Pressure swing adsorption recovery

• US 4,340,398 A
• Filed: 05/20/1981
• Issued: 07/20/1982
• Est. Priority Date: 05/20/1981
• Status: Expired due to Term

• Current Assignee: UOP Des Plaines IL A NY General Partnership
• Original Assignee: Union Carbide Corporation (Dow, Inc.)
• Inventors: Doshi, Kishore J., Patel, Kirit M.
• Primary Examiner(s): Spitzer, Robert H.
• Application Number:
  US06/265,659
• Time in Patent Office: 426 Days
• Field of Search: 55/25, 55/26, 55/62, 55/68, 55/74, 55/75, 55/179, 55/180, 55/387, 55/389, 55/58
• US Class Current: 95/103
• CPC Class Codes: B01D 2256/16 Hydrogen
• CPC Class Codes: B01D 2257/504 Carbon dioxide
• CPC Class Codes: B01D 2259/4003 with two sub-steps
• CPC Class Codes: B01D 2259/40037 with two sub-steps
• CPC Class Codes: B01D 2259/40062 Four
• CPC Class Codes: B01D 2259/40064 Five
• CPC Class Codes: B01D 2259/403 using three beds
• CPC Class Codes: B01D 2259/404 using four beds
• CPC Class Codes: B01D 2259/4067 using ten beds
• CPC Class Codes: B01D 53/047 Pressure swing adsorption
• CPC Class Codes: B01D 53/053 with storage or buffer vessel
• CPC Class Codes: Y02C 20/40 of CO2

Abstract

Void space gas is released from an adsorbent bed at a higher adsorption pressure by cocurrent depressurization of the bed. The released gas is passed to another bed of a pressure swing adsorption system to equalize the pressure therebetween, the other bed being initially at a lower pressure. A portion of the product effluent withdrawn from yet another bed of the system is not passed to the bed undergoing repressurization, as in conventional practice, but is passed to an external repressurization storage tank during said pressure equalization step. Upon completion of this step, the product effluent is withdrawn from the repressurization tank and passed to said bed undergoing repressurization.

Claims

1. In a pressure swing adsorption process for the selective adsorption of at least one gas component from a feed gas mixture in an adsorption system having at least three adsorbent beds, each of which undergoes, on a cyclic basis, higher pressure adsorption, cocurrent depressurization to intermediate pressure with release of void space gas from the bed, countercurrent depressurization to a lower desorption pressure, and repressurization to said higher pressure, and in which the void space gas released from one bed is passed to the product end of another bed initially at a lower pressure to equalize the pressure therebetween, said other bed also being repressurized by a portion of the product eflluent withdrawn from a bed undergoing adsorption at said higher pressure, the improvement comprising:

(a) introducing released void space gas to be used for said pressure equalization purposes directly into the bed undergoing repressurization to equalize the pressure between the beds at an intermediate pressure;

(b) simultaneously passing a portion of the product effluent withdrawn from a bed undergoing adsorption at said higher pressure to an external repressurization storage tank; and

(c) upon completion of said pressure equalization, passing said gas from said repressurization storage tank to said bed undergoing repressurization, together with an additional portion of product effluent withdrawn from a bed undergoing adsorption at said higher pressure, whereby product recovery is enhanced without discontinuity in the substantially uniform flow of product effluent from the adsorption system.

2. The process of claim 1 in which said feed gas mixture is passed, on a cyclic basic, to four adsorbent beds.

3. The process of claim 1 in which said feed gas mixture is passed, on a cyclic basis, to five or six adsorbent beds.

4. The process of claim 3 in which feed gas is passed to two adsorbent beds at all stages of the processing cycle.

5. The process of claim 3 in which said bed undergoing repressurization is pressure equalized with the void space gas released from another bed to a lower intermediate pressure prior to the pressure equalization of said bed to said intermediate pressure.

6. The process of claim 1 in which said feed mixture is passed, on a cyclic basis, to seven or more adsorbent beds.

7. The process of claim 6 in which feed gas is passed to at least two adsorbent beds at all stages of the processing cycle.

8. The process of claim 7 in which, prior to said pressure equalization at said intermediate pressure, each bed undergoes two pressure equalization steps to lower intermediate pressures.

9. The process of claim 8 in which said feed gas mixture is passed, on a cyclic basis, to nine or ten adsorbent beds.

10. The process of claim 9 and including a fourth pressure equalization step for each bed prior to said final repressurization.

11. The process of claim 7 in which the product effluent comprises hydrogen and the selectively adsorbed component comprises carbon dioxide.

12. The process of claim 1 and including passing a minor portion of the released void space gas to be used for said pressure equalization purposes to said repressurization storage tank prior to introducing the major portion of said void space gas directly into the bed undergoing repressurization, and introducing said void space gas from the repressurization storage tank, together with product effluent, into the bed undergoing repressurization subsequent to said introduction of said major portion of the void space gas directly into said bed.

13. In a pressure swing adsorption system of at least three adsorbent beds for the selective adsorption of at least one gas component from a feed gas mixture, said system having conduit means for withdrawing product effluent from each bed at a higher adsorption pressure, on a cyclic basis, and for withdrawing a portion of said product effluent for delivery to an other bed undergoing repressurization from a lower pressure to said higher adsorption pressure, and conduit means for passing void space gas released from each bed, on a cyclic basis, to an other bed undergoing said repressurization for pressure equalization to an intermediate pressure, the improvement comprising:

(a) an external repressurization storage tank;

(b) means for passing said withdrawn portion of the product effluent to the repressurization tank for delivery to a bed undergoing repressurization; and

(c) means for passing product effluent from the repressurization tank to an other bed undergoing repressurization, on a cyclic basis, said means providing for the passage of said product effluent to said other bed subsequent to the repressurization of said bed from a lower pressure to an intermediate pressure by pressure equalization with a bed undergoing depressurization,

whereby product recovery is enhanced without discontinuity in the substantially uniform flow of product effluent from the adsorption system.

14. The system of claim 13 in which four adsorbent beds are incorporated into said system.

15. The system of claim 13 in which five or six adsorbent beds are incorporated into said system.

16. The system of claim 13 in which at least seven adsorbent beds are incorporated into said system.

17. The system of claim 16 and including means for passing feed gas to two adsorbent beds at all stages of the processing cycle.

18. The system of claim 17 and including means for pressure equalizing said other bed undergoing repressurization, on a cyclic basis, to two lower intermediate pressures prior to said pressure equalization from such lower pressure to said intermediate pressure and the passage of product effluent from the repressurization tank to said other bed.

19. The system of claim 18 in which eight or nine adsorbent beds are incorporated into said system.

20. The system of claim 18 in which ten adsorbent beds are incorporated into said system.

21. The system of claim 13 and including means for passing void space gas from each bed, on a cyclic basis, to said repressurization tank.

22. The system of claim 17 and including means for passing void space gas from each bed, on a cyclic basis, to said repressurization tank.