US3980676A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for continuous production of propylene oxide
Assignee: Rhone Poulenc Industries SA
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Filing: 1975-03-07
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Granted: 1976-09-14
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Expires: 1995-03-07
Abstract
Abstract Propylene oxide is continuously produced by oxidation of propylene, and wherein the gaseous products of oxidation are washed with a neutral ester of phosphoric acid to prevent undesirable, competing side reactions.
Inventors
- 👤 Georges Biola
- 👤 Alain Fabre
- 👤 Gerard Schneider
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 22:19
CPC Classifications
C; C07; C07D; C07D301/00; C07D301/02; C07D301/03; C07D301/04; C07D301/06; C07D301/32
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
73 words
The method for the preparation of propylene oxide, which method comprises oxidizing propylene in liquid phase with molecular oxygen or an oxygen containing gas and thence washing the gaseous stream of said reaction with a neutral ester of phosphoric acid at a temperature below the degradation temperature of said ester whereby a greater portion of the oxidation products, propylene and solvent in said gaseous stream is absorbed by said ester of phosphoric acid.
Claim 2
Independent Claim
73 words
The method for the preparation of propylene oxide, which method comprises oxidizing propylene in liquid phase with molecular oxygen or an oxygen containing gas and thence washing the gaseous stream of said reaction with a neutral ester of phosphoric acid at a temperature below the degradation temperature of said ester whereby a greater portion of the oxidation products, propylene and solvent in said gaseous stream is absorbed by said ester of phosphoric acid.
Claim 3
Dependent Claim
27 words
The method as defined by claim 1, further comprising recycling said gaseous products not absorbed by said neutral ester of phosphoric acid to the propylene oxidation zone.
Claim 4
Dependent Claim
28 words
The method as defined by claim 3, wherein said gaseous products are recycled to said propylene oxidation zone through an oxygen containing gas stream feeding said oxidation zone.
Claim 5
Dependent Claim
68 words
The method as defined by claim 1, wherein the neutral ester of phosphoric acid exhibits the structural formula: ##EQU2## wherein R 1 , R 2 and R 3 may be the same or different and are independently selected from the group consisting of lower alkyl having from 1 to 8 carbon atoms, phenyl and phenyl alkyl with one or two alkyl groups having 1 to 3 carbon atoms.
Claim 6
Dependent Claim
17 words
The method as defined by claim 4, wherein the neutral ester of phosphoric acid is tri-n-butyl phosphate.
Claim 7
Dependent Claim
18 words
The method as defined by claim 1, further comprising feeding propylene at the head of said washing system.
Claim 8
Dependent Claim
16 words
The method as defined by claim 1, wherein the solvent of reaction is an aromatic halocarbon.
References Cited (Backward Citations)
US3238229A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-09-14 | 1980-03-15 | 1980-09-14 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-09-14 | 1984-03-15 | 1984-09-14 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-09-14 | 1988-03-15 | 1988-09-14 | $7700.00 | Window Closed / Lapsed |