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US5261947A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the production of a gas having a substantial oxygen content

Assignee: LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
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Filing: 1992-10-16
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Granted: 1993-11-16
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Expires: 2012-10-16
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Abstract

Abstract The selective adsorption of nitrogen from air is used in a system including a number of adsorbers, to give oxygen enriched gas at elevated pressure, the adsorber is regenerated by depressurization under atmospheric pressure with a pump and by repressurization with oxygen enriched gas. The pumping duration is at most equal to the duration of the production step.

Inventors

  • 👤 Leon Hay
  • 👤 Sylvie Eteve

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 07:03
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/02; B01D53/04; B01D53/047; B01D53/0476; B01D53/0473; C; C01; C01B; C01B13/00; C01B13/02; C01B13/0229; C01B13/0248; C01B13/0259; B01D2253/00; B01D2253/30; B01D2253/302; B01D2253/304; B01D2256/00; B01D2256/12; B01D2257/00; B01D2257/10; B01D2257/102; B01D2259/00; B01D2259/40; B01D2259/40011; B01D2259/40013; B01D2259/40015; B01D2259/40028; B01D2259/4003; B01D2259/40032; B01D2259/40043; B01D2259/4005; B01D2259/40052; B01D2259/40077; B01D2259/40081; B01D2259/403; B01D2259/404; B01D2259/406; B01D2259/4061; B01D2259/4062; C01B2210/00; C01B2210/0043; C01B2210/0046

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 304 words
Process for the production of a gas with substantial oxygen content at a flow higher than 60 T/day by adsorption of nitrogen present in the air, of the type where, in a plurality of n adsorbers, there is successively provided, cyclically according to a period T, on each of said adsorbers, with dephasing T/n from one adsorber to the following one: a) a step of co-current production of oxygen, having a duration x, at a pressure at least equal to atmospheric pressure, with introduction of air at least during a substantial portion of said production step; b) a step of depressurization, comprising at least in the last part thereof, a counter-current depressurization until reaching a sub-atmospheric pressure obtained by pumping; said pumping being followed, optionally, by a flushing-elution through counter-current flow of oxygen enriched gas; the minimum cycle pressure reached during said pumping step being P m ; c) a step of repressurization comprising at least a phase of counter-current repressurization with oxygen enriched gas characterized by the combination of the following steps: d) the number of adsorbers is at least 3 and the number of adsorbers in simultaneous production is at least 2; e) the duration of the production step is longer than dephasing T/n; f) the sum of the durations of counter-current depressurization and the optional flushing-elution is at most equal to the duration of the production step; and g) the step of pumping according to b) is carried out by means of "k" systems of pumping (k≧1), each being adapted to a level of partial depressurization and exerting its action successively on a same adsorber during a pumping of duration y, so that ##EQU2## with "k" lower by at least one unit than the maximum number of adsorbers in simultaneous production during at least a fraction of the time interval T/n.
Claim 2
Dependent Claim 304 words
Process for the production of a gas with substantial oxygen content at a flow higher than 60 T/day by adsorption of nitrogen present in the air, of the type where, in a plurality of n adsorbers, there is successively provided, cyclically according to a period T, on each of said adsorbers, with dephasing T/n from one adsorber to the following one: a) a step of co-current production of oxygen, having a duration x, at a pressure at least equal to atmospheric pressure, with introduction of air at least during a substantial portion of said production step; b) a step of depressurization, comprising at least in the last part thereof, a counter-current depressurization until reaching a sub-atmospheric pressure obtained by pumping; said pumping being followed, optionally, by a flushing-elution through counter-current flow of oxygen enriched gas; the minimum cycle pressure reached during said pumping step being P m ; c) a step of repressurization comprising at least a phase of counter-current repressurization with oxygen enriched gas characterized by the combination of the following steps: d) the number of adsorbers is at least 3 and the number of adsorbers in simultaneous production is at least 2; e) the duration of the production step is longer than dephasing T/n; f) the sum of the durations of counter-current depressurization and the optional flushing-elution is at most equal to the duration of the production step; and g) the step of pumping according to b) is carried out by means of "k" systems of pumping (k≧1), each being adapted to a level of partial depressurization and exerting its action successively on a same adsorber during a pumping of duration y, so that ##EQU2## with "k" lower by at least one unit than the maximum number of adsorbers in simultaneous production during at least a fraction of the time interval T/n.
Claim 3
Dependent Claim 44 words
Process for the production of oxygen according to claim 1, wherein there is provided h) a co-current depressurization between the production step and the step of counter-current depressurization, so as to provide a flushing gas for the flushing-elution, according to b) of another adsorber.
Claim 4
Dependent Claim 42 words
Process for the production of oxygen according to claim 1, wherein there is provided i) a co-current depressurization between the step of production and the step of counter-current depressurization so as to provide a partial repressurization gas for the repressurization step c).
Claim 5
Dependent Claim 25 words
Process for the production of oxygen according to claim 1, wherein the oxygen enriched gas of step b) and/or step c) consists of production oxygen.
Claim 6
Dependent Claim 26 words
Process for the production of oxygen according to claim 1, wherein the phase of counter-current repressurization of repressurization step c) is carried out with production gas.
Claim 7
Dependent Claim 24 words
Process for the production of oxygen according to claim 1, wherein the production step is carried out at least in part at maximum pressure.
Claim 8
Dependent Claim 24 words
Process for the production of oxygen according to claim 1, wherein the production step is carried out at least in part at increasing pressure.
Claim 9
Dependent Claim 26 words
Process for the production of oxygen according to claim 1, wherein the step of repressurization c) includes at least one phase of co-current repressurization with air.
Claim 10
Dependent Claim 38 words
Process for the production of oxygen according to claim 1, wherein the maximum cycle pressure P M is between atmospheric pressure and 1.6×10 5 Pascal, while the minimum cycle pressure is between 0.2×10 5 and 0.5×10 5 Pascal.
Claim 11
Dependent Claim 36 words
Process for the production of a gas having a substantial content of oxygen, according to claim 1, wherein the duration of pumping according to b) is between 20% and 40% of the duration of cycle T.
Claim 12
Dependent Claim 50 words
Process for the production of oxygen according to claim 3, wherein there is a first provided the depressurization according to i) then a co-current depressurization between the production step and the step of counter-current depressurization, so as to provide a flushing gas for the flushing-elution step b) of another adsorber.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1996-11-15 1997-05-17 1997-11-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 2000-11-15 2001-05-17 2001-11-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2004-11-15 2005-05-17 2005-11-16 $7700.00 Window Closed / Lapsed

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