Pressure swing adsorption process

• US 4,482,361 A
• Filed: 01/14/1983
• Issued: 11/13/1984
• Est. Priority Date: 01/14/1983
• Status: Expired due to Fees

• Current Assignee: UOP Des Plaines IL A NY General Partnership
• Original Assignee: Union Carbide Corporation (Dow, Inc.)
• Inventors: Whysall, Michael
• Primary Examiner(s): Spitzer, Robert
• Application Number:
  US06/457,915
• Time in Patent Office: 669 Days
• Field of Search: 55/25, 55/26, 55/58, 55/62, 55/68, 55/75, 55/179, 55/389
• US Class Current: 95/100
• CPC Class Codes: B01D 2256/16 Hydrogen
• CPC Class Codes: B01D 2257/102 Nitrogen
• CPC Class Codes: B01D 2257/504 Carbon dioxide
• CPC Class Codes: B01D 2259/40015 with two sub-steps
• CPC Class Codes: B01D 2259/40016 with three sub-steps
• CPC Class Codes: B01D 2259/4003 with two sub-steps
• CPC Class Codes: B01D 2259/40041 with more than three sub-steps
• CPC Class Codes: B01D 2259/40052 Recycled product or process gas
• CPC Class Codes: B01D 2259/404 using four beds
• CPC Class Codes: B01D 2259/4062 using six beds
• CPC Class Codes: B01D 2259/4063 using seven beds
• CPC Class Codes: B01D 53/053 with storage or buffer vessel
• CPC Class Codes: Y02C 20/40 of CO2

Abstract

Pressure swing adsorption operations for the selective adsorption of a component of a gas mixture is carried out, in multi-bed systems, so that the gas released from a bed during the cocurrent depressurization, provide-purge step is passed partly to another bed and partly to an external vessel. The gas in said vessel is thereafter used to partially repressurize said other bed after it has completed its purge step.

Claims

1. In a pressure swing adsorption process for the selective adsorption of at least one component of a feed gas mixture in an adsorption system having at least four adsorbent beds, each of which undergoes, on a cyclic basis, (1) higher pressure adsorption, (2) cocurrent depressurization from said higher pressure to upper intermediate pressure(s) with release of void space gas from the product end of the bed, said gas being passed directly to another bed(s) in the system and initially at a lower pressure than said upper intermediate pressure(s) for pressure equalization therebetween (3) further cocurrent depressurization from said upper intermediate pressure reached at the completion of step (2) above to a lower intermediate pressure with release of additional void space gas from the product end of the bed, said gas being passed directly to another bed in the system at its lower desorption pressure to provide purge gas directly to said other bed to be purged, (4) purge, in which void space gas released from another bed is passed directly thereto, with or without prior countercurrent depressurization to a lower desorption pressure, (5)partial repressurization to said upper intermediate pressure(s) by the addition of void space gas thereto, said gas being passed to the bed from another bed(s) in the system and initially at a higher pressure than said upper intermediate pressure(s) for pressure equalization therebetween and (6) final repressurization to said higher adsorption pressure from the upper intermediate pressure reached upon completion of said pressure equalization, the improvement consisting essentially of:

(a) passing a portion of the void space gas released from the product end of the adsorbent bed during step (3) above to an empty external vessel for the repressurization thereof simultaneously with the passage of another portion of said void space gas directly to another adsorbent bed in the system to be purged during step (3) above; and

(b) passing void space gas from the thus-repressurized external vessel to the same adsorbent bed into which void space gas was passed directly during step (3) above, with said passage of gas from the external vessel to said bed occurring immediately after said bed completes said purge step using purge gas provided directly in step (3) above, thus partially repressurizing said purged bed, to a pressure greater than its lower desorption pressure prior to further partial repressurization in step (5) above to upper intermediate pressures by pressure equalization with another bed or beds in the adsorption and subsequent final repressurization to said higher adsorption pressure in step (6) above, whereby the product recovery and/or purity obtained in the system are enhanced.

2. The process of claim 1 in which the adsorption system comprises six adsorbent beds.

3. The process of claim 2 in which two beds are on the adsorption step, in overlapping sequence, during all stages of the overall processing cycle.

4. The process of claim 3 in which each bed undergoes two pressure equalization-repressurization steps subsequent to repressurization from said external vessel and prior to said final repressurization to adsorption pressure.

5. The process of claim 1 in which the adsorption system comprises at least seven adsorption beds, with at least two beds being on adsorption, in overlapping sequence during all stages of the overall processing cycle, with each bed undergoing at least one cocurrent depressurization-pressure equalization directly with another bed before said cocurrent depressurization-provide purge and simultaneously repressurized said external vessel step.

6. The process of claim 5 and including a second cocurrent depressurization-pressure equalization step directly with another bed.

7. The process of claim 6 in which three beds are on adsorption, in overlapping sequence, at all stages of the overall processing cycle.

8. The process of claim 1 in which each adsorbent bed undergoes a processing cycle consisting essentially of:

(a) adsorption at higher adsorption pressure;

(b) cocurrent depressurization - direct pressure equalization in which the bed is depressurized from said higher adsorption pressure to an upper intermediate pressure with release of void space gas from the product end thereof, said gas being passed directly to another bed in the system and initially at a lower pressure than said upper intermediate pressure for pressure equalization therebetween at said upper intermediate pressure;

(c) cocurrent depressurization - provide purge gas in which the bed is depressurized from said upper intermediate pressure to a lower intermediate pressure with release of void space gas from the product end of the bed, a portion of said gas being passed to an empty external vessel for the repressurization thereof simultaneously with the passage of another portion of said void space gas directly to another adsorbed bed in the system to be purged;

(d) countercurrent depressurization in which the bed is depressurized from said lower intermediate pressure to a lower desorption pressure with release of gas from the feed end of the bed;

(e) purge at lower desorption pressure with void space gas withdrawn from another adsorbent bed in the system and passed directly to said bed during step (c) of said other adsorbent bed, void space gas from said other adsorbent bed also being simultanteously employed to repressurize said external vessel, said vessel having been emptied subsequent to step (c) above with gas therefrom having been used to partially repressurize the bed to which a portion of void space gas was passed in step (c) above for purge purposes;

(f) partial repressurization of said bed to a pressure greater than its lower desorption pressure by the passage thereto of void space gas used to repressurize the external vessel during purge step (e) above;

(g) further partial repressurization of the bed to said upper intermediate pressure by pressure equalization with another bed in the system, said other bed being initially at higher adsorption pressure; and

(h) final repressurization to adsorption pressure.

9. The process of claim 8 in which four adsorbent beds are employed in said adsorption system.

10. The process of claim 8 in which each bed undergoes a second cocurrent depressurization-direct pressure equalization - prior to the provide purge step and a repressurization by pressure equalization step to partial repressurization from said vessel.

11. The process of claim 10 in which six adsorbent beds are employed said system.

12. The process of claim 10 in which at least seven adsorbent beds employed in said system.

13. The process of claim 12 in which three adsorbent beds are on adsorption, in overlapping sequence, at all stages of the processing cycle.

14. The process of claim 8 in which the product gas withdrawn from the system comprises hydrogen.

15. The process of claim 1 in which the product gas withdrawn from the system comprises hydrogen.