Argon recovery from argon-oxygen-decarburization process waste gases

• US 5,220,797 A
• Filed: 02/19/1992
• Issued: 06/22/1993
• Est. Priority Date: 09/28/1990
• Status: Expired due to Term

• Current Assignee: BOC Group Pty Limited (Linde Plc)
• Original Assignee: BOC Group Pty Limited (Linde Plc)
• Inventors: MacLean, Donald L., Krishnamurthy, Ramachandran
• Primary Examiner(s): Bennet, Henry A.
• Assistant Examiner(s): Kilner, Christopher B.
• Application Number:
  US07/837,744
• Time in Patent Office: 489 Days
• Field of Search: 62/17, 62/18, 62/22, 62/24, 55/25, 55/66, 55/68
• US Class Current: 62/620
• CPC Class Codes: B01D 2253/102 Carbon
• CPC Class Codes: B01D 2253/106 Silica or silicates
• CPC Class Codes: B01D 2253/108 Zeolites
• CPC Class Codes: B01D 2253/116 Molecular sieves other than zeolites
• CPC Class Codes: B01D 2256/12 Oxygen
• CPC Class Codes: B01D 2256/18 Noble gases
• CPC Class Codes: B01D 2257/102 Nitrogen
• CPC Class Codes: B01D 2257/104 Oxygen
• CPC Class Codes: B01D 2257/502 Carbon monoxide
• CPC Class Codes: B01D 2257/504 Carbon dioxide
• CPC Class Codes: B01D 2259/40001 Methods relating to additional, e.g. intermediate, treatment of process gas
• CPC Class Codes: B01D 2259/40015 with two sub-steps
• CPC Class Codes: B01D 2259/4003 with two sub-steps
• CPC Class Codes: B01D 2259/40066 Six
• CPC Class Codes: B01D 2259/40069 Eight
• CPC Class Codes: B01D 2259/404 using four beds
• CPC Class Codes: B01D 2259/416 involving cryogenic temperature treatment
• CPC Class Codes: B01D 53/0476 Vacuum pressure swing adsorption
• CPC Class Codes: F25J 2200/02 in a single pressure main column system
• CPC Class Codes: F25J 2205/40 using hybrid system, i.e. combining cryogenic and non-cryogenic separation techniques
• CPC Class Codes: F25J 2205/60 : using adsorption on solid adsorbents, e.g. by temperature-swing adsorption [TSA] at the hot or cold end
• CPC Class Codes: F25J 2205/82 : using a reactor with combustion or catalytic reaction
• CPC Class Codes: F25J 2215/58 : Argon
• CPC Class Codes: F25J 2270/12 : External refrigeration with liquid vaporising loop
• CPC Class Codes: F25J 2270/14 : External refrigeration with work-producing gas expansion loop
• CPC Class Codes: F25J 2270/42 : Quasi-closed internal or closed external nitrogen refrigeration cycle
• CPC Class Codes: F25J 3/0285 : of argon
• CPC Class Codes: F25J 3/08 : Separating gaseous impurities from gases or gaseous mixtures or from liquefied gases or liquefied gaseous mixturescold traps B01D8/00
• CPC Class Codes: Y02C 20/40 : of CO2
• CPC Class Codes: Y10S 62/924 : Argon

Abstract

The present invention is directed to a method for recovering argon from a feed mixture comprising argon, carbon monoxide, carbon dioxide, nitrogen, and hydrogen which comprises the steps of (a) purifying the feed mixture to remove contaminants, (b) compressing the purified feed mixture to a separation pressure, and (c) passing the compressed purified feed mixture through a pressure swing adsorption system to separate carbon monoxide, carbon dioxide, and all or most of the nitrogen from the mixture as adsorbed products and to produce an argon-rich fraction as a non-adsorbed product. The argon-rich fraction from step (c) may be further purified by passing the fraction to a cryogenic fractional distillation system to separate hydrogen and any remaining nitrogen from the fraction as a distillate product and to produce a pure argon product. In a second and third embodiment, the invention is directed to a method for recovering argon from a feed mixture comprising argon, carbon monoxide, carbon dioxide, nitrogen, and oxygen, wherein oxygen is removed from the argon-rich fraction exiting the pressure swing adsorption system in step (c) by passing the fraction to a second pressure swing adsorption system before or after further purification of the fraction in a cryogenic fractional distillation system.

Claims

1. A method for recovering argon from a feed mixture comprising argon, carbon monoxide, carbon dioxide, nitrogen, and hydrogen which comprises the steps of:

(a) purifying the feed mixture to remove contaminants;

(b) compressing the purified feed mixture to a separation pressure;

(c) passing the compressed purified feed mixture through a pressure swing adsorption system containing a bed of adsorbent selected from the group consisting of molecular sieves and activated carbon, thereby adsorbing carbon monoxide, carbon dioxide, and all or most of the nitrogen from the mixture and producing an argon-rich fraction as a non-adsorbed product;

(d) removing a secondary depressurization product from the system and recycling it to the feed mixture;

(e) desorbing carbon monoxide, carbon dioxide and nitrogen from the adsorbent under vacuum; and

(f) passing the argon-rich fraction from step (c) to a cryogenic distillation system to separate hydrogen and any remaining nitrogen from the fraction as a distillate product and to produce a high purity argon product.

2. The method according to claim 1, wherein the argon-rich fraction withdrawn from the pressure swing adsorption system from step (c) is cooled by a heat exchanger with process waste gas leaving the cryogenic fractional distillation system prior to passing the argon-rich fraction to the cryogenic fractional distillation system.

3. The method according to claim 1, further comprising the step of recirculating a refrigerant in the cryogenic fractional distillation system in a refrigerating heat pump cycle by using a column reboiler in the cryogenic fractional distillation system as a heat sink for the refrigerating cycle to provide refrigeration at a column condenser.

4. The method according to claim 1, wherein the pure argon product contains greater than about 99% argon.

5. A method for recovering argon from a feed mixture comprising argon, carbon monoxide, carbon dioxide, nitrogen, and oxygen, which comprises the steps of:

(a) purifying the feed mixture to remove contaminants;

(b) compressing the purified feed mixture to a separation pressure;

(c) passing the compressed purified feed mixture through a first pressure swing adsorption system containing a bed of adsorbent selected from the group consisting of molecular sieves and activated carbon, thereby adsorbing carbon monoxide, carbon dioxide, and all or most of the nitrogen from the mixture and producing a first argon-rich fraction as a non-adsorbed product;

(d) removing a secondary depressurization product from the system and recycling it to the feed mixture;

(e) desorbing carbon monoxide, carbon dioxide and nitrogen from the adsorbent under vacuum;

(f) passing the first argon-rich fraction from step (c) to a second pressure swing adsorption system to separate oxygen as an adsorbed product and to produce a second argon-rich fraction as a non-adsorbed product; and

(g) passing the second argon-rich fraction from step (f) to a cryogenic fractional distillation system to separate any remaining nitrogen from the fraction as a distillate product and to produce a high purity argon product.

6. The method according to claim 5, wherein the feed mixture comprises argon in an amount greater than about 10%, carbon monoxide in an amount up to about 40%, carbon dioxide in an amount up to about 40%, nitrogen in an amount up to about 40%, and oxygen in an amount up to about 20%.

7. The method according to claim 5, wherein said adsorbent is an aluminosilicate zeolite selected from the group consisting of 5A, 10X, 13X, and mordenites.

8. The method according to claim 5, further comprising the step of passing vent gas from the first pressure swing adsorption system from step (c) to an equalization tank to minimize loss of void gas.

9. The method according to claim 5, wherein adsorbent material in the first pressure swing adsorption system from step (c) undergoes periodic regeneration with a purge gas.

10. The method according to claim 5, further comprising the step of backfilling the first pressure swing adsorption system from step (c) with product gas to repressurize the pressure swing adsorption system to increase the purity of the first argon-rich fraction.

11. The method according to claim 5, wherein the first argon-rich fraction withdrawn from the first pressure swing adsorption system from step (c) is cooled by a heat exchanger with process waste gas leaving the cryogenic fractional distillation system prior to passing the first argon-rich fraction to the cryogenic fractional distillation system.

12. The method according to claim 5, further comprising the step of recirculating a refrigerant in the cryogenic fractional distillation system in a refrigerating heat pump cycle by using a column reboiler in the cryogenic fractional distillation system as a heat sink for the refrigerating cycle to provide refrigeration at a column condenser.

13. The method according to claim 5, wherein the pure argon product contains greater than about 99% argon.

14. The method according to claim 5, wherein the purified feed mixture from step (a) is passed to a carbon dioxide separation means prior to compressing the mixture in step (b).

15. The method according to claim 14, wherein the carbon dioxide separation means is a carbon dioxide absorbent column.

16. The method according to claim 14, wherein the carbon dioxide separation means is a pressure swing adsorption system.

17. The method according to claim 5, wherein the second pressure swing adsorption separation in step (d) is carried out before the first pressure swing adsorption separation in step (c).

18. A method for recovering argon from a feed mixture comprising argon, carbon monoxide, carbon dioxide, nitrogen, and oxygen, which comprises the steps of:

(a) purifying the feed mixture to remove contaminants;

(b) compressing the purified feed mixture to a separation pressure;

(c) passing the compressed purified feed mixture through a first pressure swing adsorption system containing a bed of adsorbent selected from the group consisting of molecular sieves and activated carbon, thereby adsorbing carbon monoxide, carbon dioxide, and all or most of the nitrogen from the mixture and producing a first argon-rich fraction as a non-adsorbed product;

(d) removing a secondary depressurization product from the system and recycling it to the feed mixture;

(e) desorbing carbon monoxide, carbon dioxide and nitrogen from the adsorbent under vacuum;

(f) passing the first argon-rich fraction from step (c) to a cryogenic fractional distillation system to separate any remaining nitrogen from the fraction as a distillate product and to produce a second argon-rich fraction; and

(g) passing the second argon-rich fraction from step (f) to a second pressure swing adsorption system to separate oxygen as an adsorbed product and high purity argon as a non-adsorbed product.

19. The method according to claim 18, wherein the feed mixture comprises argon in an amount greater than about 10%, carbon monoxide in an amount up to about 40%, carbon dioxide in an amount up to about 40%, nitrogen in an amount up to about 40%, and oxygen in an amount up to about 20%.

20. The method according to claim 18, wherein said adsorbent is an aluminosilicate zeolite selected from the group consisting of 5A, 10X, 13X, and mordenites.

21. The method according to claim 18, further comprising the step of passing vent gas from the first pressure swing adsorption system from step (c) to an equalization tank to minimize loss of void gas.

22. The method according to claim 18, wherein adsorbent material in the first pressure swing adsorption system from step (c) undergoes periodic regeneration with a purge gas.

23. The method according to claim 18, further comprising the step of backfilling the first pressure swing adsorption system from step (c) with product gas to repressurize the pressure swing adsorption system to increase the purity of the first argon-rich fraction.

24. The method according to claim 18, wherein the first argon-rich fraction withdrawn from the first pressure swing adsorption system from step (c) is cooled by a heat exchanger with process waste gas leaving the cryogenic fractional distillation system prior to passing the first argon-rich fraction to the cryogenic fractional distillation system.

25. The method according to claim 18, further comprising the step of recirculating a refrigerant in the cryogenic fractional distillation system in a refrigerating heat pump cycle by using a column reboiler in the cryogenic fractional distillation system as a heat sink for the refrigerating cycle to provide refrigeration at a column condenser.

26. The method according to claim 18, wherein the pure argon product contains greater than about 99% argon.

27. The method according to claim 18, wherein the purified feed mixture from step (a) is passed to a carbon dioxide separation means prior to compressing the mixture in step (b).

28. The method according to claim 27, wherein the carbon dioxide separation means is a carbon dioxide adsorption column.

29. The method according to claim 27, wherein the carbon dioxide separation means is a pressure swing adsorption system.