IP Library Granted Patent US 9,669,348
Granted Patent B2
US 9,669,348 · App. 14/551,276 · Granted Jun 6, 2017

PSA process with one active step per phase time

Inventors: Elise Renou (Paris, FR); Christian Monereau (Montpellier, FR); Celine Carriere (Villemomble, FR)
Assignee: L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude
B01D53/047B01D2253/34B01D2256/16B01D2256/22B01D2257/102B01D2257/108B01D2257/502B01D2257/504B01D2257/7025B01D2259/4061B01D2259/4063B01D2259/40064B01D2259/40067B01D2259/4067B01D2259/4068Y02C20/20
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Quick Facts
Patent No.
US 9,669,348
App. No.
14/551,276
Granted
Jun 6, 2017
Kind
B2
Abstract

Pressure shift adsorption (PSA) process for producing a gas stream enriched with compound X from a feed gas stream, using N adsorbers with N≧5, each adsorber being subjected to a pressure cycle having a phase time corresponding to the duration of the pressure cycle divided by the number of adsorbers, and a series of active steps, characterized in that each adsorber n follows the pressure cycle with an offset of one phase time with respect to the pressure cycle of the adsorber n−1 with n≦N, and during each phase time, only one active step or a part of active step takes place.

Claims (16)

1. A pressure swing adsorption process for producing a gas stream enriched with compound X from a feed gas stream, using N adsorbers with N≧ 7 , each adsorber being subjected to a pressure cycle having:

a phase time corresponding to the duration of the pressure cycle divided by the number of adsorbers, and

a series of active steps, including at least one equalization step, characterized in that:

each adsorber n follows the pressure cycle with an offset of one phase time with respect to the pressure cycle of the adsorber n− 1 with n≦N, and

during each phase time, only one active step or a part of an active step takes place.

2. The process according to claim 1 , wherein the active steps are part of the group: adsorption, equalization at descending pressure, feed-purge, countercurrent blowdown, purge, equalization at increasing pressure, recompression by means of the feed gas stream or of the gas stream enriched with compound X and a coupling of these steps.

3. The process according to claim 1 , wherein the adsorbers used have a diameter of between 0.1 m and 6 m.

4. The process according to claim 1 , wherein the adsorbers have a height of between 1 m and 10 m.

5. The process according to claim 1 , wherein at least one step takes place over more than one phase.

6. The process according to claim 1 , wherein the phase time is greater than or equal to 10 seconds.

7. The process according to claim 1 , wherein the pressure cycle is carried out over a period of greater than 1 minute.

8. The process according to claim 1 , wherein the compound X is hydrogen or CO 2 .

9. The process according to claim 1 , wherein the adsorbers comprise particulate adsorbents.

10. The process according to claim 1 , wherein the adsorbers comprise structured adsorbents.

11. The process according to claim 1 , wherein the pressure cycle is controlled by a set of valves and/or of distributors.

12. The process according to claim 1 , wherein the feed gas stream has a flow rate of greater than 100 000 Nm 3 /h.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 24, 2015
From: RENOU, ELISE; MONEREAU, CHRISTIAN; CARRIERE, CELINE
To: L'AIR LIQUIDE, SOCIÉTÉ ANONYME POUR L'ETUDE ET L'EXPLOITATION DES PROCÉDÉS GEORGES CLAUDE
Reel/Frame 035487/0969 →
Priority Claims (1)
FR 13 61731 · Nov 28, 2013 · national
Continuity (1)
Related Publication 20150143993A1 · May 28, 2015