US4113780A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Extractive distillation of acetone
Assignee: Wintershall Dea International AG
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Filing: 1975-02-06
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Granted: 1978-09-12
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Expires: 1995-02-06
Abstract
Abstract Acetone containing less than 0.2 weight percent water is produced in an extractive distillation of acetone containing appreciable quantities of water by utilizing isopropyl alcohol as the extracting agent.
Inventors
- 👤 Gunter Strehlke
- 👤 Gunther Osterburg
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 09:02
CPC Classifications
C; C07; C07C; C07C45/00; C07C45/78; C07C45/81; C07C45/82; C07C45/83
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
172 words
A process for the production of low water content acetone from a feed comprising acetone and water, said feed having been distilled, if necessary, to remove C 6 and lighter volatile material therefrom, which comprises (a) introducing the feed into the top of the stripping section of a distillation column comprising a rectifying section and a stripping section under distillation conditions comprising a reflux ratio of 2:1 to 10:1 and a column top pressure of 0.5 to 2.0 atmospheres absolute, (b) introducing isopropyl alcohol, having a water content of 0.1 weight percent maximum, into the rectifying section intermediate the feed inlet and the column top whereby the water-containing acetone is subjected to extractive distillation by said isopropyl alcohol, said isopropyl alcohol addition being 5 to 15 volume percent of the column load, (c) recovering from the overhead from said column as the product therefrom acetone having a maximum water content of less than 0.2 weight percent, and (d) recovering from the bottoms from said column a product comprising isopropyl alcohol and water.
Claim 2
Dependent Claim
172 words
A process for the production of low water content acetone from a feed comprising acetone and water, said feed having been distilled, if necessary, to remove C 6 and lighter volatile material therefrom, which comprises (a) introducing the feed into the top of the stripping section of a distillation column comprising a rectifying section and a stripping section under distillation conditions comprising a reflux ratio of 2:1 to 10:1 and a column top pressure of 0.5 to 2.0 atmospheres absolute, (b) introducing isopropyl alcohol, having a water content of 0.1 weight percent maximum, into the rectifying section intermediate the feed inlet and the column top whereby the water-containing acetone is subjected to extractive distillation by said isopropyl alcohol, said isopropyl alcohol addition being 5 to 15 volume percent of the column load, (c) recovering from the overhead from said column as the product therefrom acetone having a maximum water content of less than 0.2 weight percent, and (d) recovering from the bottoms from said column a product comprising isopropyl alcohol and water.
Claim 3
Dependent Claim
21 words
A process according to claim 1 wherein the isopropyl alcohol of step (b) comprises the isopropyl alcohol recovered in step (d).
Claim 4
Dependent Claim
18 words
A process according to claim 1 wherein the isopropyl alcohol of step (b) comprises 0.1 weight percent water.
Claim 5
Dependent Claim
31 words
A process according to claim 1 wherein the isopropyl alcohol of step (b) comprises about 0.01 weight percent water and the acetone of step (c) comprises about 0.01 weight percent water.
Claim 6
Dependent Claim
35 words
A process according to claim 1 wherein the reflux ratio is about 4:1, the column top pressure is about 1.3 and the isopropyl alcohol of step (b) is about 10 volume percent of column load.
Claim 7
Dependent Claim
42 words
A process according to claim 1 wherein the feed is selected from the group consisting of acetone-containing reaction mixtures from acetone synthesis by dehydrogenation of isopropyl alcohol and acetone-containing reaction mixtures from methylisobutyl ketone synthesis from acetone by condensation, dehydration and hydrogenation.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-09-11 | 1982-03-13 | 1982-09-12 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-09-11 | 1986-03-13 | 1986-09-12 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-09-11 | 1990-03-13 | 1990-09-12 | $7700.00 | Window Closed / Lapsed |