Oxygen selective adsorbents

• US 5,447,557 A
• Filed: 03/23/1994
• Issued: 09/05/1995
• Est. Priority Date: 03/23/1994
• Status: Expired due to Fees

• Current Assignee: Air Products and Chemicals Incorporated (Linde Plc)
• Original Assignee: Air Products and Chemicals Incorporated (Linde Plc)
• Inventors: Mead, Mindy N., Kratz, Wilbur C., Golden, Timothy C.
• Primary Examiner(s): SPITZER, ROBERT H
• Application Number:
  US08/216,739
• Time in Patent Office: 531 Days
• Field of Search: 95/96, 95/106, 95/115, 95/138, 95/901, 95/903, 96/108, 96/153, 55/512, 55/524, 423/219
• US Class Current: 95/96
• CPC Class Codes: B01D 2253/102 Carbon
• CPC Class Codes: B01D 2256/10 Nitrogen
• CPC Class Codes: B01D 2257/104 Oxygen
• CPC Class Codes: B01D 2259/40066 Six
• CPC Class Codes: B01D 2259/40071 Nine
• CPC Class Codes: B01D 2259/402 using two beds
• 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 53/047 Pressure swing adsorption
• CPC Class Codes: B01J 20/20 comprising free carbon; comprising carbon obtained by carbonising processes
• CPC Class Codes: Y10S 95/903 Carbon

Abstract

An oxygen selective adsorbent and a method for making an oxygen selective adsorbent wherein a porous carbon substrate such as a carbon molecular sieve, activated carbon, carbon black, coal, or petroleum coke, is impregnated with a solution of an acidic species and the impregnated substrate is dried. The oxygen selective adsorbent can be used in a pressure swing adsorption process for the separation of oxygen from nitrogen, for example, in air.

Claims

1. A method for separating oxygen from air comprising the steps of:

(1) pressurizing an adsorbent bed containing an oxygen selective adsorbent comprising a porous carbon substrate impregnated with an acidic species;

(2) passing a pressurized air stream over said adsorbent bed;

(3) adsorbing oxygen from said pressurized air stream to produce a nitrogen enriched stream;

(4) withdrawing said nitrogen enriched stream from said adsorbent bed;

(5) stopping the flow of said pressurized air stream;

(6) depressurizing said adsorbent bed; and

(7) repeating steps 1 through 6 in a cyclic fashion.

2. The method of claim 1 wherein said porous carbon substrate is a carbon molecular sieve.

3. The method of claim 2 wherein said acidic species is a transition metal halide.

4. The method of claim 3 wherein said steps are carried out in two adsorbent beds so that while one bed is at step (2), the second bed is at step (5).

5. An oxygen selective adsorbent comprising a carbon molecular sieve impregnated with an acidic species.

6. The oxygen selective adsorbent of claim 5 wherein said acidic species is selected from the group consisting of ferric chloride, aluminum chloride, boric acid, hydrochloric acid, and acetic acid.

7. The oxygen selective adsorbent of claim 5 wherein said acidic species is a transition metal halide.

8. The oxygen selective adsorbent of claim 7 wherein said carbon molecular sieve is impregnated with approximately 0.01 wt % to about 10 wt % of said transition metal halide.

9. A method for making an oxygen selective adsorbent comprising:

(a) impregnating a carbon molecular sieve with a solution of an acidic species; and

(b) drying the impregnated carbon molecular sieve to form said oxygen selective adsorbent.

10. The method of claim 9 wherein said acidic species is selected from the group consisting of ferric chloride, aluminum chloride, boric acid, acetic acid and hydrochloric acid.

11. The method of claim 9 wherein said acidic species is a transition metal halide.

12. The method of claim 11 wherein said porous carbon substrate is impregnated with approximately 0.01 wt % to about 10 wt % of said transition metal halide.