Patent US4334964A successfully refreshed from Google Patents.
US4334964A
Expired / Lapsed
US
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Process for separating the reaction products obtained from etherifying lower isoolefins with methanol
Assignee: Edeleanu GmbH
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Filing: 1981-06-12
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Granted: 1982-06-15
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Expires: 2001-06-12
Abstract
Abstract A method for separating a mixture of reaction products produced in the catalytic etherification of a lower isoolefin with methanol wherein said reaction product comprises a mixture of ether, methanol, unreacted hydrocarbon and tertiary alcohol which comprises adding water to said reaction product to form a hydrocarbon phase containing said ether and an aqueous phase containing methanol and a tertiary alcohol, separating said hydrocarbon phase to recover a methyltertiary alkyl ether, introducing said alcohol-containing aqueous phase into a distillation column to separate a methanol fraction overhead, withdrawing a side stream rich in tertiary alcohol from said distillation column, stripping this side stream in a stripping column to separate a second methanol fraction overhead and a tertiary alcohol bottoms fraction and recycling the methanol overhead fraction from the stripping column to the upper part of the distillation column and recycling the overhead methanol fraction from the distillation column to the feed stream to said reactor.
Inventors
- 👤 Milan Prezelj
- 👤 Gunter Osterburg
- 👤 Joachim E. Putz
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 04:59
CPC Classifications
C; C07; C07C; C07C41/00; C07C41/01; C07C41/34; C07C41/40; C07C41/42; C07C41/05; C07C41/06; Y; Y10; Y10S; Y10S203/00; Y10S203/20
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
179 words
In a method for the production of an ether from the reaction of methanol and an isoolefin hydrocarbon feed stream in which the hydrocarbons have from 4 to 7 carbon atoms in a catalytic reactor wherein water is added to the reaction product from said reaction resulting in the formation of an organic hydrocarbon phase comprising said ether and unreacted hydrocarbons and an aqueous phase comprising methanol and a tertiary alcohol, and wherein said organic hydrocarbon phase is separated into an ether fraction and said aqueous phase is distilled in a distillation column to separate a methanol fraction overhead from said aqueous phase, the improvement which comprises withdrawing a side stream rich in tertiary alcohol from said distillation column, introducing said side stream into a stripping column and separating a second methanol fraction overhead and a tertiary alcohol bottoms fraction from said side stream, and recycling said methanol overhead fraction from the stripping column to the upper part of the distillation column and recycling the overhead methanol fraction from the distillation column to the feed stream to said reactor.
Claim 2
Dependent Claim
179 words
In a method for the production of an ether from the reaction of methanol and an isoolefin hydrocarbon feed stream in which the hydrocarbons have from 4 to 7 carbon atoms in a catalytic reactor wherein water is added to the reaction product from said reaction resulting in the formation of an organic hydrocarbon phase comprising said ether and unreacted hydrocarbons and an aqueous phase comprising methanol and a tertiary alcohol, and wherein said organic hydrocarbon phase is separated into an ether fraction and said aqueous phase is distilled in a distillation column to separate a methanol fraction overhead from said aqueous phase, the improvement which comprises withdrawing a side stream rich in tertiary alcohol from said distillation column, introducing said side stream into a stripping column and separating a second methanol fraction overhead and a tertiary alcohol bottoms fraction from said side stream, and recycling said methanol overhead fraction from the stripping column to the upper part of the distillation column and recycling the overhead methanol fraction from the distillation column to the feed stream to said reactor.
Claim 3
Dependent Claim
22 words
A method according to claim 1 in which said side stream comprises from about 30 to 50 percent of said tertiary alcohol.
Claim 4
Dependent Claim
17 words
A method according to claim 1 in which said side stream comprises about 40 percent tertiary alcohol.
Claim 5
Dependent Claim
21 words
A method according to claim 1 in which said stripping column is about one-tenth the capacity of said first distillation column.
Claim 6
Dependent Claim
34 words
A method according to claim 1 in which said side stream withdrawn from said distillation column is withdrawn from an intermediate zone of said distillation column above the feed inlet to said distillation column.
Claim 7
Dependent Claim
22 words
A method according to claim 1 in which said methanol overhead fraction from the distillation column is essentially free of tertiary alcohol.
Claim 8
Dependent Claim
19 words
A method according to claim 1 in which said tertiary alcohol bottoms fraction is blended with said ether fraction.
Claim 9
Dependent Claim
172 words
In a method for the production of methyl tertiary butyl ether from the reaction of methanol and an isobutylene hydrocarbon feed stream in a catalytic reactor wherein water is added to the reaction product from said reaction resulting in the formation of an organic hydrocarbon phase comprising methyl tertiary butyl ether and unreacted hydrocarbons and an aqueous phase comprising methanol and tertiary butanol and wherein said organic hydrocarbon phase is separated to recover a methyl tertiary butyl ether fraction and said aqueous phase is distilled in a first distillation column to separate a methanol fraction overhead, the improvement which comprises withdrawing a side stream rich in tertiary butanol from said distillation column, introducing said side stream into a stripping column and separating a second methanol fraction overhead and a tertiary butanol bottoms fraction from said side stream and recycling said methanol overhead fraction from the stripping column to the upper part of the distillation column and recycling the overhead methanol fraction from the distillation column to the feed stream to said reactor.
Claim 10
Dependent Claim
172 words
In a method for the production of methyl tertiary butyl ether from the reaction of methanol and an isobutylene hydrocarbon feed stream in a catalytic reactor wherein water is added to the reaction product from said reaction resulting in the formation of an organic hydrocarbon phase comprising methyl tertiary butyl ether and unreacted hydrocarbons and an aqueous phase comprising methanol and tertiary butanol and wherein said organic hydrocarbon phase is separated to recover a methyl tertiary butyl ether fraction and said aqueous phase is distilled in a first distillation column to separate a methanol fraction overhead, the improvement which comprises withdrawing a side stream rich in tertiary butanol from said distillation column, introducing said side stream into a stripping column and separating a second methanol fraction overhead and a tertiary butanol bottoms fraction from said side stream and recycling said methanol overhead fraction from the stripping column to the upper part of the distillation column and recycling the overhead methanol fraction from the distillation column to the feed stream to said reactor.
Claim 11
Dependent Claim
19 words
A method according to claim 8 in which said side stream comprises about 40 percent of said tertiary butanol.
Claim 12
Dependent Claim
21 words
A method according to claim 8 in which said tertiary butanol fraction and said methyl tertiary butyl ether fraction are blended.
Claim 13
Dependent Claim
210 words
In a two-step method for the production of an ether from the reaction of methanol and an isoolefin hydrocarbon feed stream in which the hydrocarbons have from 4 to 7 carbon atoms in a first and a second catalytic reactor having a distillation stage between said reactors wherein the bottom product from said distillation stage is combined with the reaction product from said second catalytic reactor and wherein water is added to said mixture resulting in the formation of an organic hydrocarbon phase comprising said ether and unreacted hydrocarbons and an aqueous phase comprising methanol and a tertiary alcohol, and wherein from said organic hydrocarbon phase is separated an ether fraction and said aqueous phase is separated in a distillation column to separate a methanol fraction overhead from said aqueous phase, the improvement which comprises withdrawing a side stream rich in tertiary alcohol from said water separation distillation column, introducing said side stream into a stripping column and separating a second methanol fraction overhead and a tertiary alcohol bottoms fraction from said side stream, and recycling said methanol overhead fraction from the stripping column to the upper part of the distillation column and recycling the overhead methanol fraction from the distillation column to the feed stream to said first reactor.
Claim 14
Dependent Claim
210 words
In a two-step method for the production of an ether from the reaction of methanol and an isoolefin hydrocarbon feed stream in which the hydrocarbons have from 4 to 7 carbon atoms in a first and a second catalytic reactor having a distillation stage between said reactors wherein the bottom product from said distillation stage is combined with the reaction product from said second catalytic reactor and wherein water is added to said mixture resulting in the formation of an organic hydrocarbon phase comprising said ether and unreacted hydrocarbons and an aqueous phase comprising methanol and a tertiary alcohol, and wherein from said organic hydrocarbon phase is separated an ether fraction and said aqueous phase is separated in a distillation column to separate a methanol fraction overhead from said aqueous phase, the improvement which comprises withdrawing a side stream rich in tertiary alcohol from said water separation distillation column, introducing said side stream into a stripping column and separating a second methanol fraction overhead and a tertiary alcohol bottoms fraction from said side stream, and recycling said methanol overhead fraction from the stripping column to the upper part of the distillation column and recycling the overhead methanol fraction from the distillation column to the feed stream to said first reactor.
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) | 1985-06-14 | 1985-12-14 | 1986-06-15 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-06-14 | 1989-12-14 | 1990-06-15 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-06-14 | 1993-12-14 | 1994-06-15 | $7700.00 | Window Closed / Lapsed |