US4472178A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Adsorptive process for the removal of carbon dioxide from a gas
Assignee: Air Products and Chemicals Inc
•
Filing: 1983-07-05
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Granted: 1984-09-18
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Expires: 2003-07-05
Abstract
Abstract A process is set forth for the removal of carbon dioxide from air in an adsorption bed wherein the regeneration energy is reduced by the use of a heat recuperator and a purge sequence which avoids the removal of heat from the adsorption bed during regeneration.
Inventors
- 👤 Ravi Kumar
- 👤 Shivaji Sircar
- 👤 Wilbur C. Kratz
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 19:04
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/02; B01D53/04; B01D53/0462; B01D2253/00; B01D2253/10; B01D2253/104; B01D2253/106; B01D2253/108; B01D2257/00; B01D2257/50; B01D2257/504; B01D2257/80; B01D2259/00; B01D2259/40; B01D2259/40011; B01D2259/40035; B01D2259/40037; B01D2259/40043; B01D2259/4005; B01D2259/40052; B01D2259/40058; B01D2259/40062; B01D2259/40077; B01D2259/40081; B01D2259/40083; B01D2259/40086; B01D2259/40088; B01D2259/4009; B01D2259/402; B01D2259/416; B01D2259/65; B01D2259/655; B01D53/047; B01D53/26; B01D53/261; Y; Y02; Y02C; Y02C20/00; Y02C20/40
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
228 words
In a process for removing carbon dioxide from a gas stream in an adsorbent bed by temperature swing adsorption comprising flowing a water-depleted gas feed stream containing carbon dioxide through said bed to selectively adsorb carbon dioxide, the improvement comprising the steps of: (a) passing the carbon dioxide-depleted gas product of the adsorbent bed through a recuperator to retain heat from said adsorbent bed; (b) bypassing the flow of carbon dioxide-depleted gas product around said recuperator after the gas reaches a predetermined lower temperature level, but while continuing the adsorption; (c) discontinuing the flow of water-depleted feed gas through said bed when the gas product of said bed reaches a predetermined level of carbon dioxide; (d) reducing the pressure of the bed and initiating the purging of the bed countercurrently with a heated water and carbon dioxide-depleted purge gas, which is heated to an elevated temperature by externally supplied heat and heat recovered from said recuperator until a thermal zone exists in said bed; (e) continuing the purge of the adsorbent bed without externally supplied heat until the thermal zone in said bed is approximately at the feed end of the bed; (f) discontinuing the flow of purge gas, and (g) repressurizing the bed countercurrently with water and carbon dioxide-depleted gas until the bed reaches a preset pressure level such that the adsorption cycle can be initiated again.
Claim 2
Dependent Claim
228 words
In a process for removing carbon dioxide from a gas stream in an adsorbent bed by temperature swing adsorption comprising flowing a water-depleted gas feed stream containing carbon dioxide through said bed to selectively adsorb carbon dioxide, the improvement comprising the steps of: (a) passing the carbon dioxide-depleted gas product of the adsorbent bed through a recuperator to retain heat from said adsorbent bed; (b) bypassing the flow of carbon dioxide-depleted gas product around said recuperator after the gas reaches a predetermined lower temperature level, but while continuing the adsorption; (c) discontinuing the flow of water-depleted feed gas through said bed when the gas product of said bed reaches a predetermined level of carbon dioxide; (d) reducing the pressure of the bed and initiating the purging of the bed countercurrently with a heated water and carbon dioxide-depleted purge gas, which is heated to an elevated temperature by externally supplied heat and heat recovered from said recuperator until a thermal zone exists in said bed; (e) continuing the purge of the adsorbent bed without externally supplied heat until the thermal zone in said bed is approximately at the feed end of the bed; (f) discontinuing the flow of purge gas, and (g) repressurizing the bed countercurrently with water and carbon dioxide-depleted gas until the bed reaches a preset pressure level such that the adsorption cycle can be initiated again.
Claim 3
Dependent Claim
20 words
The process of claim 1 wherein the water-depleted feed gas stream is introduced into the adsorbent bed at 50-150 psia.
Claim 4
Dependent Claim
20 words
The process of claim 2 wherein the water-depleted feed gas stream is introduced into the adsorbent bed at 40°-150° F.
Claim 5
Dependent Claim
24 words
The process of claim 3 wherein the adsorption is discontinued when the gas product obtains a carbon dioxide level of up to 1 PPM.
Claim 6
Dependent Claim
34 words
The process of claim 1 wherein a plurality of adsorbent beds are utilized in which at least one bed is an adsorption mode while at least one other bed is in a regeneration mode.
Claim 7
Dependent Claim
22 words
The process of claim 5 wherein the water-depleted feed gas stream is delivered from a plurality of switching pressure swing adsorption beds.
Claim 8
Dependent Claim
13 words
The process of claim 6 wherein the water-depleted gas feed stream is air.
Claim 9
Dependent Claim
26 words
The process of claim 6 wherein the water and carbon dioxide-depleted gas product is supplied to an air separation system to recover oxygen and or nitrogen.
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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) | 1987-09-18 | 1988-03-19 | 1988-09-18 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-09-18 | 1992-03-19 | 1992-09-18 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-09-18 | 1996-03-19 | 1996-09-18 | $7700.00 | Window Closed / Lapsed |