US4421530A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for removing oxygen from mixed gas streams using a swing adiabatic absorption-isothermal desorption cycle
Assignee: Air Products and Chemicals Inc
•
Filing: 1982-09-13
•
Granted: 1983-12-20
•
Expires: 2002-09-13
Abstract
Abstract An adiabatic-isothermal swing absorption process is disclosed for the removal of essentially all oxygen contained in an inert gas stream. The oxygen is absorbed from an inert gas stream adiabatically on to a dioxygen absorbent and then desorbed from the absorbent isothermally by the use of external heat. The process method utilizes at least two switching beds of the dioxygen absorbent in which one bed is in an absorbing mode while the other bed is in a desorbing mode.
Inventors
- 👤 Augustine I. Dalton, Jr.
- 👤 John J. Sheridan, III
- 👤 David A. Zagnoli
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 03:03
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/02; B01D53/04; B01D53/047; B01D2253/00; B01D2253/10; B01D2253/112; B01D2253/1122; B01D2253/25; B01D2256/00; B01D2256/18; B01D2257/00; B01D2257/10; B01D2257/104; B01D2259/00; B01D2259/40; B01D2259/40007; B01D2259/40009; B01D2259/40011; B01D2259/40043; B01D2259/4005; B01D2259/40052; B01D2259/40058; B01D2259/40062; B01D2259/40064; B01D2259/402; B01D2259/416; B01D2259/65; B01D2259/655
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
316 words
A process for removing oxygen from an inert gas stream containing oxygen by adiabatic absorption of the oxygen on a dioxygen absorbent and isothermal desorption of the oxygen during dioxygen absorbent regeneration wherein the process is designed to operate below the temperature of decomposition of the absorbent comprising the steps of: (a) introducing an oxygen-containing inert gas stream into a first bed of a dioxygen absorbent at a temperature chosen on an isotherm of the particular dioxygen absorbent so as to allow adiabatic absorption to proceed without reaching the temperature of degradation of said absorbent; (b) adiabatically absorbing essentially all of the oxygen content of said inert gas stream on said dioxygen absorbent, while removing an essentially oxygen-free inert gas from said bed; (c) terminating said absorption on said first bed before oxygen therethrough in said bed; (d) switching the flow of the inert gas stream to a second dioxygen absorbent bed for adiabatic absorption of the oxygen content of said stream, while removing an essentially oxygen-free inert gas from said bed; (e) desorbing said first bed isothermally by supplying a high temperature heat exchange fluid to said bed to drive absorbed oxygen off said dioxygen absorbent; (f) cooling said first bed to the initial absorbent temperature; (g) representing said first bed with essentially pure oxygen-free inert gas from the downstream flow of product gas from said second bed; (h) terminating said absorption on said second bed before oxygen breakthrough in said bed; (i) switching the flow of the inert gas stream back to the first bed, while desorbing the second bed as described in step (e) above; (j) cooling said second bed to the initial absorbent temperature; (k) repressurizing the second bed with essentially pure oxygen-free inert gas from the downstream flow of product gas from said first bed; (1) cyclically repeating steps (a) through (k) for the production of an essentially oxygen-free inert gas.
Claim 2
Dependent Claim
316 words
A process for removing oxygen from an inert gas stream containing oxygen by adiabatic absorption of the oxygen on a dioxygen absorbent and isothermal desorption of the oxygen during dioxygen absorbent regeneration wherein the process is designed to operate below the temperature of decomposition of the absorbent comprising the steps of: (a) introducing an oxygen-containing inert gas stream into a first bed of a dioxygen absorbent at a temperature chosen on an isotherm of the particular dioxygen absorbent so as to allow adiabatic absorption to proceed without reaching the temperature of degradation of said absorbent; (b) adiabatically absorbing essentially all of the oxygen content of said inert gas stream on said dioxygen absorbent, while removing an essentially oxygen-free inert gas from said bed; (c) terminating said absorption on said first bed before oxygen therethrough in said bed; (d) switching the flow of the inert gas stream to a second dioxygen absorbent bed for adiabatic absorption of the oxygen content of said stream, while removing an essentially oxygen-free inert gas from said bed; (e) desorbing said first bed isothermally by supplying a high temperature heat exchange fluid to said bed to drive absorbed oxygen off said dioxygen absorbent; (f) cooling said first bed to the initial absorbent temperature; (g) representing said first bed with essentially pure oxygen-free inert gas from the downstream flow of product gas from said second bed; (h) terminating said absorption on said second bed before oxygen breakthrough in said bed; (i) switching the flow of the inert gas stream back to the first bed, while desorbing the second bed as described in step (e) above; (j) cooling said second bed to the initial absorbent temperature; (k) repressurizing the second bed with essentially pure oxygen-free inert gas from the downstream flow of product gas from said first bed; (1) cyclically repeating steps (a) through (k) for the production of an essentially oxygen-free inert gas.
Claim 3
Dependent Claim
17 words
The process of claim 1 wherein the inert gas stream is an argon stream contaminated with oxygen.
Claim 4
Dependent Claim
38 words
The process of claim 1 wherein the dioxygen absorbent is selected from the class comprising metal chelates of Group III--VIII metals which will bind molecular oxygen reversibly while preserving the oxygen to oxygen bond of the oxygen molecule.
Claim 5
Dependent Claim
14 words
The process of claim 1 wherein the dioxygen absorbent is Salcomine or its derivatives.
Claim 6
Dependent Claim
19 words
The process of claim 1 wherein the absorbent beds of dioxygen chelate also contain a high heat capacity material.
Claim 7
Dependent Claim
23 words
The process of claim 5 wherein the dioxygen absorbent and the heat capacity additive are provided in the absorbent beds in simple admixture.
Claim 8
Dependent Claim
22 words
The process of claim 5 wherein the high heat capacity material is selected from the group consisting particulate copper and particulate alumina.
Claim 9
Dependent Claim
21 words
The process of claim 5 wherein the dioxygen absorbent is physically supported on the heat capacity material in the absorbent bed.
Claim 10
Dependent Claim
27 words
The process of claim 5 wherein the dioxygen absorbent and the heat capacity additive are encapsulated or bonded together in a polymer matrix in said absorbent bed.
Claim 11
Dependent Claim
28 words
The process of claim 1, 2, 3, 4 or 5 wherein the absorption in said beds is initiated at subambient temperatures during initial start up of each bed.
Claim 12
Dependent Claim
64 words
The process of claim 1, 2, 3, 4 or 5 wherein a portion of the oxygen from the desorption of one bed is used to purge the residual inert feed gas from the void volume of the other bed during the subsequent desorption of said other bed such that the residual inert feed gas is passed to another absorbent bed in the absorption step.
References Cited (Backward Citations)
US2450276A
Cited
US2523549A
Cited
US2874030A
Cited
US2810454A
Cited
US2909410A
Cited
US2944627A
Cited
US3055732A
Cited
US3237379A
Cited
US3176444A
Cited
US3323288A
Cited
US3361531A
Cited
US3430418A
Cited
US3636679A
Cited
US3960769A
Cited
US3969481A
Cited
US3980763A
Cited
US3996028A
Cited
US4026680A
Cited
US4025605A
Cited
US3986849A
Cited
US4032617A
Cited
US4011306A
Cited
US4077780A
Cited
US4203958A
Cited
US4234322A
Cited
US4239509A
Cited
US4194892A
Cited
US4299719A
Cited
US4366085A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1986-12-19 | 1987-06-20 | 1987-12-20 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-12-19 | 1991-06-20 | 1991-12-20 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-12-19 | 1995-06-20 | 1995-12-20 | $7700.00 | Window Closed / Lapsed |