US4371380A
Expired / Lapsed
US
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Pressure swing adsorption process
Assignee: Linde GmbH
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Filing: 1980-04-24
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Granted: 1983-02-01
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Expires: 2000-04-24
Abstract
Abstract A pressure swing adsorption process conducted with plural cyclically reversible adsorbers, each of the adsorbers undergoing identical switching cycles. The switching cycles include sequentially at least one adsorption phase, at least two expansion phases, at least one desorption phase employing a purge gas which is foreign and inert relative to the material adsorbed in the adsorbent phase, a displacement phase employing a gas obtained from an expansion phase of one of the adsorbers to displace the purge gas, and at least one pressure build-up phase.
Inventors
- 👤 Christian Benkmann
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 18:27
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/02; B01D53/04; B01D53/047; B01D2253/00; B01D2253/10; B01D2253/106; B01D2256/00; B01D2256/12; B01D2256/14; B01D2256/16; B01D2257/00; B01D2257/10; B01D2257/104; B01D2257/50; B01D2257/504; B01D2257/80; B01D2259/00; B01D2259/40; B01D2259/40011; B01D2259/40028; B01D2259/4003; B01D2259/40035; B01D2259/40041; B01D2259/40043; B01D2259/4005; B01D2259/40056; B01D2259/40058; B01D2259/40067; B01D2259/40075; B01D2259/40077; B01D2259/40079; B01D2259/404; B01D2259/406; B01D2259/4066; B01D53/26; B01D53/261; Y; Y02; Y02C; Y02C20/00; Y02C20/40
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
86 words
In a pressure swing adsorption process for the purification or separation of gaseous mixtures, using plural, cyclically reversible adsorbers, each of which passes through identical switching cycles, wherein each switching cycle comprises sequentially at least one adsorption phase, two expansion phases, a desporption phase, and a pressure buildup phase, the improvement comprising effecting desorption by purging with a foreign gas, following the desorption with a displacement phase, and conducting the displacement of the foreign gas with a gas or gaseous mixture discharged during an expansion phase.
Claim 2
Dependent Claim
86 words
In a pressure swing adsorption process for the purification or separation of gaseous mixtures, using plural, cyclically reversible adsorbers, each of which passes through identical switching cycles, wherein each switching cycle comprises sequentially at least one adsorption phase, two expansion phases, a desporption phase, and a pressure buildup phase, the improvement comprising effecting desorption by purging with a foreign gas, following the desorption with a displacement phase, and conducting the displacement of the foreign gas with a gas or gaseous mixture discharged during an expansion phase.
Claim 3
Dependent Claim
28 words
A process according to claim 1, characterized in that the displacement is conducted with the aid of the gas or gaseous mixture discharged during the final expansion phase.
Claim 4
Dependent Claim
43 words
A process according to claim 1, or 2, characterized in that the pressure difference produced between the beginning and the end of the expansion phase coupled with the displacement phase is approximately equal to the pressure ambient at the end of the desorption.
Claim 5
Dependent Claim
74 words
A process to claim 3 comprising the separation of gaseous reaction products from a gaseous stream stemming from an oxygen-consumming reaction and still containing oxygen, the oxygen proportion of the gaseous stream to be recycled into the reaction, wherein the oxygen to be fed to the reaction is obtained by air fractionation and the nitrogen obtained during the course of the air fractionation is utilized as the foreign gas to support the desorption phase.
Claim 6
Dependent Claim
76 words
A process according to claims 1 or 2 for the separation of gaseous reaction products from a gaseous stream stemming from an oxygen-consuming reaction and still containing oxygen, the oxygen proportion of which gaseous stream is to be recycled into the reaction, wherein the oxygen to be fed to the reaction is obtained by air fractionation, and nitrogen obtained during the course of the air fractionation is utilized as the foreign gas to support the desorption.
Claim 7
Dependent Claim
41 words
A process according to claim 1 or 2 comprising the separation of hydrogen from a hydrogen enriched gaseous stream containing carbon dioxide and steam, and stream resulting from a partial oxidation of hydrocarbon-rich materials, and the foreign purge gas comprises nitrogen.
Claim 8
Dependent Claim
37 words
A process according to claim 1 or 2 wherein the components purged by the foreign purge gas in the desorption step are organic acids adsorbed from a gaseous stream resulting from biological oxidation of polysaccharides with oxygen.
Claim 9
Dependent Claim
23 words
A process according to claim 1 wherein said foreign gas comprises an inert gas of low adsorbability relative to the gaseous component adsorbed.
Claim 10
Dependent Claim
102 words
In a pressure swing adsorption process for the purification or separation of gaseous mixture, said process employing plural, cyclically reversible adsorbers, each adsorber passing through identical switching cycles with each cycle comprising sequentially at least one adsorption phase, two expansion phases, a desorption phase, and a pressure buildup phase, the improvement comprising the steps of purging each on adsorber during the desorption phase thereof with a foreign purge gas of low adsorbability relative to the gaseous component adsorbed, and displacing the foreign purge gas with a gas or gaseous mixture discharged during the expansion phase of another one of the plural adsorbers.
Claim 11
Dependent Claim
102 words
In a pressure swing adsorption process for the purification or separation of gaseous mixture, said process employing plural, cyclically reversible adsorbers, each adsorber passing through identical switching cycles with each cycle comprising sequentially at least one adsorption phase, two expansion phases, a desorption phase, and a pressure buildup phase, the improvement comprising the steps of purging each on adsorber during the desorption phase thereof with a foreign purge gas of low adsorbability relative to the gaseous component adsorbed, and displacing the foreign purge gas with a gas or gaseous mixture discharged during the expansion phase of another one of the plural 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) | 1986-01-31 | 1986-08-02 | 1987-02-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-01-31 | 1990-08-02 | 1991-02-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-01-31 | 1994-08-02 | 1995-02-01 | $7700.00 | Window Closed / Lapsed |