US4450294A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for recovering oxygenated organic compounds from dilute aqueous solutions employing solid sorbent
Assignee: Millennium Petrochemicals Inc
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Filing: 1982-11-01
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Granted: 1984-05-22
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Expires: 2002-11-01
Abstract
Abstract An oxygenated organic compound, such as ethanol, is recovered from a dilute aqueous stream thereof by contacting said stream with crosslinked polyvinylpyridine resin or nuclear substituted derivative thereof to effect selective sorption of the compound by said resin. The sorbed compound is thereafter removed from the resin by stripping with an inert gas such as carbon dioxide.
Inventors
- 👤 Julian Feldman
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 20:06
CPC Classifications
C; C07; C07C; C07C29/00; C07C29/74; C07C29/76; C07C31/00; C07C31/02; C07C31/08
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
55 words
A process for recovering an oxygenated organic compound from a dilute aqueous solution thereof which comprises contacting said dilute aqueous solution with crosslinked polyvinylpyridine resin or nuclear substituted derivative thereof under such conditions that at least a portion of the compound will be sorbed by said resin and thereafter desorbing the compound from said resin.
Claim 2
Dependent Claim
55 words
A process for recovering an oxygenated organic compound from a dilute aqueous solution thereof which comprises contacting said dilute aqueous solution with crosslinked polyvinylpyridine resin or nuclear substituted derivative thereof under such conditions that at least a portion of the compound will be sorbed by said resin and thereafter desorbing the compound from said resin.
Claim 3
Dependent Claim
18 words
The process of claim 1 wherein the oxygenated organic compound comprises alcohols, aldehydes, ketones, ethers, acids and esters.
Claim 4
Dependent Claim
25 words
The process of claim 2 wherein the oxygenated organic compound is selected from the group consisting of acetone, acetic acid, butyric acid, n-propanol and n-butanol.
Claim 5
Dependent Claim
12 words
The process of claim 1 wherein the crosslinked polyvinylpyridine is crosslinked poly(4-vinylpyridine).
Claim 6
Dependent Claim
17 words
The process of claim 1 further comprising the step of desorbing the compound employing an inert gas.
Claim 7
Dependent Claim
12 words
The process of claim 5 wherein the inert gas is carbon dioxide.
Claim 8
Dependent Claim
26 words
The process of claim 1 wherein the process is carried out at elevated temperature thereby increasing relative adsorption of crosslinked polyvinylpyridine for the oxygenated organic compound.
Claim 9
Dependent Claim
12 words
The process of claim 7 wherein the crosslinked polyvinylpyridine is crosslinked poly(4-vinylpyridine).
Claim 10
Dependent Claim
136 words
A process for recovering an oxygenated organic compound from a fermentation vessel at a concentration which is higher than the concentration of the compound in the fermentation medium which comprises: (a) contacting the fermentation compound present in the dilute aqueous stream from the fermentation vessel with crosslinked polyvinylpyridine resin or nuclear substituted derivative thereof to sorb a percentage of the compound present in said stream; (b) employing the aqueous stream which has been contacted with the resin to adsorb compound present in the gaseous carbon dioxide stream produced in the fermentation vessel in an adsorption zone; (c) combining the dilute aqueous compound stream resulting from step (b) with the fermentation compound stream of step (a); and, (d) desorbing compound sorbed in step (a) with substantially compound-free carbon dioxide obtained from the adsorption zone of step (b).
Claim 11
Dependent Claim
136 words
A process for recovering an oxygenated organic compound from a fermentation vessel at a concentration which is higher than the concentration of the compound in the fermentation medium which comprises: (a) contacting the fermentation compound present in the dilute aqueous stream from the fermentation vessel with crosslinked polyvinylpyridine resin or nuclear substituted derivative thereof to sorb a percentage of the compound present in said stream; (b) employing the aqueous stream which has been contacted with the resin to adsorb compound present in the gaseous carbon dioxide stream produced in the fermentation vessel in an adsorption zone; (c) combining the dilute aqueous compound stream resulting from step (b) with the fermentation compound stream of step (a); and, (d) desorbing compound sorbed in step (a) with substantially compound-free carbon dioxide obtained from the adsorption zone of step (b).
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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) | 1987-05-22 | 1987-11-21 | 1988-05-22 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-05-22 | 1991-11-21 | 1992-05-22 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-05-22 | 1995-11-21 | 1996-05-22 | $7700.00 | Window Closed / Lapsed |