Patent US5540758A successfully refreshed from Google Patents.
US5540758A
Expired / Lapsed
US
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VSA adsorption process with feed/vacuum advance and provide purge
Assignee: Air Products and Chemicals Inc
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Filing: 1995-06-30
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Granted: 1996-07-30
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Expires: 2015-06-30
Abstract
Abstract A process for separating a feed gas mixture into a more strongly adsorbable component and a less strongly adsorbable component in a plurality of adsorbent beds containing an adsorbent selective for the more strongly adsorbable component using cocurrent depressurization to provide purge gas and pressurization by product end to product end pressure equalization between beds simultaneous with cocurrent ambient and elevated pressure feed pressurization, and countercurrent evacuation. Oxygen product can be recovered from air at high recovery and adsorbent productivity levels using the process.
Inventors
- 👤 Rakesh Agrawal
- 👤 Ravi Kumar
- 👤 Tarik Naheiri
- 👤 Charles F. Watson
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 15:22
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/02; B01D53/04; B01D53/047; B01D53/0476; B01D2256/00; B01D2256/12; B01D2257/00; B01D2257/10; B01D2257/102; B01D2259/00; B01D2259/40; B01D2259/402; B01D53/0407; B01D53/0446
Claims Analysis
Total Claims: 19
Claim 1
Independent Claim
358 words
A process for selectively separating a more strongly adsorbable component from a less strongly adsorbable component of a feed gas mixture in a plurality of adsorption beds containing an adsorbent selective for the more strongly adsorbable component, comprising the steps of: (a) introducing a feed gas mixture at elevated pressure containing said more strongly adsorbable component and said less strongly adsorbable component into an inlet of a first adsorption bed containing said adsorbent selective for the more strongly adsorbable component and adsorbing the more strongly adsorbable component on the adsorbent while the less strongly adsorbable component passes through said first bed unadsorbed as a product and continuing until the adsorption front of said more strongly adsorbable component approaches an outlet of said first bed and terminating the introduction of said feed gas mixture; (b) cocurrently depressurizing said first bed to an intermediate pressure to remove a cocurrent depressurization gas from said first bed and passing said cocurrent depressurization gas to an outlet of a bed undergoing purging of step (e); (c) further cocurrently depressurizing said first bed to a lower pressure to remove additional cocurrent depressurization gas from said first bed and passing said additional cocurrent depressurization gas to an outlet of a bed of said plurality of adsorption beds at lower pressure undergoing repressurizing of step (f) to at least partially pressure equalize the two beds, while countercurrently depressurizing said first bed by connection to a source of vacuum; (d) countercurrently evacuating said first bed under vacuum conditions to remove said more strongly adsorbable component; (e) countercurrently purging said first bed with said cocurrent depressurization gas from a bed of said plurality of adsorption beds undergoing step (b) to remove additional more strongly adsorbable component from said first bed; (f) repressurizing said first bed with ambient pressure feed gas mixture, elevated pressure feed gas mixture and said cocurrent depressurization gas from a bed of said plurality of adsorption beds undergoing the cocurrent depressurization of step (c); (g) further repressurizing said first bed with elevated pressure feed gas mixture; and (h) performing steps (a) through (g) in each of said plurality of adsorption beds in a phased sequence.
Claim 2
Dependent Claim
358 words
A process for selectively separating a more strongly adsorbable component from a less strongly adsorbable component of a feed gas mixture in a plurality of adsorption beds containing an adsorbent selective for the more strongly adsorbable component, comprising the steps of: (a) introducing a feed gas mixture at elevated pressure containing said more strongly adsorbable component and said less strongly adsorbable component into an inlet of a first adsorption bed containing said adsorbent selective for the more strongly adsorbable component and adsorbing the more strongly adsorbable component on the adsorbent while the less strongly adsorbable component passes through said first bed unadsorbed as a product and continuing until the adsorption front of said more strongly adsorbable component approaches an outlet of said first bed and terminating the introduction of said feed gas mixture; (b) cocurrently depressurizing said first bed to an intermediate pressure to remove a cocurrent depressurization gas from said first bed and passing said cocurrent depressurization gas to an outlet of a bed undergoing purging of step (e); (c) further cocurrently depressurizing said first bed to a lower pressure to remove additional cocurrent depressurization gas from said first bed and passing said additional cocurrent depressurization gas to an outlet of a bed of said plurality of adsorption beds at lower pressure undergoing repressurizing of step (f) to at least partially pressure equalize the two beds, while countercurrently depressurizing said first bed by connection to a source of vacuum; (d) countercurrently evacuating said first bed under vacuum conditions to remove said more strongly adsorbable component; (e) countercurrently purging said first bed with said cocurrent depressurization gas from a bed of said plurality of adsorption beds undergoing step (b) to remove additional more strongly adsorbable component from said first bed; (f) repressurizing said first bed with ambient pressure feed gas mixture, elevated pressure feed gas mixture and said cocurrent depressurization gas from a bed of said plurality of adsorption beds undergoing the cocurrent depressurization of step (c); (g) further repressurizing said first bed with elevated pressure feed gas mixture; and (h) performing steps (a) through (g) in each of said plurality of adsorption beds in a phased sequence.
Claim 3
Dependent Claim
25 words
The process of claim 1 wherein said bed is repressurized in step (g) with ambient pressure feed gas mixture and elevated pressure feed gas mixture.
Claim 4
Dependent Claim
25 words
The process of claim 1 wherein said bed is repressurized in step (g) initially with feed gas mixture and then with less strongly adsorbable component.
Claim 5
Dependent Claim
25 words
The process of claim 1 wherein said bed is repressurized in step (g) initially with less strongly adsorbable component and then with feed gas mixture.
Claim 6
Dependent Claim
23 words
The process of claim 1 wherein said bed is repressurized in step (g) with less strongly adsorbable component and feed gas mixture simultaneously.
Claim 7
Dependent Claim
27 words
The process of claim 1 wherein said feed gas mixture is air, said more strongly adsorbable component is nitrogen and said less strongly adsorbable component is oxygen.
Claim 8
Dependent Claim
14 words
The process of claim 1 wherein the process is carried out in two beds.
Claim 9
Dependent Claim
17 words
The process of claim 1 wherein the pressure equalization of step (c) is a complete pressure equalization.
Claim 10
Dependent Claim
288 words
A process for selectively separating nitrogen from oxygen in air in two adsorption beds containing an adsorbent selective for nitrogen, comprising the steps of: (a) introducing feed air at elevated pressure into an inlet of a first adsorption bed containing said adsorbent selective for nitrogen and adsorbing nitrogen on the adsorbent while oxygen passes through said first bed unadsorbed as a product until the adsorption front of nitrogen approaches an outlet of said first bed and terminating the introduction of air into said first bed; (b) cocurrently depressurizing said first bed to remove a cocurrent depressurization gas consisting mainly of oxygen from said first bed and passing said cocurrent depressurization gas to an outlet of said second bed at lower pressure undergoing said purging of step (e); (c) further cocurrently depressurizing said first bed to remove additional cocurrent depressurization gas from said first bed and passing said additional cocurrent depressurization gas to an outlet of said second bed at said lower pressure undergoing repressurizing of step (f) to at least partially pressure equalize said first bed and said second bed, while countercurrently depressurizing said first bed by connection to a source of vacuum; (d) countercurrently evacuating said first bed under vacuum conditions to remove nitrogen; (e) countercurrently purging said first bed with oxygen from said second bed undergoing step (b) to remove additional nitrogen from said first bed; (f) repressurizing said first bed with ambient pressure air, elevated pressure feed air and cocurrent depressurization gas from said second bed at higher pressure undergoing the cocurrent depressurization of step (c); (g) further repressurizing said first bed with elevated pressure feed air; and (h) performing steps (a) through (g) in each of said two adsorption beds in a phased sequence.
Claim 11
Dependent Claim
288 words
A process for selectively separating nitrogen from oxygen in air in two adsorption beds containing an adsorbent selective for nitrogen, comprising the steps of: (a) introducing feed air at elevated pressure into an inlet of a first adsorption bed containing said adsorbent selective for nitrogen and adsorbing nitrogen on the adsorbent while oxygen passes through said first bed unadsorbed as a product until the adsorption front of nitrogen approaches an outlet of said first bed and terminating the introduction of air into said first bed; (b) cocurrently depressurizing said first bed to remove a cocurrent depressurization gas consisting mainly of oxygen from said first bed and passing said cocurrent depressurization gas to an outlet of said second bed at lower pressure undergoing said purging of step (e); (c) further cocurrently depressurizing said first bed to remove additional cocurrent depressurization gas from said first bed and passing said additional cocurrent depressurization gas to an outlet of said second bed at said lower pressure undergoing repressurizing of step (f) to at least partially pressure equalize said first bed and said second bed, while countercurrently depressurizing said first bed by connection to a source of vacuum; (d) countercurrently evacuating said first bed under vacuum conditions to remove nitrogen; (e) countercurrently purging said first bed with oxygen from said second bed undergoing step (b) to remove additional nitrogen from said first bed; (f) repressurizing said first bed with ambient pressure air, elevated pressure feed air and cocurrent depressurization gas from said second bed at higher pressure undergoing the cocurrent depressurization of step (c); (g) further repressurizing said first bed with elevated pressure feed air; and (h) performing steps (a) through (g) in each of said two adsorption beds in a phased sequence.
Claim 12
Dependent Claim
22 words
The process of claim 9 wherein said bed is repressurized in step (g) with ambient pressure air and elevated pressure feed air.
Claim 13
Dependent Claim
24 words
The process of claim 9 wherein said first bed is repressurized in step (g) initially with elevated pressure feed air and then with oxygen.
Claim 14
Dependent Claim
24 words
The process of claim 9 wherein said first bed is repressurized in step (g) initially with oxygen and then with elevated pressure feed air.
Claim 15
Dependent Claim
21 words
The process of claim 9 wherein said bed is repressurized in step (g) with oxygen and elevated pressure feed air simultaneously.
Claim 16
Dependent Claim
22 words
The process of claim 9 wherein said elevated pressure feed air is at a pressure in the range of approximately 15-30 psia.
Claim 17
Dependent Claim
22 words
The process of claim 9 wherein said elevated pressure feed air is at a pressure in the range of approximately 15-24 psia.
Claim 18
Dependent Claim
29 words
The process of claim 9 wherein at the end of said countercurrent evacuation of step (d) said bed is at a pressure in the range of approximately 1-10 psia.
Claim 19
Dependent Claim
14 words
The process of claim 9 wherein the pressure equalization of step (c) is complete.
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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) | 1999-07-30 | 2000-01-29 | 2000-07-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2003-07-30 | 2004-01-29 | 2004-07-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2007-07-30 | 2008-01-29 | 2008-07-30 | $7700.00 | Window Closed / Lapsed |