US5354346A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Purge effluent repressurized adsorption process
Assignee: Air Products and Chemicals Inc
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Filing: 1992-10-01
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Granted: 1994-10-11
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Expires: 2012-10-01
Abstract
Abstract A pressure swing adsorption process is set forth for the recovery of two gas products at high recovery and high purity using the steps of adsorption, depressurization, low pressure purge, evacuation and repressurization. The purge effluent and a portion of the depressurization effluent are used to partially accomplish the repressurization step.
Inventors
- 👤 Ravi Kumar
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 17:07
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/02; B01D53/04; B01D53/047; B01D2253/00; B01D2253/10; B01D2253/102; B01D2253/104; B01D2253/106; B01D2253/108; B01D2259/00; B01D2259/40; B01D2259/40001; B01D2259/40011; B01D2259/40058; B01D2259/40066; B01D2259/40069; B01D2259/406; B01D2259/4061
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
371 words
In a pressure swing adsorption process for the recovery of two gas products at high recovery and high purity from a feed gas stream containing said products wherein a first gas product is one or more, less strongly adsorbed components and a second gas product is one or more, more strongly adsorbed components, and wherein said process comprises the steps of: (a) introducing a feed gas stream at elevated pressure containing said one or more, less strongly adsorbed components and said one or more, more strongly adsorbed components into one of a plurality of parallel adsorptive beds filled with one or more adsorbents selective for said one or more, more strongly adsorbed components, so as to retain said one or more, more strongly adsorbed components on said one or more adsorbents and allow said one or more, less strongly adsorbed components to pass through said bed for recovery as said first gas product at high recovery and high purity; (b) terminating the introduction of said feed gas stream into said bed before said one or more, more strongly adsorbed components break through the downstream end of said bed and depressurizing said bed to approximately ambient pressure to remove said one or more, less strongly adsorbed components from said bed and recycling at least a portion of the resulting depressurization effluent to said feed gas stream; (c) passing a low pressure purge gas stream of one or more, more strongly adsorbed components through said bed to remove any residual one or more, less strongly adsorbed components from said bed; (d) evacuating said bed to a subambient pressure to recover said one or more, more strongly adsorbed components as said second gas product at high recovery and high purity; and (e) repressurizing said bed with one or more, less strongly adsorbed components to approximately the pressure of the feed gas stream, wherein the steps (a) through (e) are performed on said plurality of beds to result in a continuous process; the improvement to increase the energy efficiency of the process comprising a purge effluent repressurization step wherein said bed is partially repressurized after step (d) and prior to step (e) with the effluent from one of said parallel beds presently undergoing step (c).
Claim 2
Dependent Claim
371 words
In a pressure swing adsorption process for the recovery of two gas products at high recovery and high purity from a feed gas stream containing said products wherein a first gas product is one or more, less strongly adsorbed components and a second gas product is one or more, more strongly adsorbed components, and wherein said process comprises the steps of: (a) introducing a feed gas stream at elevated pressure containing said one or more, less strongly adsorbed components and said one or more, more strongly adsorbed components into one of a plurality of parallel adsorptive beds filled with one or more adsorbents selective for said one or more, more strongly adsorbed components, so as to retain said one or more, more strongly adsorbed components on said one or more adsorbents and allow said one or more, less strongly adsorbed components to pass through said bed for recovery as said first gas product at high recovery and high purity; (b) terminating the introduction of said feed gas stream into said bed before said one or more, more strongly adsorbed components break through the downstream end of said bed and depressurizing said bed to approximately ambient pressure to remove said one or more, less strongly adsorbed components from said bed and recycling at least a portion of the resulting depressurization effluent to said feed gas stream; (c) passing a low pressure purge gas stream of one or more, more strongly adsorbed components through said bed to remove any residual one or more, less strongly adsorbed components from said bed; (d) evacuating said bed to a subambient pressure to recover said one or more, more strongly adsorbed components as said second gas product at high recovery and high purity; and (e) repressurizing said bed with one or more, less strongly adsorbed components to approximately the pressure of the feed gas stream, wherein the steps (a) through (e) are performed on said plurality of beds to result in a continuous process; the improvement to increase the energy efficiency of the process comprising a purge effluent repressurization step wherein said bed is partially repressurized after step (d) and prior to step (e) with the effluent from one of said parallel beds presently undergoing step (c).
Claim 3
Dependent Claim
49 words
The process of claim 1 wherein the improvement further comprises a depressurization effluent repressurization step wherein said bed is partially repressurized after step (d) and prior to the purge effluent repressurization step with a last portion of the effluent from one of said parallel beds presently undergoing step (b).
Claim 4
Dependent Claim
24 words
The process of claim 1 wherein the elevated pressure of said feed gas stream is in the range of approximately 30 to 500 psia.
Claim 5
Dependent Claim
18 words
The process of claim 1 wherein the depressurization is conducted down to a pressure of approximately 15 psia.
Claim 6
Dependent Claim
23 words
The process of claim 1 wherein the evacuation is conducted down to a pressure in the range of approximately 40 to 200 torr.
Claim 7
Dependent Claim
35 words
The process of claim 1 wherein said less strongly adsorbed components and said more strongly adsorbed components are selected from the group consisting of hydrogen, oxygen, carbon dioxide, nitrogen, carbon monoxide, methane, and other hydrocarbons.
Claim 8
Dependent Claim
21 words
The process of claim 1 wherein the adsorbent is selected from the group consisting of zeolites, carbons, aluminas and silica gels.
Claim 9
Dependent Claim
20 words
The process of claim 1 wherein the feed gas temperature is in the range of approximately 0° to 300° F.
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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) | 1997-10-10 | 1998-04-11 | 1998-10-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2001-10-10 | 2002-04-11 | 2002-10-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2005-10-10 | 2006-04-11 | 2006-10-11 | $7700.00 | Window Closed / Lapsed |