine, e.g. used in a Rankine cycle · CPC title

• F25J2270/18

  External refrigeration with incorporated cascade loop · CPC title

• F25J1/005

  by expansion of a gaseous refrigerant stream with extraction of work · CPC title

• F25J2240/90

  Hot gas waste turbine of an indirect heated gas for power generation · CPC title

• F25J2270/60

  Closed external refrigeration cycle with single component refrigerant [SCR], e.g. C1-, C2- or C3-hydrocarbons · CPC title