Selective adsorption on magnesium-containing clinoptilolites

• US 4,964,889 A
• Filed: 12/04/1989
• Issued: 10/23/1990
• Est. Priority Date: 12/04/1989
• Status: Expired due to Term

• Current Assignee: UOP Llc (Honeywell International Inc.)
• Original Assignee: UOP Llc (Honeywell International Inc.)
• Inventors: Chao, Chien-Chung
• Primary Examiner(s): SPITZER, ROBERT H
• Application Number:
  US07/445,502
• Time in Patent Office: 323 Days
• Field of Search: 55/58, 55/68, 55/75, 55/389, 423/239, 423/328, 423/331, 502/60, 502/514
• US Class Current: 95/96
• CPC Class Codes: B01D 2253/108 Zeolites
• CPC Class Codes: B01D 2256/24 Hydrocarbons
• 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 53/02 by adsorption, e.g. preparative gas chromatography solid sorbent compositions B01J20/00, preparation of inorganic compounds or elements C01
• CPC Class Codes: B01D 53/04 with stationary adsorbents B01D53/025 takes precedence
• CPC Class Codes: B01D 53/047 Pressure swing adsorption
• CPC Class Codes: B01J 20/186 Chemical treatments in view of modifying the properties of the sieve, e.g. increasing the stability or the activity, also decreasing the activity
• CPC Class Codes: Y02C 20/40 of CO2
• CPC Class Codes: Y10S 95/902 Molecular sieve

Abstract

Gases having molecular dimensions equal to or smaller than nitrogen are selectively adsorbed and separated from other gases having molecular dimensions equal to or larger than methane using a clinoptilolite molecular sieve that contains magnesium cations. The clinoptilolite molecular sieves of the present invention can be ion-exchanged with magnesium cations and optionally with other cations such as lithium, sodium, potassium, calcium, barium, strontium, zinc, copper, cobalt, iron and manganese to produce the desired separation characteristics. Processes are disclosed for separating gases by adsorbing at an elevated pressure and regenerating, or desorbing, by reducing the pressure. Methods for the preparation of a magnesium-exchanged clinoptilolite are disclosed.

Claims

1. A process for separating a first gas containing molecules having molecular dimensions equal to or smaller than nitrogen from a feed containing mixtures thereof with at least one other gas containing molecules having molecular dimensions equal to or larger than methane, which comprises contacting the feed with a clinoptilolite molecular sieve that has a magnesium cation content that is sufficient to cause the first gas to be selectively absorbed on the clinoptilolite molecular sieve, said magnesium cation content being at least about 5 equivalent percent of the ion-exchangeable cations in the clinoptilolite molecular sieve, and recovering an effluent having a reduced amount of the first gas relative to the feed.

2. A process according to claim 1 wherein the clinoptilolite molecular sieve has been ion-exchanged with magnesium cations.

3. A process according to claim 1 wherein from about 5 to 85 equivalent percent of the ion-exchangeable cations in the clinoptilolite are magnesium cations.

4. A process according to claim 3 wherein from about 10 to 65 equivalent percent of the ion-exchangeable cations in the clinoptilolite are magnesium cations.

5. A process according to claim 1 wherein the clinoptilolite molecular sieve has been ion-exchanged with at least one cation selected from the group consisting of lithium, potassium, sodium, calcium, barium, strontium, zinc, copper, cobalt, iron and manganese catios, to an extent that not more than about 95 equivalent percent of the ion-exchangeable cations are cations from said group.

6. A process according to claim 5 wherein from about 2 to 80 equivalent percent of the ion-exchangeable cations in the clinoptilolite are potassium cations.

7. A process according to claim 5 wherein from about 2 to 40 equivalent percent of the ion-exchangeable cations in the clinoptilolite are sodium cations.

8. A process according to claim 5 wherein from about 10 to 75 equivalent percent of the ion-exchangeable cations in the clinoptilolite are potassium cations and from about 4 to 35 equivalent percent of the ion-exchangeable cations in the clinoptilolite are sodium cations.

9. A process according to claim 5 wherein from about 5 to 45 equivalent percent of the ion-exchangeable cations in the clinoptilolite are magnesium cations and from about 30 to 80 equivalent percent of the ion-exchangeable cations in the clinoptilolite are potassium cations and from about 4 to 35 equivalent percent of the ion-exchangeable cations in the clinoptilolite are sodium cations.

10. A process according to claim 5 wherein from about 45 to 85 equivalent percent of the ion-exchangeable cations in the clinoptilolite are magnesium cations and from about 2 to 30 equivalent percent of the ion-exchangeable cations in the clioptilolite are potassium cations and from about 4 to 35 equivalent percent of the ion-exchangeable cations in the clinoptilolite are sodium cations.

11. A process according to claim 1 wherein the first gas comprises at least one of carbon monoxide, carbon dioxide, nitrogen and oxygen.

12. A process according to claim 1 wherein the other gas comprises at least one of methane, ethylene, ethane, propylene, propane, a butane and a butene.

13. A process according to claim 1 wherein the feed comprises nitrogen and methane.

14. A process according to claim 1 wherein the feed comprises carbon monoxide and methane.

15. A process according to claim 1 wherein the clinoptilolite molecular sieve is a natural clinoptilolite.

16. A process for separating a first gas containing molecules having molecular dimension equal to or smaller than nitrogen from a feed containing mixtures thereof with at least one other gas containing molecules having molecular dimensions equal to or larger than methane by the selective adsorption of the gas, which comprises the steps of:

(a) passing the feed to an absorber bed containing a clinoptilolite molecular sieve that has a magnesium cation content that is sufficient to cause the first gas to be selectively absorbed on the clinoptilolite molecular sieve, said mangesium cation content being at least about 5 equivalent percent of the ion-exchangeable cations in the clinoptilolite molecular sieve at conditions effective to cause the first gas to be selectively absorbed on said clinoptilolite, said conditions selected from a temperature of from about-50°

to 100°

C. and at a pressure of from about 0.2 psia to 1500 psia and recovering an effluent having a reduced amount of the first gas relative to the feed, and;

(b) regenerating said absorber bed by desorbing nitrogen therefrom by decreasing the pressure in said absorber bed to below the adsorption pressure of step (a) and to within the range of 0.1 torr to 150 psia.

17. A process according to claim 16 wherein the clinoptilolite molecular sieve has been ion-exchanged with magnesium cations.

18. A process according to claim 16 wherein the clinoptilolite molecular sieve has been ion-exchanged with at least one cation selected from the group consisting of lithium, potassium, sodium, calcium, barium, strontium, zinc, copper, cobalt, iron and manganese cations, to an extent that not more than about 95 equivalent percent of the ion-exchangeable cations are cations from said group.

19. A process according to claim 16 wherein the feed comprises a nitrogen-containing natural gas.

20. A process according to claim 16 wherein the feed comprises a nitrogen-containing petroleum gas.

21. A process according to claim 16 wherein the feed comprises a reformer effluent gas.

22. A process according to claim 16 wherein step (a) is performed at a temperature of from about 0°

to 50°

C. and at a pressure of from about 50 psia to 500 psia.

23. A process according to claim 16 wherein step (b) is performed at a pressure of from about 0.1 torr to 250 torr.

24. A process for the production of a modified clinoptilolite wherein at least about 5 equivalent percent of the ion-exchangeable cations in the clinoptilolite comprises magnesium cations, said process comprising subjecting a clinoptilolite to at least one ion-exchange with a solution containing any one or more of lithium, potassium, calcium, sodium, barium, strontium, zinc, copper, cobalt, iron and manganese cations, thereby producing an ion-exchanged clinoptilolite, and thereafter subjecting said ion-exchanged clinoptilolite to ion-exchange with a solution containing magnesisum cations to produce a magnesium-exchanged clinoptilolite.

25. A process according to claim 24 wherein from about 5 to 85 equivalent percent of the ion-exchangeable cations in the clinoptilolite are magnesium cations and from about 2 to 80 equivalent percent of the ion-exchangeable cations in the clinoptilolite are potassium cations and from about 2 to 40 equivalent percent of the ion-exchangeable cations in the clinoptilolite are sodium cations.

26. A process according to claim 25 wherein from about 5 to 45 equivalent percent of the ion-exchangeable cations in the clinoptilolite are magensium cations and from about 30 to 80 equivalent percent of the ion-exchangeable cations in the clinoptilolite are potassium cations and from about 4 to 35 equivalent percent of the ion-exchangeable cations in the clinoptilolite are sodium cations.

27. A process according to claim 25 wherein from about 45 to 85 equivalent percent of the ion-exchangeable cations in the clinoptilolite are magnesium cations, from about 2 to 30 equivalent percent of the ion-exchangeable cations in the clinoptilolite are potassium cations and from about 4 to 35 equivalent percent of the ion-exchangeable cations in the clinoptilolite are sodium cations.

28. A process according to claim 24 wherein the ion-exchanged clinoptilolite is admixed with a binder and heated to produce pellets of clinoptilolite bound together by the binder, and the ion-exchange with magnesium cations is effected on the pellets so formed.

29. A process according to claim 28 wherein the binder is a clay binder.

30. A process according to claim 24 wherein the magnesium clinoptilolite is heated at a temperature and for a time sufficient to cause the clinoptilolite to become activated.

31. A process according to claim 30 wherein the magnesium clinoptilolite is heated in air to a temperature of about 300°

-650°

C. for about 1 hour.