Cryogenic adsorption process for xenon recovery

Patent metadata

Field	Value
Publication number	US-10295255-B2
Application number	US-201615244359-A
Country	US
Kind code	B2
Filing date	Aug 23, 2016
Priority date	Aug 23, 2016
Publication date	May 21, 2019
Grant date	May 21, 2019

Abstract

An adsorption process for xenon recovery from a cryogenic liquid or gas stream is described wherein a bed of adsorbent is contacted with the aforementioned xenon containing liquid or gas stream and adsorbs the xenon selectively from this fluid stream. The adsorption bed is operated to at least near full breakthrough with xenon to enable a deep rejection of other stream components, prior to regeneration using the temperature swing method. Operating the adsorption bed to near full breakthrough with xenon, prior to regeneration, enables production of a high purity product from the adsorption bed and further enables oxygen to be used safely as a purge gas, even in cases where hydrocarbons are co-present in the feed stream.

First claim

We claim:

1. An adsorption process for the recovery of xenon from a cryogenic feed stream containing xenon which comprises:
i. feeding the feed stream at cryogenic temperatures into the inlet of an adsorption vessel having an inlet and an outlet and containing an adsorbent bed therein, wherein said adsorbent bed contains at least one AgX adsorbent selective for xenon,
ii. maintaining said adsorbent bed on feed until the xenon concentration at the outlet of said bed is greater than or equal to 70% of the xenon concentration at the inlet to said adsorbent bed,
iii. ending the feed to the adsorption bed and purging same with a purge gas,
iv. increasing the temperature of said adsorbent bed to a temperature effective to desorb substantially all of said xenon from the adsorbent in said adsorbent bed,
v. recovering the xenon product desorbed from said adsorbent bed,
vi. cooling said adsorbent bed to cryogenic temperatures with a cryogenic fluid, and
repeating steps i.-vi. in a cyclic manner.

2. The process of claim 1 wherein said cryogenic feed stream is an oxygen feed stream which, in addition to xenon, comprises at least one other adsorbable component.

3. The process of claim 2 wherein said at least one other adsorbable component is a hydrocarbon or krypton.

4. The process of claim 3 wherein said hydrocarbon is methane, ethane, ethylene, propane or combinations thereof.

5. The process of claim 4 wherein said at least one other adsorbable component comprises krypton, methane, or both krypton and methane.

6. The process of claim 1 wherein said cryogenic feed stream is in a liquid or gaseous state.

7. The process of claim 1 wherein said feed stream comprises 1-200 ppm xenon, 500-2000 ppm Kr, 500-2000 ppm hydrocarbons, 0-100 ppm N 2 O, 0-100 ppm CO 2 , 0-1200 ppm of Ar and ppm amounts of N 2 and other atmospheric gases, balance O 2 .

8. The process of claim 1 wherein said purge gas comprises oxygen, nitrogen and/or argon.

9. The process of claim 8 wherein said purge gas is substantially free of xenon.

10. The process of claim 1 wherein said adsorbent bed of step i. is pre-cooled to a temperature of ≤120K.

11. The process of claim 5 wherein said adsorbent bed of step i. is pre-cooled to a temperature of ≤90K.

12. The process of claim 3 wherein said purge step is continued until the hydrocarbons level at the outlet of said adsorbent bed are ≤50 ppm.

13. The process of claim 3 wherein said purge step is continued until the hydrocarbons level at the outlet of said adsorbent bed are ≤10 ppm.

14. The process of claim 1 wherein in step iv., the temperature of the adsorbent bed is increased from cryogenic temperatures to at least 250 K in order to recover a xenon product at a concentration of ≥1% xenon.

15. The process of claim 12 wherein in step iv. wherein said xenon product contains<50 ppm hydrocarbons.

16. The process of claim 1 wherein in step vi., the adsorbent bed is cooled to a temperature of <120 K.

17. The process of claim 1 wherein said adsorbent bed is maintained on feed until the xenon concentration at the outlet of said bed is greater than or equal to 95% of the xenon concentration at the inlet to said adsorbent bed.

18. The process of claim 1 comprising at least two adsorbent beds wherein said adsorbent beds are out of phase with each other.

19. The process of claim 16 wherein said beds are connected in series for a portion of the feed step.

20. The process of claim 1 wherein oxygen is the purge gas.

21. The process of claim 1 wherein cryogenic oxygen gas and/or liquid oxygen is used as the cryogenic fluid in step vi.

22. The process of claim 1 wherein the ion exchange level is at least 80% Ag on an equivalents basis.

23. The process of claim 22 wherein the ion exchange level of said zeolite is at least 90% Ag on an equivalents basis.

24. The process of claim 3 wherein krypton is recovered from the outlet of the adsorbent bed during step i and the recovery of krypton is continued until either the hydrocarbon concentration in the krypton product reaches 50 ppm or until the xenon concentration at the outlet of the adsorbent bed is greater than or equal to 70% of the xenon concentration at the inlet to said adsorbent bed.

Assignees

• Barrett Philip A
• Stephenson Neil A
• Stuckert Nicholas R
• Freiert Michael
• Du Hai
• Masin Rachael A
• Swindlehurst Garrett R
• Praxair Technology Inc

Inventors

• Barrett Philip A
• Stephenson Neil A
• Stuckert Nicholas R
• Freiert Michael
• Du Hai
• Masin Rachael A
• Swindlehurst Garrett R

Classifications

• C01B23/0078

  Temperature swing adsorption · CPC title

• B01D2257/702

  Hydrocarbons · CPC title

• C01B2210/0037

  Xenon · CPC title

• B01D2259/40056

  Gases other than recycled product or process gas · CPC title

• B01J2220/56

  Use in the form of a bed · CPC title