US4554386A
Expired / Lapsed
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Process for the preparation of methyl tertiary butyl ether
Assignee: DSM BV
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Filing: 1984-03-30
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Granted: 1985-11-19
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Expires: 2004-03-30
Abstract
Abstract A process for the preparation of methyl tertiary butyl ether (MTBE) in two stages: the first stage comprising the reaction of isobutene with methanol in the presence of an acid catalyst, yielding MTBE, while the second stage comprises firstly the conversion of normal-butenes present in the hydrocarbon flow, which remains behind after separation of the MTBE formed in the first stage into isobutene and secondly passing the mixture thus obtained to a reaction zone to form MTBE. Optionally an extra amount of methanol can be supplied to said reaction zone. Said reaction zone can be the same as that used in the same first stage or another one.
Inventors
- 👤 Christiaan Groeneveld
- 👤 Dirk Knol
- 👤 Johannes D. M. Verstegen
- 👤 Jacobus Jansen
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
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
193 words
In a process for the preparation of methyl tertiary butyl ether by contacting an isobutene-containing hydrocarbon feed, predominantly consisting of hydrocarbons with four carbon atoms, with methanol in a reaction zone in the presence of a catalyst and separating the methyl tertiary butyl ether thus formed from the reaction mixture, the improvement essentially comprising the combination of steps of: carrying out a first reaction between isobutene contained in said hydrocarbon feed and methanol in a first reaction zone in the presence of a catalyst, and separating methyl tertiary butyl ether thus formed from a first residual hydrocarbon stream containing normal-butene; introducing at least a portion of said residual hydrocarbon stream into an isomerization zone wherein at least a portion of the normal-butene introduced therein is converted to form a second residual hydrocarbon stream containing isobutene; and introducing said second residual hydrocarbon stream, together with a further amount of methanol, into a second reaction zone, separate from said first reaction zone, wherein isobutene contained in said second residual hydrocarbon stream is reacted with said further amount of methanol in the presence of a catalyst to form a further amount of methyl tertiary butyl ether.
Claim 2
Dependent Claim
193 words
In a process for the preparation of methyl tertiary butyl ether by contacting an isobutene-containing hydrocarbon feed, predominantly consisting of hydrocarbons with four carbon atoms, with methanol in a reaction zone in the presence of a catalyst and separating the methyl tertiary butyl ether thus formed from the reaction mixture, the improvement essentially comprising the combination of steps of: carrying out a first reaction between isobutene contained in said hydrocarbon feed and methanol in a first reaction zone in the presence of a catalyst, and separating methyl tertiary butyl ether thus formed from a first residual hydrocarbon stream containing normal-butene; introducing at least a portion of said residual hydrocarbon stream into an isomerization zone wherein at least a portion of the normal-butene introduced therein is converted to form a second residual hydrocarbon stream containing isobutene; and introducing said second residual hydrocarbon stream, together with a further amount of methanol, into a second reaction zone, separate from said first reaction zone, wherein isobutene contained in said second residual hydrocarbon stream is reacted with said further amount of methanol in the presence of a catalyst to form a further amount of methyl tertiary butyl ether.
Claim 3
Dependent Claim
31 words
The process of claim 1 wherein said methyl tertiary butyl ether formed in said second reaction in said second reaction zone is separated from a third residual hydrocarbon stream containing butanes.
Claim 4
Dependent Claim
13 words
The process of claim 2 wherein said butanes are discharged from the process.
Claim 5
Dependent Claim
25 words
The process of claim 1 wherein from between about 20 and 80 percent of said first residual hydrocarbon stream is introduced into said isomerization zone.
Claim 6
Dependent Claim
25 words
The process of claim 1 wherein from between about 40 and 60 percent of said first residual hydrocarbon stream in introduced into said isomerization zone.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1988-11-18 | 1989-05-20 | 1989-11-19 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-11-18 | 1993-05-20 | 1993-11-19 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-11-18 | 1997-05-20 | 1997-11-19 | $7700.00 | Window Closed / Lapsed |