US4287379A
Expired / Lapsed
US
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Process for obtaining isobutene from C4 -hydrocarbon mixtures containing isobutene
Assignee: BASF SE
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Filing: 1980-04-07
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Granted: 1981-09-01
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Expires: 2000-04-07
Abstract
Abstract A process for obtaining isobutene from a C 4 -hydrocarbon mixture containing isobutene, by reacting the mixture with a primary alcohol in the presence of an acid condensing agent and decomposing the resulting tertiary ether in the presence of an acid catalyst at an elevated temperature, wherein a primary C 3 - or C 4 -alcohol is used.
Inventors
- 👤 Erwin Brunner
- 👤 Eckart Schubert
- 👤 Alfred Lindner
- 👤 Franz Merger
- 👤 Klaus Volkamer
- 👤 Max Strohmeyer
- 👤 Gerhard Sandrock
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 15:33
CPC Classifications
C; C07; C07C; C07C41/00; C07C41/01; C07C41/34; C07C41/40; C07C41/42; C07C11/00; C07C11/02; C07C11/08; C07C11/09; C07C41/05; C07C41/06; C07C7/00; C07C7/148; C07C7/14875; C07C7/14891
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
321 words
A process for obtaining isobutene from a C 4 -hydrocarbon mixture containing isobutene, which comprises (a) reacting the mixture with a primary C 3 - or C 4 -alcohol in the presence of an ion exchanger in its acid form as a condensing agent to form the corresponding C 3 - or C 4 -alkyl tert-butyl ether by feeding the primary C 3 - or C 4 -alcohol and the C 4 -hydrocarbon mixture, with or without prior mixing, to an etherification reaction zone which contains the ion exchanger; (b) distilling the reaction mixture obtained from the etherification reaction zone in a first distillation zone, taking off as the top product without water washing a C 4 -hydrocarbon mixture comprising the unconverted hydrocarbons and not more than 1,000 ppm by weight of the primary C 3 - or C 4 -alcohol and taking off as the bottom product the resulting C 3 - or C 4 -alkyl tert-butyl ether, which may contain therein primary C 3 - or C 4 -alcohol which may have been added in excess; (c) feeding the bottom product to a second reaction zone, containing an acid catalyst, in which the C 3 - or C 4 -alkyl tert-butyl ether is decomposed at an elevated temperature to give isobutene and primary C 3 - and C 4 -alcohol; (d) feeding the mixture of isobutene and primary C 3 - and C 4 -alcohol produced in step (c) to a second distillation zone, taking off as the top product without a water wash isobutene containing not more than 500 ppm by weight of primary C 3 - or C 4 -alcohol and taking off as the bottom product the remaining primary C 3 - or C 4 - alcohol produced in step (c); and (e) Recycling the primary C 3 - or C 4 -alcohol which is the bottom product of step (d) to the etherification reaction zone.
Claim 2
Dependent Claim
321 words
A process for obtaining isobutene from a C 4 -hydrocarbon mixture containing isobutene, which comprises (a) reacting the mixture with a primary C 3 - or C 4 -alcohol in the presence of an ion exchanger in its acid form as a condensing agent to form the corresponding C 3 - or C 4 -alkyl tert-butyl ether by feeding the primary C 3 - or C 4 -alcohol and the C 4 -hydrocarbon mixture, with or without prior mixing, to an etherification reaction zone which contains the ion exchanger; (b) distilling the reaction mixture obtained from the etherification reaction zone in a first distillation zone, taking off as the top product without water washing a C 4 -hydrocarbon mixture comprising the unconverted hydrocarbons and not more than 1,000 ppm by weight of the primary C 3 - or C 4 -alcohol and taking off as the bottom product the resulting C 3 - or C 4 -alkyl tert-butyl ether, which may contain therein primary C 3 - or C 4 -alcohol which may have been added in excess; (c) feeding the bottom product to a second reaction zone, containing an acid catalyst, in which the C 3 - or C 4 -alkyl tert-butyl ether is decomposed at an elevated temperature to give isobutene and primary C 3 - and C 4 -alcohol; (d) feeding the mixture of isobutene and primary C 3 - and C 4 -alcohol produced in step (c) to a second distillation zone, taking off as the top product without a water wash isobutene containing not more than 500 ppm by weight of primary C 3 - or C 4 -alcohol and taking off as the bottom product the remaining primary C 3 - or C 4 - alcohol produced in step (c); and (e) Recycling the primary C 3 - or C 4 -alcohol which is the bottom product of step (d) to the etherification reaction zone.
Claim 3
Dependent Claim
24 words
The process of claim 1, wherein the exit temperature of the reaction mixture from the etherification reaction zone is from 25° to 65° C.
Claim 4
Dependent Claim
43 words
The process of claim 1 or 2, wherein the isobutene contained in the C 4 - hydrocarbon mixture is converted to the extent of not less than 90% to the C 3 - or C 4 -alkyl tert-butyl ether in the etherification reaction.
Claim 5
Dependent Claim
51 words
The process of claim 3 wherein the etherification reaction is carried out continuously and the quotient of the volume of the etherification reaction zone and the throughput of the C 4 -hydrocarbon mixture, containing isobutene, and the primary C 3 - or C 4 -alcohol is from 0.01 to 5 hours.
Claim 6
Dependent Claim
57 words
The process of claim 3 wherein the top product taken off the first distillation zone is a C 4 -hydrocarbon mixture, comprising the unconverted hydrocarbons and containing not more than 200 ppm by weight of C 3 - or C 4 -alkyl tert-butyl ether or di-C 3 -alkyl ether or di-C 4 -alkyl ether or mixtures thereof.
Claim 7
Dependent Claim
41 words
The process of claim 3 wherein a bottom product comprising the C 3 - and/or C 4 -alkyl tert-butyl ether formed and containing not more than 1,000 ppm by weight of C 4 -hydrocarbon is taken off the first distillation zone.
Claim 8
Dependent Claim
56 words
The process of claim 3 wherein the bottom product obtained from the first distillation zone and containing the C 3 - or C 4 -alkyl tert-butyl ether formed is employed, without separation from the primary C 3 - or C 4 -alcohol contained in the said bottom product, as the starting material for the decomposition stage.
Claim 9
Dependent Claim
31 words
The process of claim 3 wherein the decomposition of the C 3 - or C 4 -alkyl tert-butyl ether is carried out under a pressure of from 2 to 15 bars.
Claim 10
Dependent Claim
62 words
The process of claim 3 wherein, in the second distillation zone, isobutene which is not less than 99.3% by weight pure and contains not more than 100 ppm by weight of di-C 3 -alkyl ether or di-C 4 -alkyl ether and/or C 3 - or C 4 -alkyl tert-butyl ether is taken off as the top product, without interpolating a water wash.
Claim 11
Dependent Claim
66 words
The process of claim 3 wherein the content, in the primary C 3 - or C 4 -alcohol recycled to the etherification reaction zone, of di-C 3 -alkyl ether or di-C 4 -alkyl ether which may form in very small amounts as the by-product but accumulates in the recycled primary C 3 - or C 4 -alcohol is restricted to from 2 to 20% by weight.
Claim 12
Dependent Claim
53 words
The process of claim 3 wherein, when using isobutanol as the primary C 4 -alcohol, a small isobutanol bleed-stream is taken off the side of the second distillation zone or form the bottom product of the second distillation zone and is dehydrated at an elevated temperature in the presence of a dehydration catalyst.
Claim 13
Dependent Claim
22 words
The process of claim 11 wherein an isobutanol part-stream containing from 3 to 40% by weight of diisobutyl ether is bled off.
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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) | 1984-08-31 | 1985-03-02 | 1985-09-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-08-31 | 1989-03-02 | 1989-09-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-08-31 | 1993-03-02 | 1993-09-01 | $7700.00 | Window Closed / Lapsed |