US4042633A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for preparing diisopropyl ether
Assignee: Petro Canada Inc
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Filing: 1976-06-07
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Granted: 1977-08-16
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Expires: 1996-06-07
Abstract
Abstract Diisopropyl ether is prepared from isopropanol in liquid phase in contact with particular Montmorillonite clay catalysts, optionally in the presence of added propylene. The process is operated in a continuous manner by continuously feeding liquid isopropanol, optionally with added propylene, into a reaction space where the feed contacts the catalyst at 120° to 250° C for an average contact time of 1 to 120 minutes. Pressure is maintained in the reactor to keep a liquid phase in contact with the solid catalyst. Effluent withdrawn continuously from the reaction space at the feed rate is separated by fractionation to recover diisopropyl ether.
Inventors
- 👤 Hanbury John Woods
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 10:20
CPC Classifications
C; C07; C07C; C07C41/00; C07C41/01; C07C41/05; C07C41/06; C07C41/09
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
103 words
A process for the preparation of diisopropyl ether which comprises continuously feeding isopropanol, and optionally propylene, in the liquid phase under pressure into a reactor in which the feed material comes into effective contact with a solid catalyst, continuously withdrawing a mixture of reaction products and unreacted isopropanol and propylene from the reactor, and recovering diisopropyl ether from the mixture, said solid catalyst comprising acidic, sulfuric acid treated, Montmorillonite clay containing sufficient residual acidity to impart a pH below 4 thereto, said reactor being heated to maintain a temperature in the reactor in the range from substantially 120° C. to substantially 250° C.
Claim 2
Dependent Claim
103 words
A process for the preparation of diisopropyl ether which comprises continuously feeding isopropanol, and optionally propylene, in the liquid phase under pressure into a reactor in which the feed material comes into effective contact with a solid catalyst, continuously withdrawing a mixture of reaction products and unreacted isopropanol and propylene from the reactor, and recovering diisopropyl ether from the mixture, said solid catalyst comprising acidic, sulfuric acid treated, Montmorillonite clay containing sufficient residual acidity to impart a pH below 4 thereto, said reactor being heated to maintain a temperature in the reactor in the range from substantially 120° C. to substantially 250° C.
Claim 3
Dependent Claim
109 words
A process for the preparation of diisopropyl ether which comprises continuously feeding isopropanol, and optionally propylene, in the liquid phase under pressure into an elongated reactor containing a solid catalyst, continuously withdrawing the resulting mixture of reaction products and unreacted isopropanol and propylene from the reactor at a point remote from the point of introduction of the reactants, and recovering diisopropyl ether from the mixture, said solid catalyst comprising acidic, sulfuric acid treated, Montmorillonite clay containing sufficient residual acidity to impart a pH below 4 thereto, and said reactor being heated to maintain a temperature in the reactor in the range from substantially 120° C. to substantially 250° C.
Claim 4
Dependent Claim
109 words
A process for the preparation of diisopropyl ether which comprises continuously feeding isopropanol, and optionally propylene, in the liquid phase under pressure into an elongated reactor containing a solid catalyst, continuously withdrawing the resulting mixture of reaction products and unreacted isopropanol and propylene from the reactor at a point remote from the point of introduction of the reactants, and recovering diisopropyl ether from the mixture, said solid catalyst comprising acidic, sulfuric acid treated, Montmorillonite clay containing sufficient residual acidity to impart a pH below 4 thereto, and said reactor being heated to maintain a temperature in the reactor in the range from substantially 120° C. to substantially 250° C.
Claim 5
Dependent Claim
28 words
A process as claimed in claim 1 in which the pressure in the reactor is maintained in the range from 500 to 1000 psig (35 to 69 atmospheres).
Claim 6
Dependent Claim
58 words
A process as claimed in claim 2, in which isopropanol alone is continuously fed into a tubular reactor containing finely divided Montmorillonite clay dispersed on inert carrier, at a liquid hourly space velocity in the range from 0.5 to 50, with the temperature of reaction in the reactor being maintained in the range from 175° to 225° C.
Claim 7
Dependent Claim
65 words
A process as claimed in claim 2 in which a mixture of isopropanol and propylene, in molar proportions up to substantially one mole propylene per mole of isopropanol, is fed to the reactor in liquid phase, at a liquid hourly space velocity in the range from 0.5 to 50 while the temperature in the reactor is maintained in the range from 175° to 225° C.
Claim 8
Dependent Claim
22 words
A process as claimed in claim 5 in which the liquid hourly space velocity is in the range from 5 to 25.
Claim 9
Dependent Claim
28 words
A process as claimed in claim 5 in which the pressure in the reactor is maintained in the range from 500 to 1600 psig (35 to 110 atmospheres).
References Cited (Backward Citations)
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US2148288A
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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) | 1980-08-15 | 1981-02-14 | 1981-08-16 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-08-15 | 1985-02-14 | 1985-08-16 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-08-15 | 1989-02-14 | 1989-08-16 | $7700.00 | Window Closed / Lapsed |