Hydrogen purification by selective adsorption

• US 4,077,779 A
• Filed: 10/15/1976
• Issued: 03/07/1978
• Est. Priority Date: 10/15/1976
• Status: Expired due to Term

• Current Assignee: Air Products and Chemicals Incorporated (Linde Plc)
• Original Assignee: Air Products and Chemicals Incorporated (Linde Plc)
• Inventors: Sircar, Shivaji, Zondlo, John W.
• Primary Examiner(s): Hart, Charles N.
• Assistant Examiner(s): Cross, E. Rollins
• Application Number:
  US05/732,609
• Time in Patent Office: 508 Days
• Field of Search: 55/62, 55/68, 55/74, 55/58, 55/26, 55/25
• US Class Current: 95/26
• CPC Class Codes: B01D 2253/102 Carbon
• CPC Class Codes: B01D 2256/16 Hydrogen
• CPC Class Codes: B01D 2257/504 Carbon dioxide
• CPC Class Codes: B01D 2257/702 Hydrocarbons
• CPC Class Codes: B01D 2257/7025 Methane
• CPC Class Codes: B01D 2259/4003 with two sub-steps
• CPC Class Codes: B01D 2259/40052 Recycled product or process gas
• CPC Class Codes: B01D 2259/40056 Gases other than recycled product or process gas
• CPC Class Codes: B01D 2259/40066 Six
• CPC Class Codes: B01D 2259/404 using four beds
• CPC Class Codes: B01D 2259/4062 using six beds
• CPC Class Codes: B01D 53/0476 Vacuum pressure swing adsorption
• CPC Class Codes: C01B 2203/043 Regenerative adsorption process in two or more beds, one for adsorption, the other for regeneration
• CPC Class Codes: C01B 2203/0475 the impurity being carbon dioxide
• CPC Class Codes: C01B 2203/048 the impurity being an organic compound
• CPC Class Codes: C01B 3/56 by contacting with solids; Regeneration of used solids C01B3/508 takes precedence
• CPC Class Codes: Y02C 20/20 of methane
• CPC Class Codes: Y02C 20/40 of CO2
• CPC Class Codes: Y02P 20/151 Reduction of greenhouse gas [GHG] emissions, e.g. CO2
• CPC Class Codes: Y02P 20/156 Methane [CH4]

Abstract

Hydrogen-containing gas mixtures are subjected to selective adsorption in a pressure swing cyclic system to remove carbon dioxide and/or hydrocarbon gases, obtaining high recovery of hydrogen at high purity. The system can also be employed for separation of methane from admixture with CO₂.

Claims

1. The method of separating the components of a gaseous mixture into a primary gaseous product and a secondary gaseous product, in a system comprising a plurality of adsorption zones operated in cycle in a predetermined timed sequence, each of which adsorption zones contains a bed of solid sorbent preferentially selective for said secondary gaseous product component, which method comprises the following sequence of operational steps performed in the order recited in each of said adsorption zones in its turn:

(a) during a predetermined time period introducing the gaseous mixture to be separated to one of said adsorption zones and passing the same through the bed of sorbent in said zone while discharging from said zone unsorbed gas as primary gaseous product, said adsorption zone having been previously brought to desired superatmospheric feed gas pressure with primary gaseous product withdrawn from another adsorbent zone of said system;

(b) terminating operation of step (a) above as applied to the designated adsorbent zone and rinsing said zone in the direction of initial feed gas flow therethrough, with a stream of recompressed secondary gaseous product and at about the prevailing superatmospheric pressure of said adsorbent zone, while discharging from said zone a gaseous rinse effluent which is recycled to another adsorption zone of said system then undergoing step (a) for admixture with gaseous feed mixture being admitted to said other adsorption zone;

(c) lowering to an intermediate level the pressure in the zone that has undergone step (b) to desorb from said zone residual gas therein present and withdrawing said residual gas from said zone in a direction counter to that of earlier feed gas flow therein, said withdrawn residual gas being recompressed for use, at least in part, to rinse an adsorption zone of said system undergoing step (b);

(d) at about said intermediate pressure level purging the zone that has just undergone step (c) with air or an inert gas less strongly sorbed than said secondary gaseous product component of the feed gas mixture;

thereafter

(e) evacuating the thus purged zone to a sub-atmospheric pressure level to remove therefrom purge gas introduced in step (d), and

(f) repressuring the zone to about the feed pressure of step (a) by admission thereto of a part of the primary product gas component withdrawn from an adsorption zone of said series then undergoing step (a).

2. The method as defined in claim 1 wherein said gaseous mixture to be separated comprises hydrogen in admixture with at least one gas from the group consisting of CO₂ and CH₄.

3. The method as defined in claim 2 wherein said secondary product gas component is non-combustible and air is utilized as purge gas in step (d).

4. The method as defined in claim 2 wherein an inert gas is utilized as purge gas in step (d).

5. The method as defined in claim 2 wherein said system comprises four adsorbent zones in parallel operation, and the recompressed gas from step (c) is stored for subsequent use in an adsorption zone undergoing step (b).

6. The method as defined in claim 2 wherein said system comprises six adsorbent zones in parallel operation and the recompressed gas from step (c) is sent directly to another adsorption zone of said system then undergoing step (b).

7. The method as defined in claim 1 wherein said gaseous mixture to be separated comprises predominantly hydrogen, in admixture with a lesser quantity of CO₂.

8. The method as defined in claim 7 wherein the solid sorbent comprises activated carbon.

9. The method as defined in claim 1 wherein said gaseous mixture to be separated comprises CO₂ in admixture with methane.

10. The method as defined in claim 1 wherein said system comprises four adsorbent zones in parallel operation, and the recompressed gas from step (c) is stored for subsequent use in an adsorption zone undergoing step (b).

11. The method as defined in claim 1 wherein said system comprises six adsorbent beds in parallel operation and the recompressed gas from step (c) is sent directly to another adsorption zone of said system then undergoing step (b).

12. The method as defined in claim 1 wherein said evacuation of the adsorption zone undergoing step (e) is effected in a direction counter to that of initial passage of the feed gas mixture through said zone.

13. The method as defined in claim 1 wherein said evacuation of the adsorption zone undergoing step (e) is effected simultaneously at opposite ends of said zone.

14. The method as defined in claim 1 wherein said evacuation of the adsorption zone undergoing step (e) is effected at a position intermediate the feed and discharge ends of the column.

15. The method as defined in claim 1 wherein the solid sorbent comprises activated carbon.