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US3881996A Expired / Lapsed US ⏱️ 0.0 years remaining

Recovery of propylene oxide by plural stage distillation

Assignee: Lyondell Chemical Technology LP
•
Filing: 1973-11-21
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Granted: 1975-05-06
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Expires: 1993-11-21
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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.

References Cited (Backward Citations)

US3251862A Cited
US3350421A Cited
US3350420A Cited
US3350419A Cited
US3350417A Cited
US3398062A Cited
US3351635A Cited
US3580819A Cited

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

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