US3881996A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Recovery of propylene oxide by plural stage distillation
Assignee: Lyondell Chemical Technology LP
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Filing: 1973-11-21
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Granted: 1975-05-06
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Expires: 1993-11-21
Abstract
Abstract Propylene oxide is recovered from a substantially propylenefree, crude propylene oxide product obtained by catalytic oxidation of propylene with an organic hydroperoxide. The crude product is distilled to remove acetaldehyde as an overhead product. A bottoms product is then distilled to separate propylene oxide as an overhead product from propionaldehyde and other higher boiling materials.
Inventors
- 👤 John P Schmidt
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-23 22:51
CPC Classifications
C; C07; C07D; C07D301/00; C07D301/32
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
168 words
IN A PROCESS FOR RECOVERING PROPYLENE OXIDE IN A HIGH STATE OF PURITY FROM A CRUDE PROPYLENE OXIDE PRODUCT OBTAINED BY THE CATALYTIC EPOXIDATION OF PROPYLENE WITH AN OGANIC HYDROPEROXIDE, SAID PRODUCT INCLUDING PROPYLENE, PROPYLENE OXIDE, ACETALDEHYDE, PROPIONALDEHYDE AND OTHER MATERIAL HAVING A HIGHER BOILING POINT THAN THAT OF PROPYLENE OXIDE, THE IMPROVEMENT CONSISTING OF THE SEQUENTIAL STEPS OF A. REMOVING PROPYLENE BY DISTILLATION FROM SAID PRODUCT TO OBTAIN A SUBSTANTIALLY PROPYLENE-FREE CRUDE PROPYLENE OXIDE PRODUCT, FOLLOWED BY B. CHARGING THE SAID SUBSTANTIALLY PROPYLENE-FREE, CRUDE PROPYLENE OXIDE PRODUCT INTO A FIRST FRACTIONATOR, WITHDRAWING THEREFROM A FIRST DISTILLATION OVERHEAD CONTAINING ACETALDEHYDE, AND WITHDRAWING THEREFROM A FIRST DISTILLATION BOTTOMS CONTAINING PROPYLENE OXIDE, PROPIONALDEHYDE, AND SAID MATERIAL HAVING A HIGHER BOILING POINT THAT THAT OF PROPYLENE OXIDE, FOLLOWED BY C. CHARGING THE SAID FIRST DISTILLATION BOTTOMS TO A SECOND FRACTIONATOR, WITHDRAWING THEREFROM A SECOND DISSILATION OVERHEAD CONTAINING PROPYLENE OXIDE SUBSTANTIALLY FREE OF ALDEHYDES AND OF SAID HIGHER BOILING MATERIAL, AND WITHDRAWING THEREFROM A SECOND DISTILLATION BOTTOMS CONTAINING SAID HIGHER BOILING MATERIAL.
Claim 2
Dependent Claim
168 words
IN A PROCESS FOR RECOVERING PROPYLENE OXIDE IN A HIGH STATE OF PURITY FROM A CRUDE PROPYLENE OXIDE PRODUCT OBTAINED BY THE CATALYTIC EPOXIDATION OF PROPYLENE WITH AN OGANIC HYDROPEROXIDE, SAID PRODUCT INCLUDING PROPYLENE, PROPYLENE OXIDE, ACETALDEHYDE, PROPIONALDEHYDE AND OTHER MATERIAL HAVING A HIGHER BOILING POINT THAN THAT OF PROPYLENE OXIDE, THE IMPROVEMENT CONSISTING OF THE SEQUENTIAL STEPS OF A. REMOVING PROPYLENE BY DISTILLATION FROM SAID PRODUCT TO OBTAIN A SUBSTANTIALLY PROPYLENE-FREE CRUDE PROPYLENE OXIDE PRODUCT, FOLLOWED BY B. CHARGING THE SAID SUBSTANTIALLY PROPYLENE-FREE, CRUDE PROPYLENE OXIDE PRODUCT INTO A FIRST FRACTIONATOR, WITHDRAWING THEREFROM A FIRST DISTILLATION OVERHEAD CONTAINING ACETALDEHYDE, AND WITHDRAWING THEREFROM A FIRST DISTILLATION BOTTOMS CONTAINING PROPYLENE OXIDE, PROPIONALDEHYDE, AND SAID MATERIAL HAVING A HIGHER BOILING POINT THAT THAT OF PROPYLENE OXIDE, FOLLOWED BY C. CHARGING THE SAID FIRST DISTILLATION BOTTOMS TO A SECOND FRACTIONATOR, WITHDRAWING THEREFROM A SECOND DISSILATION OVERHEAD CONTAINING PROPYLENE OXIDE SUBSTANTIALLY FREE OF ALDEHYDES AND OF SAID HIGHER BOILING MATERIAL, AND WITHDRAWING THEREFROM A SECOND DISTILLATION BOTTOMS CONTAINING SAID HIGHER BOILING MATERIAL.
Claim 3
Dependent Claim
23 words
The process of claim 1, wherein said first fractionator is operated at a bottom zone temperature of from about 35*C. to about 100*C.
Claim 4
Dependent Claim
23 words
The process of claim 1, wherein said second fractionator is operated at a bottom zone temperature of from about 50*C. to about 100*C.
Claim 5
Dependent Claim
23 words
The process of claim 1, wherein said second fractionator is operated at a bottom zone temperature of from about 60*C. to about 90*C.
Claim 6
Dependent Claim
28 words
The process of claim 1, wherein said substantially propylene-free, crude propylene oxide product also contains water, which is withdrawn from said second fractionator in said second distillation bottoms.
Claim 7
Dependent Claim
12 words
The process of claim 1, wherein said organic hydroperoxide is ethylbenzene hydroperoxide.
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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) | 1978-05-05 | 1978-11-04 | 1979-05-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1982-05-05 | 1982-11-04 | 1983-05-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1986-05-05 | 1986-11-04 | 1987-05-06 | $7700.00 | Window Closed / Lapsed |