US4409421A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the preparation of pure tert.-olefins
Assignee: Bayer AG
•
Filing: 1982-06-04
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Granted: 1983-10-11
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Expires: 2002-06-04
Abstract
Abstract Pure tert.-olefins are prepared from mixtures of hydrocarbons, which contain at least one such tert.-olefin, by reaction with an alkanol to give the corresponding alkyl tert.-alkyl ethers, and subsequent cleavage of these ethers back to the corresponding pure tert.-olefins and the alkanol, and the separation of the pure tert.-olefin from the alkanol. For this, the alkanol present after the cleavage of the ether is separated from the tert.-olefin to the extent of 60 to 99% by weight by distillation, and the residual amount of alcohol in the olefin fraction is removed by adsorption from this fraction onto a synthetic ion exchanger as an absorber resin. The admixture of the alkanol to the mixture of hydrocarbons with at least one tert.-olefin is carried out partly by using the alkanol fraction arising from the separating off of the pure tert.-olefin, and partly by desorption of the alkanol from the absorber resin with the aid of the mixture of hydrocarbons containing at least 1 tert.-olefin.
Inventors
- 👤 Jens Herwig
- 👤 Bruno Schulwitz
- 👤 Bernhard Schleppinghoff
- 👤 Hans-Volker Scheef
- 👤 Peter M. Lange
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 05:20
CPC Classifications
C; C07; C07C; C07C41/00; C07C41/01; C07C41/05; C07C41/06; C07C7/00; C07C7/12; C07C7/148; C07C7/14875; C07C7/14891
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
235 words
In a process for the preparation of a pure tertiary olefin comprising the steps of: (A) contacting at least one tertiary olefin in a hydrocarbon stream within which it is in admixture with other hydrocarbons with an alkanol whereby to form an alkyl tertiary alkyl ether; (B) separating off the residual hydrocarbons which are largely free of tertiary olefins from said alkyl tertiary alkyl ether; (C) cleaving said alkyl tertiary alkyl ether back to said tertiary olefin and alkanol; and (D) separating pure tertiary olefin from alkanol, the improvement wherein: (E) said alkanol, at the cleavage from said tertiary alkyl ether, is separated off by distilling off from said tertiary olefin to the extent of 60 to 99% by weight; (F) residual alkanol in admixture with said tertiary olefin is separated from said tertiary olefin by passing the mixture of residual alkanol and tertiary olefin over a synthetic ion exchanger which contains groups which exchange cations or anions or a mixture thereof whereby said alkanol becomes absorbed on said synthetic ion exchanger and substantially pure tertiary olefin is removed; and thereafter absorbed alkanol on said synthetic ion exchanger is desorbed by contacting said synthetic ion exchanger containing absorbed alkanol with a mixture of hydrocarbons containing at least one tertiary olefin; and (G) reacting said desorbed alkanol from step (F), while in admixture with at least one tertiary olefin to form said alkyl tertiary alkyl ether.
Claim 2
Dependent Claim
235 words
In a process for the preparation of a pure tertiary olefin comprising the steps of: (A) contacting at least one tertiary olefin in a hydrocarbon stream within which it is in admixture with other hydrocarbons with an alkanol whereby to form an alkyl tertiary alkyl ether; (B) separating off the residual hydrocarbons which are largely free of tertiary olefins from said alkyl tertiary alkyl ether; (C) cleaving said alkyl tertiary alkyl ether back to said tertiary olefin and alkanol; and (D) separating pure tertiary olefin from alkanol, the improvement wherein: (E) said alkanol, at the cleavage from said tertiary alkyl ether, is separated off by distilling off from said tertiary olefin to the extent of 60 to 99% by weight; (F) residual alkanol in admixture with said tertiary olefin is separated from said tertiary olefin by passing the mixture of residual alkanol and tertiary olefin over a synthetic ion exchanger which contains groups which exchange cations or anions or a mixture thereof whereby said alkanol becomes absorbed on said synthetic ion exchanger and substantially pure tertiary olefin is removed; and thereafter absorbed alkanol on said synthetic ion exchanger is desorbed by contacting said synthetic ion exchanger containing absorbed alkanol with a mixture of hydrocarbons containing at least one tertiary olefin; and (G) reacting said desorbed alkanol from step (F), while in admixture with at least one tertiary olefin to form said alkyl tertiary alkyl ether.
Claim 3
Dependent Claim
27 words
A process according to claim 1, wherein said synthetic ion exchanger is an ion exchanger with the matrix composed of styrene/divinylbenzene, phenol/formaldehyde, (meth)acrylic acid (derivative)/divinylbenzene or epichlorohydrin/polyamine.
Claim 4
Dependent Claim
61 words
A process according to claim 1, wherein 0.8 to 5 mols of alkanol are reacted according to step (A) per mol of tertiary olefin or mixture of tertiary olefins, said alcohol comprising at least in part some of the alkanol desorbed by desorption with said mixture of hydrocarbons and alkanol removed from a mixture of alkanol and tertiary olefin by distillation.
Claim 5
Dependent Claim
22 words
A process according to claim 1, wherein said alkanol is absorbed at 0°-60° C. under a pressure of 0.2 to 20 bars.
Claim 6
Dependent Claim
28 words
A process according to claim 1, wherein alkanol desorption is carried out at a temperature of 0° to 100° C. at a pressure of 0.2 to 30 bars.
Claim 7
Dependent Claim
28 words
A process according to claim 4, wherein alkanol desorption is carried out at a temperature of 0° to 100° C. under a pressure of 0.2 to 30 bars.
Claim 8
Dependent Claim
27 words
A process according to claim 1, wherein the loading of the absorber layer is 0.1 to 100 kilograms of inlet stream per kilogram of absorber per hour.
References Cited (Backward Citations)
US3170000A
Cited
US3409691A
Cited
US3489808A
Cited
US3634535A
Cited
US3751507A
Cited
US3922217A
Cited
US4287379A
Cited
EP0022510A1
Cited
US4320232A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1986-10-10 | 1987-04-11 | 1987-10-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-10-10 | 1991-04-11 | 1991-10-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-10-10 | 1995-04-11 | 1995-10-11 | $7700.00 | Window Closed / Lapsed |