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Iso-C4 compound reactions with perfluorosulfonic acid resin catalysts

Assignee: Texas Petrochemicals Corp
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Filing: 1976-07-06
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Granted: 1977-12-27
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Expires: 1996-07-06
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Abstract

Abstract Perfluorosulfonic acid resin membranes are active catalysts for the hydration and polymerization of isobutene and dehydration of t-butanol. The membranes offer unique advantages for hydration and dehydration since they are semi-permeable to water and impermeable to hydrocarbons.

Inventors

  • 👤 William R. Cares

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 16:59
CPC Classifications
C; C07; C07C; C07C1/00; C07C1/20; C07C1/24; B; B01; B01J; B01J10/00; B01J10/007; B01J14/00; B01J14/005; B01J35/00; B01J35/50; B01J35/58; B01J35/59; C07C2/00; C07C2/02; C07C2/04; C07C2/06; C07C2/08; C07C2/26; C08; C08F; C08F10/00; C07C2531/00; C07C2531/02; C07C2531/06; C07C2531/08; C07C2531/10

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 54 words
A process for producing t-butanol comprising contacting isobutene and water with a membrane of a perfluorosulfonic acid resin which is the copolymer of sulfonyl fluorovinyl ether and a fluorocarbon at a temperature in the range of about 0° to 150° C, said membrane separating said isobutene and water and recovering a product containing t-butanol.
Claim 2
Dependent Claim 54 words
A process for producing t-butanol comprising contacting isobutene and water with a membrane of a perfluorosulfonic acid resin which is the copolymer of sulfonyl fluorovinyl ether and a fluorocarbon at a temperature in the range of about 0° to 150° C, said membrane separating said isobutene and water and recovering a product containing t-butanol.
Claim 3
Dependent Claim 11 words
The process according to claim 1 carried out in vapor phase.
Claim 4
Dependent Claim 11 words
The process according to claim 1 carried out in liquid phase.
Claim 5
Dependent Claim 18 words
The process according to claim 1 wherein the temperature is in the range of 15 to 90° C.
Claim 6
Dependent Claim 49 words
The process according to claim 1 where isobutene is contacted with one side of a membrane of perfluorosulfonic acid resin and water is contacted at the same time with the opposite side of said membrane at a temperature of 0° to 150° C and t-butanol recovered from the isobutene.
Claim 7
Dependent Claim 25 words
The process according to claim 5 wherein the process is continuous and the LHSV of the isobutene is in the range of 0.1 to 3.0.
Claim 8
Dependent Claim 90 words
In the process for the preparation of the t-butanol by reacting isobutene and water in the presence of an acid catalyst at temperatures in the range of about 120° to 150° C, wherein the improvement comprises employing as the acid catalyst a membrane of a perfluorosulfonic acid resin which is the copolymer of sulfonyl fluorovinyl ether and a fluorocarbon, contacting isobutene with one side of said membrane and water with the other side thereof, said membrane separating said isobutene and water and recovering t-butanol from said isobutene contacting said membrane.
Claim 9
Dependent Claim 90 words
In the process for the preparation of the t-butanol by reacting isobutene and water in the presence of an acid catalyst at temperatures in the range of about 120° to 150° C, wherein the improvement comprises employing as the acid catalyst a membrane of a perfluorosulfonic acid resin which is the copolymer of sulfonyl fluorovinyl ether and a fluorocarbon, contacting isobutene with one side of said membrane and water with the other side thereof, said membrane separating said isobutene and water and recovering t-butanol from said isobutene contacting said membrane.
Claim 10
Dependent Claim 15 words
The process according to claim 7 wherein said perfluorosulfonic acid resin membrane in a tube.
Claim 11
Dependent Claim 16 words
The process according to claim 17 wherein said membrane is about 2 to 20 mils thick.

References Cited (Backward Citations)

US3256250A Cited
US3328471A Cited
US3950442A Cited
US3994983A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-12-26 1981-06-27 1981-12-27 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-12-26 1985-06-27 1985-12-27 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-12-26 1989-06-27 1989-12-27 $7700.00 Window Closed / Lapsed

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