Patent US4512778A successfully refreshed from Google Patents.
US4512778A
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Adsorption processes
Assignee: LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
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Filing: 1983-10-12
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Granted: 1985-04-23
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Expires: 2003-10-12
Abstract
Abstract The gas originating from the expansion during the stage (T 6 ) is directed into a buffer tank and each adsorber has an operating cycle delayed by 1/nth of the cycle period (T) with respect to a preceding one, and each production stage has a duration of (x/n)T, "n" being greater than or equal to 6, and "x" greater than or equal to 2, and each expansion stage at an intermediate pressure has a shorter duration than each elution stage.
Inventors
- 👤 Guy Simonet
- 👤 Leon Hay
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 08:45
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/02; B01D53/04; B01D53/047; B01D2259/00; B01D2259/40; B01D2259/40011; B01D2259/40028; B01D2259/4003; B01D2259/40035; B01D2259/40037; B01D2259/40041; B01D2259/40043; B01D2259/4005; B01D2259/40052; B01D2259/40058; B01D2259/40067; B01D2259/40071; B01D2259/40075; B01D2259/406; B01D2259/4062; B01D2259/4063; B01D2259/4065; B01D2259/4066
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
253 words
In an adsorption process utilising a plurality of adsorbers with the following successive operating stages: isobaric production at so-called high pressure in equidirectional flow on several adsorbers at the same time, at least one decompression in equidirectional flow by balancing with another adsorber which is in the course of recompression in contradirectional flow, decompression to intermediate pressure in equidirectional flow, final decompression to so-called low pressure in contradirectional flow, elution at the said low pressure in contradirectional flow, recompression in contradirectional flow by at least one balancing action, final recompression in contradirectional flow by derivation of a part of the production flow, the improvement which consists in that the gas originating from the said decompression to intermediate pressure is fed into a buffer tank and the gas used for elution is drawn from the said buffer tank, and in that each adsorber has an operating cycle delayed by 1/nth of a cycle period (T) with respect to a preceding one (n being the number of adsorbers), and in that each production stage has a duration of (x/n)T (x being the number of adsorbers in simultaneous production), with "n" greater than or equal to 6, and "x" greater than or equal to 2, and in that the time period to decompress each adsorber to an intermediate pressure is less than the time period to elute each adsorber, and in that the gas drawn from the buffer tank for elution of an adsorber is supplied to that buffer tank by at least two different adsorbers.
Claim 2
Dependent Claim
253 words
In an adsorption process utilising a plurality of adsorbers with the following successive operating stages: isobaric production at so-called high pressure in equidirectional flow on several adsorbers at the same time, at least one decompression in equidirectional flow by balancing with another adsorber which is in the course of recompression in contradirectional flow, decompression to intermediate pressure in equidirectional flow, final decompression to so-called low pressure in contradirectional flow, elution at the said low pressure in contradirectional flow, recompression in contradirectional flow by at least one balancing action, final recompression in contradirectional flow by derivation of a part of the production flow, the improvement which consists in that the gas originating from the said decompression to intermediate pressure is fed into a buffer tank and the gas used for elution is drawn from the said buffer tank, and in that each adsorber has an operating cycle delayed by 1/nth of a cycle period (T) with respect to a preceding one (n being the number of adsorbers), and in that each production stage has a duration of (x/n)T (x being the number of adsorbers in simultaneous production), with "n" greater than or equal to 6, and "x" greater than or equal to 2, and in that the time period to decompress each adsorber to an intermediate pressure is less than the time period to elute each adsorber, and in that the gas drawn from the buffer tank for elution of an adsorber is supplied to that buffer tank by at least two different adsorbers.
Claim 3
Dependent Claim
35 words
An adsorption process according to claim 1, wherein the ratio between the period of an elution stage and the period of a stage of decompression to an intermediate pressure is equal to at least 1.5.
Claim 4
Dependent Claim
12 words
An adsorption process according to claim 2, wherein said ratio is 2.
Claim 5
Dependent Claim
12 words
An adsorption process according to claim 2, wherein said ratio is 3.
Claim 6
Dependent Claim
30 words
An adsorption process according to claim 1, wherein the number n of adsorbers is one of the numerals six and seven and comprises a single decompression with a balancing action.
Claim 7
Dependent Claim
54 words
An adsorption process according to claim 1, wherein the number n of adsorbers is one of the numerals seven, eight and nine, and comprises two successive decompressions performed firstly with an adsorber which had already been exposed to a first balancing action, and then with another adsorber at the end of an elution stage.
Claim 8
Dependent Claim
26 words
An adsorption process according to claim 1, wherein the number n of adsorbers is nine and comprises three successive decompressions by balancing with three other adsorbers.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1988-04-22 | 1988-10-22 | 1989-04-23 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-04-22 | 1992-10-22 | 1993-04-23 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-04-22 | 1996-10-22 | 1997-04-23 | $7700.00 | Window Closed / Lapsed |