Method for argon production via cold pressure swing adsorption
Methods and systems for purifying argon from a crude argon stream are disclosed, employing pressure swing adsorption at cold temperatures from −186° C. to −20° C.; more preferably from −150° C. to −50° C.; and most preferably from −130° C. to −80° C. with oxygen-selective zeolite adsorbent. In some embodiments, the oxygen-selective zeolite adsorbent is a 4A zeolite, a chabazite, or a combination thereof.
1. A method for producing a purified argon product, the method comprising:
providing a pressurized crude argon vapor stream at a temperature from −186° C. to −20° C.;
introducing the pressurized crude argon vapor stream into a pressure swing adsorption apparatus containing an oxygen-selective zeolite adsorbent and operating the pressure swing adsorption apparatus at a temperature from −186° C. to −20° C.;
withdrawing an argon enriched product from the pressure swing adsorption apparatus; and
regenerating the oxygen-selective zeolite at a pressure greater than prevailing ambient pressure; wherein the operating temperature of the pressure swing adsorption apparatus during operation is not increased except as a function of pressure change or adsorption/desorption.
2. The method of claim 1 , wherein the pressurized crude argon vapor stream comes from an air distillation process produced from the top or near top of a crude argon column, having a composition comprising oxygen, nitrogen, and 50 mole % to 99.5 mole % argon.
3. The method of claim 1 , wherein the pressurized crude argon vapor stream comprises oxygen, about 70 mole % to about 97 mole % argon, and about 0.5 mole % nitrogen.
4. The method of claim 1 , wherein the pressurized crude argon vapor stream is introduced into the pressure swing adsorption apparatus at a temperature from −150° C. to −50° C., and operating the pressure swing adsorption apparatus at a temperature from −150° C. to −50° C.
5. The method of claim 1 , wherein the pressurized crude argon vapor stream is introduced into the pressure swing adsorption apparatus at a temperature from −130° C. to −80° C., and operating the pressure swing adsorption apparatus at a temperature from −130° C. to −80° C.
6. The method of claim 1 , wherein the pressurized crude argon vapor stream is introduced into the pressure swing adsorption apparatus at a feed pressure from 2 bara to 20 bara.
7. The method of claim 1 , wherein the pressurized crude argon vapor stream is introduced into the pressure swing adsorption apparatus at a feed pressure from 2 bara to 8 bara.
8. The method of claim 1 , wherein the oxygen-selective zeolite adsorbent is selected from the 4A type zeolites and sodium exchanged chabazite zeolites.
9. The method of claim 1 , wherein the oxygen-selective zeolite adsorbent is a sodium exchanged chabazite zeolite having a Si/Al ratio from 1.3 to 1.8.
10. The method of claim 9 , wherein the sodium exchanged chabazite zeolite has a Si/Al ratio of about 1.6.
11. The method of claim 1 , wherein the pressure swing adsorption apparatus also comprises one or more equilibrium based zeolites for removing nitrogen.
12. The method of claim 11 , wherein the equilibrium based zeolites for removing nitrogen are selected from sodium X-type zeolite, calcium X-type zeolite, calcium exchanged A zeolite (CaA or 5A), or combinations thereof.
13. The method of claim 1 , wherein prior to introducing the pressurized crude argon vapor stream into the pressure swing adsorption apparatus, at least a portion of the pressurized crude argon vapor stream is increased in pressure to form a compressed argon-containing stream to be fed to the pressure swing adsorption apparatus.
14. The method of claim 1 , wherein the pressurized crude argon vapor stream is created by withdrawing crude argon from an air distillation process as a low pressure vapor, warming the low pressure crude argon vapor and compressing the warmed low pressure crude argon vapor from 2 bara to 8 bara to form the pressurized crude argon vapor.
15. The method of claim 14 , further comprising cooling the pressurized crude argon vapor to from −186° C. to −20° C.
16. The method of claim 1 , wherein the pressurized crude argon vapor stream is created by withdrawing crude argon from an air distillation process as a low pressure vapor and directly compressing the low pressure crude argon vapor to from 2 bara to 8 bara to form the pressurized crude argon vapor.
17. The method of claim 16 , further comprising, adjusting the temperature of the pressurized crude argon vapor to from −186° C. to −20° C.
18. The method of claim 1 , wherein the pressurized crude argon vapor stream is created by withdrawing crude argon from an air distillation process as a low pressure liquid, increasing the pressure of the low pressure crude argon liquid to from 2 bara to 8 bara, and vaporizing the pressurized crude argon liquid to form the pressurized crude argon vapor stream.
19. The method of claim 18 , further comprising adjusting the temperature of the pressurized crude argon vapor stream to from −186° C. to −20° C.
20. The method of claim 1 , wherein regenerating the oxygen-selective zeolite adsorbent is conducted at a pressure from 0.1 bar to 0.5 bar above prevailing ambient pressure.
21. The method of claim 1 , wherein regenerating the oxygen-selective zeolite adsorbent comprises withdrawing an oxygen-enriched gas from the pressure swing adsorption apparatus and recycling it back into a cryogenic distillation column.
22. The method of claim 1 , further comprising feeding the argon enriched product into a distillation column to remove nitrogen.
23. A method for producing a purified argon product, the method comprising:
providing a pressurized crude argon stream from a first cryogenic distillation column;
vaporizing the pressurized crude argon stream;
introducing the vaporized crude argon stream at a temperature from −186° C. to −20° C. and a feed pressure from 2 bara to 8 bara into a pressure swing adsorption (PSA) apparatus containing an oxygen-selective zeolite adsorbent;
operating the PSA apparatus at a temperature from −186° C. to −20° C.;
withdrawing an argon enriched product from the PSA apparatus; and
regenerating the oxygen-selective zeolite at a pressure greater than prevailing ambient pressure; wherein the operating temperature of the PSA apparatus during operation is not increased except as a function of pressure change or adsorption/desorption.
24. The method of claim 23 , wherein the vaporized crude argon stream is introduced to the PSA apparatus at a temperature from −150° C. to −50° C., and operating the PSA apparatus at a temperature from −150° C. to −50° C.
25. The method of claim 23 , wherein the vaporized crude argon stream is introduced to the PSA apparatus at a temperature from −130° C. to −80° C., and operating the PSA apparatus at a temperature from −130° C. to −80° C.
26. The method of claim 23 , wherein the oxygen-selective zeolite adsorbent is selected from 4A zeolites, sodium exchanged chabazites, or combinations thereof.