US4969935A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for treating a gaseous mixture by adsorption
Assignee: LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
•
Filing: 1989-07-05
•
Granted: 1990-11-13
•
Expires: 2009-07-05
Abstract
Abstract This PSA cycle comprises two successive pressure equilibration steps in the course of which gas is withdrawn in a cocurrent manner from an adsorber at the beginning of countercurrent decompression and respectively introduced in a countercurrent manner and then in a cocurrent manner in another adsorber at the beginning of recompression. Application in the production of impure oxygen from air of the atmosphere.
Inventors
- 👤 Leon Hay
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 22:49
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/02; B01D53/04; B01D53/047; B01D2253/00; B01D2253/10; B01D2253/104; B01D2253/106; B01D2256/00; B01D2256/12; B01D2257/00; B01D2257/10; B01D2257/102; B01D2257/11; B01D2259/00; B01D2259/40; B01D2259/40011; B01D2259/4002; B01D2259/40024; B01D2259/40028; B01D2259/40032; B01D2259/40043; B01D2259/4005; B01D2259/40052; B01D2259/40058; B01D2259/40069; B01D2259/403
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
320 words
Process for treating a gaseous mixture of constituents by pressure swing adsorption, the process comprising providing three, and no more than three, adsorbers, and performing for each adsorber, a cycle comprising the following successive operational stages, the cycle being staggered from one adsorber to the other by a duration T/3 in which T designates the duration of the cycle: (a) a substantially isobaric adsorption stage at a high pressure of the cycle, said adsorption stage comprising admission of the mixture into the adsorber through a first end, termed inlet end, of the adsorber, with circulation of the mixture in the adsorber and simultaneous withdrawal at the other end, termed outlet end, of the adsorber of an enriched fraction enriched with one of the constituents of which a part forms a production gas, the direction of circulation in the adsorber in the course of said adsorption stage being termed cocurrent; (b) a desorption stage comprising at least an initial decompression step from said high pressure to a low pressure of the cycle, said decompression step comprising an initial sub-step (b1) for equilibrating pressures in the course of which gas is withdrawn from said adsorber in a cocurrent manner simultaneously with decompression by countercurrent withdrawal of gas from said adsorber and is transferred into another adsorber which is at the beginning of a pressure raising stage (c) described hereinafter; and (c) a recompression stage for raising pressure to said high pressure, said recompression stage (c) comprising an initial pressure-equilibrating step in the course of which the first-mentioned adsorber receives a received gas coming from another adsorber which is in said initial sub-step (b1), said initial pressure-equilibrating step being divided into two successive sub-steps, namely a first sub-step during which said received gas is introduced in a countercurrent manner into the first-mentioned adsorber, and subsequently a second sub-step during which said received gas is introduced in a cocurrent manner into the first-mentioned adsorber.
Claim 2
Dependent Claim
320 words
Process for treating a gaseous mixture of constituents by pressure swing adsorption, the process comprising providing three, and no more than three, adsorbers, and performing for each adsorber, a cycle comprising the following successive operational stages, the cycle being staggered from one adsorber to the other by a duration T/3 in which T designates the duration of the cycle: (a) a substantially isobaric adsorption stage at a high pressure of the cycle, said adsorption stage comprising admission of the mixture into the adsorber through a first end, termed inlet end, of the adsorber, with circulation of the mixture in the adsorber and simultaneous withdrawal at the other end, termed outlet end, of the adsorber of an enriched fraction enriched with one of the constituents of which a part forms a production gas, the direction of circulation in the adsorber in the course of said adsorption stage being termed cocurrent; (b) a desorption stage comprising at least an initial decompression step from said high pressure to a low pressure of the cycle, said decompression step comprising an initial sub-step (b1) for equilibrating pressures in the course of which gas is withdrawn from said adsorber in a cocurrent manner simultaneously with decompression by countercurrent withdrawal of gas from said adsorber and is transferred into another adsorber which is at the beginning of a pressure raising stage (c) described hereinafter; and (c) a recompression stage for raising pressure to said high pressure, said recompression stage (c) comprising an initial pressure-equilibrating step in the course of which the first-mentioned adsorber receives a received gas coming from another adsorber which is in said initial sub-step (b1), said initial pressure-equilibrating step being divided into two successive sub-steps, namely a first sub-step during which said received gas is introduced in a countercurrent manner into the first-mentioned adsorber, and subsequently a second sub-step during which said received gas is introduced in a cocurrent manner into the first-mentioned adsorber.
Claim 3
Dependent Claim
63 words
Process according to claim 1, wherein the desorption stage comprises a final elution step at the low pressure of the cycle in the course of which gas withdrawn from the outlet end of another adsorber which is in an adsorption stage is introduced in a countercurrent manner into the first-mentioned adsorber while gas is withdrawn from the inlet end of said first-mentioned adsorber.
Claim 4
Dependent Claim
50 words
Process according to claim 1, wherein the pressure raising stage comprises a final step during which is first-mentioned adsorber is recompressed in a countercurrent manner until said high pressure of the cycle is reached by gas withdrawn at the outlet end of another adsorber which is in the adsorption stage.
Claim 5
Dependent Claim
28 words
Process according to claim 1, wherein the gaseous mixture is essentially constituent by oxygen, nitrogen, and argon, and said enriched fraction contains substantially 90 to 95% of oxygen.
References Cited (Backward Citations)
US3430418A
Cited
US3564816A
Cited
US3717974A
Cited
US3636679A
Cited
US3738087A
Cited
US3796022A
Cited
US4042349A
Cited
US3923477A
Cited
US4519813A
Cited
US4431432A
Cited
US4640694A
Cited
US4512779A
Cited
GB2154465A
Cited
GB2155805A
Cited
US4650500A
Cited
FR2579484A1
Cited
US4840647A
Cited
EP0248720A1
Cited
US4781735A
Cited
US4756723A
Cited
FR2612083A1
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1993-11-12 | 1994-05-14 | 1994-11-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1997-11-12 | 1998-05-14 | 1998-11-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2001-11-12 | 2002-05-14 | 2002-11-13 | $7700.00 | Window Closed / Lapsed |