Process for air fractionation by low-temperature rectification

• US 4,883,518 A
• Filed: 11/14/1988
• Issued: 11/28/1989
• Est. Priority Date: 11/13/1987
• Status: Expired due to Fees

• Current Assignee: Linde AG (Linde Plc)
• Original Assignee: Linde AG (Linde Plc)
• Inventors: Eggendorfer, Gunnar, Skolaude, Werner, Corduan, Horst
• Primary Examiner(s): Capossela, Ronald C.
• Application Number:
  US07/270,606
• Time in Patent Office: 379 Days
• Field of Search: 62/11, 62/32, 62/36, 62/38, 62/42, 62/43
• US Class Current: 62/646
• 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 3/042 having an intermediate feed connection
• CPC Class Codes: F25J 3/04224 Cores associated with a liquefaction or refrigeration cycle
• CPC Class Codes: F25J 3/04278 using external refrigeration units, e.g. closed mechanical or regenerative refrigeration units
• CPC Class Codes: F25J 3/04296 Claude expansion, i.e. expanded into the main or high pressure column
• CPC Class Codes: F25J 3/04345 and comprising a gas work expansion loop
• 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
• CPC Class Codes: Y10S 62/94 High pressure column

Abstract

In a system for air fractionation by low-temperature rectification, refrigeration is produced in a cooling stage by compression and expansion of the feed air or of nitrogen from rectification. By using the work gained during expansion for compressing only a partial stream of the gas passed through the cooling stage, the system according to this invention operates with increased efficiency and lower operating costs.

Claims

1. In a process for air fractionation by low-temperature rectification comprising a rectification step from which nitrogen and product oxygen streams are obtained and a cooling stage wherein a process gas of the air fractionation is employed as working gas to produce refrigeration by compression and expansion of at least a portion of said working gas, the improvement comprising:

compressing said working gas in said cooling stage and thereafter dividing said working gas into a first partial stream and a second partial stream, both of which are at least partially cooled and at least partially subjected to engine expansion, said first partial stream being expanded at a temperature higher than that at which the second partial stream is expanded;

compressing at least said second partial stream, prior to expansion, wherein work gained during expansion of at least a part of one of said partial streams is utilized in the compression of said second partial stream, said compression of said second partial stream being performed in two compression stages; and

introducing at least a portion of at least one of said partial streams to the rectification step.

2. A process according to claim 1, wherein work gained during expansion of both partial streams is utilized in said two compression stages for compression of said second partial stream.

3. A process according to claim 2, wherein work gained during expansion of said second partial stream is utilized in a first compression stage of said two compression stages for compression of said second partial stream.

4. A process according to claim 3, wherein work gained during expansion of said first partial stream is utilized in a second stage of said two compression stages for compression of said second partial stream.

5. A process according to claim 1, wherein work gained during expansion of said second partial stream is utilized in a first compression stage of said two compression stages for compression of said second partial stream.

6. A process according to claim 5, wherein work gained during expansion of said first partial stream is utilized in a second stage of said two compression stages for compression of said second partial stream.

7. A process according to claim 1, wherein work gained during expansion of said first partial stream is utilized in a second stage of said two compression stages for compression of said second partial stream.

8. A process according to claim 1, wherein said first partial stream is engine expanded without subsequent or prior compression.

9. A process according to claim 1, wherein a portion of at least one of said partial streams is recycled, after expansion, to said working gas to a point upstream of the compression of said working gas.

10. A process according to claim 9, wherein a portion of each of said partial streams is recycled, after expansion, to said working gas to a point upstream of the compression of said working gas.

11. A process according to claim 9, wherein the entirety of said first partial stream is recycled to said working gas to a point upstream of the compression of said working gas.

12. A process according to claim 1, wherein both partial streams are fed in their entirety to the rectification.

13. A process according to claim 1, further comprising, prior to the introduction of air to the air fractionation process, compressing the air to be fractionated and purifying the air to be fractionated by removal of steam and carbon dioxide.

14. A process according to claim 13, wherein after purification of said air to be fractionated, the air to be fractionated is cooled and then delivered directly to a high pressure stage of a two-stage rectification.

15. A process according to claim 14, wherein said working gas is a nitrogen-enriched gas removed from said rectification step.

16. A process according to claim 13, wherein said working gas is the air to be fractionated.

17. A process according to claim 16, wherein after prepurification of said air to be fractionated, the air is delivered directly to said cooling stage.

18. A process according to claim 1, wherein said working gas is the air to be fractionated.

19. A process according to claim 18, wherein said rectification step comprises a rectification column having a first high pressure stage and a second low pressure stage, said first and second stages of said rectification column being in heat exchange relation by a condenser-evaporator.

20. A process according to claim 19, wherein gaseous product nitrogen is removed from the head of said second stage or said rectification column, gaseous product oxygen is removed from a lower portion of said second stage of said rectification column, product liquid nitrogen is removed from an upper portion of said second stage of said rectification column, and product liquid oxygen is removed from the bottom of said second stage of said rectification column.

21. A process according to claim 18, wherein at least a portion of at least one of said partial streams is subjected to cooling by external coolant in said cooling stage.

22. A process according to claim 21, wherein a portion of said second partial stream is subjected to cooling by external coolant in said cooling stage prior to expansion of said second partial stream.

23. A process according to claim 21, wherein said at least a portion of at least one of said partial streams is cooled by external coolant to a temperature which is higher than or equal to the inlet temperature of the expansion device employed in the expansion of at least a portion of said first partial stream.

24. A process according to claim 1, wherein said working gas is a nitrogen-enriched gas removed from said rectification step.

25. A process according to claim 24, wherein at least a portion of said nitrogen-enriched gas employed as said work gas is heated by heat exchange with said partial streams prior to compression of said working gas.

26. A process according to claim 25, wherein a side stream of said nitrogen-enriched gas is heated by heat exchange with the air to be fractionated prior to compression of said working gas.

27. A process according to claim 26, wherein a portion of said second partial stream, which is not subjected to expansion in an expansion device from which work is gained, is delivered to a high pressure stage of a two-stage rectification.

28. A process according to claim 25, wherein said rectification step comprises a rectification column having a first high pressure stage and a second low pressure stage, said first and second stages of said rectification column being in heat exchange relation by a condenser-evaporator.

29. A process according to claim 28, wherein said nitrogen-enriched gas is removed from the head of said high pressure stage of said rectification column.

30. A process according to claim 24, wherein at least a portion of at least one of said partial streams is subjected to cooling by external coolant in said cooling stage.

31. A process according to claim 30, wherein said at least a portion of at least one of said partial streams is cooled by external coolant to a temperature which is higher than or equal to the inlet temperature of the expansion device employed in the expansion of at least a portion of said first partial stream.

32. A process according to claim 1, wherein said rectification step comprises a rectification column having a first high pressure stage and a second low pressure stage, said first and second stages of said rectification column being in heat exchange relation by a condenser-evaporator.

33. A process according to claim 32, wherein gaseous product nitrogen is removed from the head of said second stage or said rectification column, gaseous product oxygen is removed from a lower portion of said second stage of said rectification column, product liquid nitrogen is removed from an upper portion of said second stage of said rectification column, and product liquid oxygen is removed from the bottom of said second stage of said rectification column.

34. A process according to claim 1, wherein at least a portion of at least one of said partial streams is subjected to cooling by external coolant in said cooling stage.

35. An apparatus for air fractionation by low-temperature rectification comprising:

(a) compression means for compressing the air to be fractionated;

(b) means for dividing resultant compressed air into a first partial stream and a second partial stream;

(c) heat exchange means for cooling said first partial stream;

(d) expansion means for expanding the cooled first partial stream to remove mechanical energy therefrom;

(e) recycle means for recycling the expanded first partial stream to a point upstream of said compression means (a);

(f) two serially connected compression stages for compressing said second partial stream;

(g) heat exchange means for cooling resultant compressed second partial stream;

(h) expansion means for expanding at least a portion of said second partial stream to remove mechanical energy therefrom;

(i) a two-stage rectification column comprising a first high-pressure stage and a second low-pressure stage, said first stage and said second stage being in heat exchange relation by a condenser-evaporator;

(j) delivery means for delivering said second partial stream to said first stage of said rectification column; and

(k) product delivery means for removing gaseous and liquid product nitrogen and gaseous and liquid product oxygen from said second pressure stage of said rectification column;

wherein said two serially connected compression stages are in connection with expansion means (d) and (h) whereby mechanical energy obtained in said expansion means (d) and (h) is utilized to operate said two serially connected compression stages.

36. An apparatus for air fractionation by low-temperature rectification comprising:

(a) heat exchange means for cooling air to be fractionated;

(b) a two-stage rectification column comprising a first high-pressure stage and a second low-pressure stage, said first stage and said second stage being in heat exchange relation by a condenser-evaporator, said first stage having an inlet means for delivery of cooled air to be fractionated, said second stage having product delivery means for removal of gaseous and liquid product nitrogen and gaseous and liquid product oxygen therefrom;

(c) outlet means for removing nitrogen-enriched gas from an upper portion of said first stage of said rectification column;

(d) compression means in fluid communication with said outlet means (c) for compressing said nitrogen-enriched gas;

(e) means for dividing the compressed nitrogen-enriched gas into a first partial stream and a second partial stream;

(f) cooling means for cooling said first partial stream;

(g) expansion means for expanding said first partial stream to remove mechanical energy therefrom;

(h) recycle means for recycling the expanded first partial stream to a point upstream of said compression means (d);

(i) two serially connected compressed stages for compressing said second partial stream;

(j) cooling means for cooling the compressed second partial stream;

(k) expansion means for expanding at least a portion of said second partial stream to remove mechanical energy therefrom; and

(l) delivery means for delivering at least a portion of said second partial stream to said first high-pressure stage of said rectification column;

wherein said two serially connected compression stages are in connection with expansion means (g) and (k) whereby mechanical energy obtained in said expansion means (g) and (k) is utilized to operate said two serially connected compression stages.