Method and apparatus for gas liquefaction with plural work expansion of feed as refrigerant and air separation cycle embodying the same

• US 5,271,231 A
• Filed: 08/10/1992
• Issued: 12/21/1993
• Est. Priority Date: 08/10/1992
• Status: Expired due to Fees

• Current Assignee: L'Air Liquide SA, Liquid Air Engineering Corporation
• Original Assignee: L'Air Liquide Societe Anonyme Pour L'Etude et L'Exploitation Des Procedes Georges Claude (L'Air Liquide SA), Liquid Air Engineering Corporation
• Inventors: Tranier, Jean P., Ha, Bao
• Primary Examiner(s): Capossela, Ronald C.
• Application Number:
  US07/926,406
• Time in Patent Office: 498 Days
• Field of Search: 62/9, 62/39
• US Class Current: 62/615
• CPC Class Codes: F25J 1/0015 Nitrogen
• CPC Class Codes: F25J 1/0035 by gas expansion with extraction of work
• CPC Class Codes: F25J 1/0037 of a return stream
• CPC Class Codes: F25J 1/004 by flash gas recovery F25J1/0267 takes precedence
• 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 1/0208 in combination with an internal quasi-closed refrigeration loop, e.g. with deep flash recycle loop F25J1/021 takes precedence
• CPC Class Codes: F25J 1/0234 Integration with a cryogenic air separation unit cryogenic separation of air F25J3/04
• CPC Class Codes: F25J 2210/06 Splitting of the feed stream, e.g. for treating or cooling in different ways
• CPC Class Codes: F25J 2270/06 with multiple gas expansion loops
• CPC Class Codes: F25J 2270/90 External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration
• CPC Class Codes: F25J 2290/10 Mathematical formulae, modeling, plot or curves; Design methods
• CPC Class Codes: F25J 3/04224 Cores associated with a liquefaction or refrigeration cycle
• CPC Class Codes: F25J 3/04357 and comprising a gas work expansion loop
• CPC Class Codes: F25J 3/04393 using multiple or multistage gas work expansion
• CPC Class Codes: F25J 3/04412 in a classical double column flowsheet, i.e. with thermal coupling by a main reboiler-condenser in the bottom of low pressure respectively top of high pressure column

Abstract

A method of liquefying a low-boiling gas, in which gas is compressed to a high pressure, is cooled in heat exchange structure and is isenthalpically expanded to condense a portion of the same to liquid. The liquid being separated from residual gas and the residual gas is used to cool the heat exchange structure and is then recycled. A portion of the gas is compressed to an intermediate pressure between the high and low pressures, is isentropically expanded at a first temperature and is used to cool a relatively warm portion of heat exchange structure and is then recycled. A portion of the high pressure gas is isentropically expanded at a second temperature and used to cool a relatively cool portion of the heat exchange structure and then again isentropically expanded at a third temperature to that low pressure and returned through the heat exchange structure to cool the same and is then recycled. That first temperature is higher than the second temperature and that second temperature is higher than the third temperature. The gas is preferably nitrogen. The cycle can be part of an air separation unit, whose low pressure nitrogen product is make-up for the liquefaction cycle and whose high pressure nitrogen product is merged with the low pressure cycle gas.

Claims

1. In a method of liquefying a low-boiling gas, in which said gas is compressed to a high pressure, is cooled in heat exchange means and is expanded to a low pressure to liquefy at least a portion of the same;

the improvement comprising compressing a portion of said gas to an intermediate pressure between said high and low pressures, isentropically expanding said intermediate pressure gas at a first temperature and using the isentropically expanded gas to cool a relatively warm portion of said heat exchange means and then recycling said isentropically expanded gas, isentropically expanding a portion of said high pressure gas at a second temperature and using the same to cool a relatively cool portion of said heat exchange means and then again isentropically expanding at least some of the latter portion of gas at a third temperature to said low pressure and returning the same through the heat exchange means to cool the heat exchange means and then recycling the latter gas, said first temperature being higher than said second temperature and said second temperature being higher than said third temperature.

2. A method as claimed in claim 1, and cooling said intermediate pressure gas in the warm end of said heat exchange means prior to isentropic expansion thereof.

3. A method as claimed in claim 2, and cooling the high pressure gas to a lower temperature than the intermediate pressure gas, in said heat exchange means, prior to isentropic expansion of said portion of said high pressure gas.

4. A method as claimed in claim 1, and cooling said high pressure gas in a relatively warm portion of said heat exchange means prior to isentropic expansion of said portion thereof.

5. A method as claimed in claim 1, and separating liquid from the last-mentioned isentropically expanded gas.

6. A method as claimed in claim 1, in which said low-boiling gas has a boiling point no higher than that of oxygen.

7. A method as claimed in claim 6, in which said low-boiling gas is nitrogen.

8. A method as claimed in claim 6, in which said low-boiling gas is air.

9. A method as claimed in claim 1, wherein said intermediate pressure stream undergoes said isentropic expansion to said low pressure.

10. A method as claimed in claim 1, wherein said intermediate pressure gas undergoes said isentropic expansion to a pressure between said low pressure and said intermediate pressure.

11. A method as claimed in claim 1, wherein a portion of said gas between the last two isentropic expansions is diverted prior to the last isentropic expansion and is returned through said heat exchange means to a warm end thereof and recycled.

12. A method as claimed in claim 1, wherein a portion of said gas between the last two isentropic expansions is diverted prior to the last isentropic expansion and is passed through a portion of said heat exchange means to cool the same but is withdrawn from said heat exchange means prior to reaching a warm end thereof and is recycled with said intermediate pressure gas.

13. A method as claimed in claim 1, further comprising subjecting a portion of said intermediate pressure gas to external refrigeration at a temperature level above -45°

C. prior to said isentropic expansion thereof.

14. A method as claimed in claim 13, wherein the portion of said intermediate gas that is subjected to external refrigeration bypasses said heat exchange means prior to said isentropic expansion thereof and the remainder of said intermediate pressure gas passes through and is cooled in a warm end of said refrigeration means prior to said isentropic expansion thereof.

15. A method as claimed in claim 1, wherein a portion of said intermediate pressure gas bypasses said isentropic expansion thereof and instead continues through said heat exchange means to a cold end thereof and is expanded.

16. A method as claimed in claim 1, wherein a portion of said gas between the last two isentropic expansions is diverted prior to the last isentropic expansion, cooled in a cold end of said heat exchange means and expanded.

17. In an air separation method comprising compressing and cooling air, introducing the cooled air into a high pressure stage of a two-stage air distillation column comprising also a low pressure stage, withdrawing oxygen-rich liquid from the lower end of the high pressure stage and expanding the same and introducing the same into said low pressure stage for separation in said low pressure stage, withdrawing liquid nitrogen from the high pressure stage and expanding and introducing the same into the low pressure stage as reflux, and withdrawing nitrogen from the top of the low pressure stage;

the improvement comprising using said gaseous nitrogen as feed to the liquefaction cycle of claim 1.

18. An air separation method as claimed in claim 17, further comprising withdrawing gaseous nitrogen from the top of the high pressure stage, using the same to cool said air, and then merging the same with gas in said liquefaction cycle at said low pressure of said cycle.

19. An air separation method as claimed in claim 17, wherein liquid nitrogen produced in said liquefaction cycle is expanded and supplied to said low pressure stage as reflux.

20. An air separation method as claimed in claim 17, wherein gaseous nitrogen from said high pressure stage is used first to cool incoming air and then to cool a warmer portion of said heat exchange means.

21. A method as claimed in claim 17, wherein said high pressure stage is at said low pressure of said liquefaction cycle.

22. In apparatus for liquefying a low-boiling gas, in which said gas is compressed to a high pressure, is cooled in heat exchange means and is expanded to a low pressure to condense at least a portion of the same to liquid, the improvement comprising means for compressing a portion of said gas to an intermediate pressure between said high and low pressures, means for isentropically expanding said intermediate pressure gas at a first temperature and for using the isentropically expanded gas to cool a relatively warm portion of said heat exchange means and for then recycling said isentropically expanded gas, means for isentropically expanding a portion of said high pressure gas at a second temperature and for using the same to cool a relatively cool portion of said heat exchange means and for then again isentropically expanding at least some of the latter portion of gas at a third temperature to said low pressure and for returning the same through the heat exchange means to cool the heat exchange means and for then recycling the latter gas, said first temperature being higher than said second temperature and said second temperature being higher than said third temperature.

23. Apparatus as claimed in claim 22, and means for cooling said intermediate pressure gas in the warm end of said heat exchange means prior to isentropic expansion thereof.

24. Apparatus as claimed in claim 23, and means for cooling the high pressure gas to a lower temperature than the intermediate pressure gas, in said heat exchange means, prior to isentropic expansion of said portion of said high pressure gas.

25. Apparatus as claimed in claim 22, and means for cooling said high pressure gas in a relatively warm portion of said heat exchange means prior to isentropic expansion of said portion thereof.

26. Apparatus as claimed in claim 22, and means for separating liquid from the last-mentioned isentropically expanded gas.

27. Apparatus as claimed in claim 22, wherein said intermediate pressure stream undergoes said isentropic expansion to said low pressure.

28. Apparatus as claimed in claim 22, wherein said intermediate pressure gas undergoes said isentropic expansion to a pressure between said low pressure and said intermediate pressure.

29. Apparatus as claimed in claim 22, further comprising means for diverting a portion of said gas between the last two isentropic expansions prior to the last isentropic expansion and for returning the same through said heat exchange means to a warm end thereof for recycle.

30. Apparatus as claimed in claim 22, further comprising means for diverting a portion of said gas between the last two isentropic expansions prior to the last isentropic expansion and for passing the same through a portion of said heat exchange means to cool the same but for withdrawing the same from said heat exchange means prior to reaching a warm end thereof and for recycling the same with said intermediate pressure gas.

31. Apparatus as claimed in claim 22, further comprising means for subjecting a portion of said intermediate pressure gas to external refrigeration at a temperature level above -45°

C. prior to said isentropic expansion thereof.

32. Apparatus as claimed in claim 31, wherein the portion of said intermediate gas that is subjected to external refrigeration bypasses said heat exchange means prior to said isentropic expansion thereof and the remainder of said intermediate pressure gas passes through and is cooled in a warm end of said refrigeration means prior to said isentropic expansion thereof.

33. Apparatus as claimed in claim 22, further comprising means for bypassing a portion of said intermediate pressure gas past said isentropic expansion thereof and for instead conveying the same through said heat exchange means to a cold end thereof and for expanding the same.

34. Apparatus as claimed in claim 22, further comprising means for diverting a portion of said gas between the last two isentropic expansions prior to the last isentropic expansion, and for cooling the same in a cold end of said heat exchange means and for expanding the same.

35. An air separation apparatus comprising means compressing and cooling air to partially liquefy the same, and for introducing the partially liquefied air into a high pressure stage of a two-stage air distillation column comprising also a low pressure stage, and for withdrawing oxygen-rich liquid from the lower end of the high pressure stage and expanding the same and for introducing the same into said low pressure stage for separation in said low pressure stage, and for withdrawing liquid nitrogen from the high pressure stage and for expanding and introducing the same into the low pressure stage as reflux, and for withdrawing nitrogen from the top of the low pressure stage;

the improvement comprising means for using said gaseous nitrogen as feed to the liquefaction apparatus of claim 22.

36. An air separation apparatus as claimed in claim 35, further comprising means for withdrawing gaseous nitrogen from the top of the high pressure stage, means for using the same to cool said air, and means for then merging the same with gas in said liquefaction apparatus at said low pressure of said liquefaction apparatus.

37. An air separation apparatus as claimed in claim 35, further comprising means whereby liquid nitrogen from said phase separation is expanded and supplied to said low pressure stage as reflux.

38. An air separation apparatus as claimed in claim 35, further comprising means whereby gaseous nitrogen from said high pressure stage is used first to cool incoming air and then to cool a warmer portion of said heat exchange means.

39. An air separation apparatus as claimed in claim 35, wherein said high pressure stage is at said low pressure of said liquefaction apparatus.