Self-refrigerated LNG process

• US 6,564,578 B1
• Filed: 01/18/2002
• Issued: 05/20/2003
• Est. Priority Date: 01/18/2002
• Status: Active Grant

• Current Assignee: BP Corporation North America Incorporated (BP PLC)
• Original Assignee: BP Corporation North America Incorporated (BP PLC)
• Inventors: Fischer-Calderon, Ernesto
• Primary Examiner(s): DOERRLER, WILLIAM CHARLES
• Application Number:
  US10/050,922
• Time in Patent Office: 487 Days
• Field of Search: 626/11, 626/13, 626/12, 626/19
• US Class Current: 62/613
• CPC Class Codes: F25J 1/0022 Hydrocarbons, e.g. natural gas
• CPC Class Codes: F25J 1/004 by flash gas recovery F25J1/0267 takes precedence
• CPC Class Codes: F25J 1/0042 by liquid expansion with extraction of work
• CPC Class Codes: F25J 1/0045 by vaporising a liquid return stream
• CPC Class Codes: F25J 1/0202 in a quasi-closed internal refrigeration loop F25J1/0208, F25J1/0219, F25J1/0224 take precedence
• CPC Class Codes: F25J 1/0254 controlling particular process parameter, e.g. pressure, temperature

Abstract

The present invention is directed to a process for producing LNG by directing a feed stream comprising natural gas to a cooling stage that (a) cools the feed stream in at least one cooling step producing a cooled feed stream, (b) expands the cooled feed stream in at least one expansion step by reducing the pressure of the cooled feed stream producing a refrigerated vapor component and a liquid component, and (c) separates at least a portion of the refrigerated vapor component from the liquid component wherein at least a portion of the cooling for the process is derived from at least a portion of the refrigerated vapor component; and repeating steps (a) through (c) one or more times until at least substantial portion of the feed stream in the first cooling stage is processed into LNG wherein the feed stream in step (a) comprises at least a portion of the liquid component produced from a previous cooling stage.

Claims

1. A process for producing LNG, comprising:

(a) directing a feed stream comprising natural gas to a cooling stage, the cooling stage comprising the steps of;

(i) cooling the feed stream in at least one cooling step producing a cooled feed stream;

(ii) expanding the cooled feed stream in at least one expansion step by reducing the pressure of the cooled feed stream producing a refrigerated vapor component and a liquid component; and

(iii) separating at least a portion of the refrigerated vapor component from the liquid component; and

(b) repeating step (a) one or more times until at least a substantial portion of the feed stream in the first cooling stage is processed into LNG wherein the feed stream comprises at least a portion of the liquid component from step (iii) of a previous cooling stage;

wherein at least a portion of the cooling for step (i) in at least one cooling stage is derived from at least a portion of the refrigerated vapor component produced in at least one cooling stage.

2. The process of claim 1, wherein the feed stream in step (a) for each successive cooling stage further comprises at least a portion of the refrigerated vapor component from step (iii) of a previous cooling stage.

3. The process of claim 1, wherein step (a) is repeated at least two additional times.

4. The process of claim 1, wherein step (a) is repeated at least three additional times.

5. The process of claim 1, wherein at least one cooling stage further comprises the step of compressing the refrigerated vapor component to produce a compressed vapor component.

6. The process of claim 5, wherein at least one cooling stage further comprises the step of recycling the compressed vapor component into the feed stream from at least one cooling stage.

7. A process for producing LNG, comprising:

(a) directing a feed stream to a cooling stage, the cooling stage comprising the steps of;

(i) cooling the feed stream in at least one cooling step producing a cooled feed stream;

(ii) expanding the cooled feed stream in at least one expansion step by reducing the pressure of the cooled feed stream producing a refrigerated vapor component and a liquid component; and

(iii) separating at least a portion of the refrigerated component from the liquid component; and

(b) repeating step (a) one or more times wherein the feed stream comprises the liquid component from step (iii) of at least one cooling stage;

wherein at least a portion of the cooling for step (i) in at least one cooling stage is derived from at least a portion of the refrigerated vapor component produced in at least one cooling stage;

wherein the inlet pressure of the feed stream in step (b), as measured in psia, is at least ⅓

the inlet pressure of the feed stream, as measured in psia, of the immediately preceding cooling stage provided that the inlet pressure of said feed stream of the immediately preceding cooling stage is at least 75 psia.

8. The process of claim 7, wherein the inlet pressure of the feed stream in step (b) is at least ⅓

the inlet pressure of the feed stream of the immediately preceding cooling stage provided that the inlet pressure of said feed stream of the immediately preceding cooling stage is at least 150 psia.

9. The process of claim 7, wherein the inlet pressure of the feed stream in step (b) is at least ½

the inlet pressure of the feed stream of the immediately preceding cooling stage provided that the inlet pressure of said feed stream of the immediately preceding cooling stage is at least 150 psia.

10. The process of claim 7, wherein the inlet pressure of the feed stream in step (b) is at least ½

the inlet pressure of the feed stream of the immediately preceding cooling stage provided that the inlet pressure of said feed stream of the immediately preceding cooling stage is at least 75 psia.

11. The process of claim 7, wherein the pressure of the feed stream in the first cooling stage is at least 1000 psia and step (a) is repeated at least two additional times.

12. The process of claim 8, wherein the pressure of the feed stream in the first cooling stage is at least about 1000 psia and step (a) is repeated at least three additional times.

13. The process of claim 9, wherein the pressure of the feed stream in the first cooling stage is at least about 1000 psia and step (a) is repeated at least three additional times.

14. The process of claim 7, wherein at least one cooling stage further comprises the step of recycling the compressed vapor component into the feed stream from at least one previous cooling stage.

15. A process for producing LNG, comprising:

(a) sending a feed stream comprising natural gas to a cooling stage, the cooling stage comprising the steps of;

(i) cooling the feed stream in at least one cooling step producing a cooled feed stream;

(ii) expanding the cooled feed stream in at least one expansion step by reducing the pressure of the cooled feed stream producing a refrigerated vapor component and a liquid component; and

(iii) separating in at least one separation step at least a portion of the refrigerated component from the liquid component;

(b) repeating step (a) one or more times wherein the feed stream comprises at least a portion of the liquid component from step (iii) of a previous cooling stage;

wherein at least a portion of the cooling for step (i) in at least one cooling stage is derived from at least a portion of the refrigeration vapor component produced in at least one cooling stage, and

wherein at least one cooling stage employs multiple separation steps that are integrally operated with at least an equal number of expansion steps.

16. The process of claim 15, wherein step (a) is repeated at least two times.

17. The process of claim 15, wherein step (a) is repeated at least three times.

18. The process of claim 15, wherein at least one cooling stage further comprises the step of compressing the refrigerated vapor component to produce a compressed vapor component.

19. The process of claim 18, wherein at least one cooling stage further comprises the step of recycling the compressed vapor component into the feed stream from at least one cooling stage.

20. The process of claim 19, wherein the compressed vapor component is recycled into the feed stream of the first cooling stage.

21. A process for producing LNG, comprising:

(a) directing a feed stream having a pressure of at least 1,000 psia to a first cooling stage, the first cooling stage comprising the steps of;

(i) cooling the feed stream producing a cooled feed stream;

(ii) expanding the cooled feed stream by reducing the pressure of the cooled feed stream producing a refrigerated vapor component and a liquid component; and

(iii) separating at least a portion of the refrigerated vapor component from the liquid component; and

(b) directing a second feed stream comprising at least a portion of the liquid component produced in the first cooling stage and having a pressure, at least ⅓

the pressure of the first feed stream to a second cooling stage, the second cooling stage comprising the steps of;

(i) cooling the second feed stream producing a second cooled feed stream;

(ii) expanding the second cooled feed stream by reducing the pressure of the second cooled feed stream producing a second refrigerated vapor component and a second liquid component; and

(iii) separating at least a portion of the second refrigerated vapor component from the second liquid component;

wherein at least a portion of the cooling for step (i) in the first cooling stage or for step (i) in the second cooling stage is derived from at least a portion of the refrigerated vapor component or from at least a portion of the second refrigerated component.

22. The process of claim 21, further comprising directing a third feed stream comprising at least a portion of the second liquid component produced in the second cooling stage and having a pressure at least ⅓

the pressure of the second feed stream to a third cooling stage, the third cooling stage comprising the steps of (i) cooling the third feed stream producing a third cooled feed stream;

(ii) expanding the third cooled feed stream by reducing the pressure of the third cooled feed stream producing a third refrigerated vapor component and a third liquid component; and

(iii) separating at least a portion of the third refrigerated vapor component from the third liquid component;

wherein at least a portion of the cooling for step (i) in the first, second or third cooling stages is derived from at least a portion of the refrigerated vapor component, at least a portion of the second refrigerated component or at least a portion of the third refrigerated component.