US4482775A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Isomerization of C4 alkenes
Assignee: Catalytic Distillation Technologies
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Filing: 1982-09-22
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Granted: 1984-11-13
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Expires: 2002-09-22
Abstract
Abstract A method for isomerizing isobutene or n-butene to produce a mixture of isobutene and normal butene, and polymerizing at least a portion thereof to produce isobutene/n-butene codimer, which comprieses feeding at least 80 weight % of either the isobutene or n-butene to a catalytic distillation reactor containing a fixed bed acidic cation exchange resin catalyst packing which provides both the catalyst sites and distillation sites for the reaction products, isomerizing a portion of the isobutene or n-butene to produce a mixture of isobutene and n-butene and reacting at least a portion of the isobutene and n-butene to form codimer of isobutene and n-butene, whereby an overhead fraction containing any unreacted isobutene and n-butene and a bottoms fraction containing codimer is produced. The result of the reaction is substantially the same regardless whether the feed is isobutene or n-butene. Other aspects of the invention, include combinations of procedures to produce high purity isobutene and n-butene. Either isobutene or n-butene product (depending on the desired product) can be recycled as feed, thus substantially carrying out the isomerization to extinction and total conversion to the desired product.
Inventors
- 👤 Lawrence A. Smith, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 11:47
CPC Classifications
C; C07; C07C; C07C7/00; C07C7/005; B; B01; B01D; B01D3/00; B01D3/009; C07C7/148; Y; Y02; Y02P; Y02P20/00; Y02P20/10; Y10; Y10S; Y10S203/00; Y10S203/06; Y10S585/00; Y10S585/919; Y10S585/921; Y10S585/949; Y10S585/954
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
213 words
A method for producing high purity isobutene comprising: (a) feeding a hydrocarbon stream wherein the predominant reactive hydrocarbon comprises at least 80 weight percent n-butene to a distillation column reactor containing a fixed bed acidic cation exchange resin packing, (b) concurrently in said distillation column reactor: (1) contacting said n-butene with said fixed bed to isomerize a portion thereof to form a mixture of isobutene and n-butene, (2) reacting a portion of said normal butene with a portion of said isobutene to form codimer, and (3) fractionating the resulting mixture at a reflux ratio of 0.5 to 20:1, (c) withdrawing an overhead containing isobutene and n-butene at a point above said fixed bed, (d) withdrawing said codimer at a point below said fixed bed, (e) depolymerizing said codimer to produce an isobutene and n-butene stream, (f) contacting said depolymerized stream with an acidic cation exchange resin and an alcohol to selectively react said isobutene with said alcohol to form an ether, (g) separating said ether and unreacted n-butene by fractionation, (h) recovering an n-butene overhead, (i) recovering an ether bottoms product, (j) contacting said ether product in vapor phase with an acidic catalyst to dissociate said ether into isobutene and alcohol, (k) separating said alcohol and said isobutene and (l) recovering said isobutene.
Claim 2
Independent Claim
213 words
A method for producing high purity isobutene comprising: (a) feeding a hydrocarbon stream wherein the predominant reactive hydrocarbon comprises at least 80 weight percent n-butene to a distillation column reactor containing a fixed bed acidic cation exchange resin packing, (b) concurrently in said distillation column reactor: (1) contacting said n-butene with said fixed bed to isomerize a portion thereof to form a mixture of isobutene and n-butene, (2) reacting a portion of said normal butene with a portion of said isobutene to form codimer, and (3) fractionating the resulting mixture at a reflux ratio of 0.5 to 20:1, (c) withdrawing an overhead containing isobutene and n-butene at a point above said fixed bed, (d) withdrawing said codimer at a point below said fixed bed, (e) depolymerizing said codimer to produce an isobutene and n-butene stream, (f) contacting said depolymerized stream with an acidic cation exchange resin and an alcohol to selectively react said isobutene with said alcohol to form an ether, (g) separating said ether and unreacted n-butene by fractionation, (h) recovering an n-butene overhead, (i) recovering an ether bottoms product, (j) contacting said ether product in vapor phase with an acidic catalyst to dissociate said ether into isobutene and alcohol, (k) separating said alcohol and said isobutene and (l) recovering said isobutene.
Claim 3
Dependent Claim
21 words
The method according to claim 1 wherein said hydrocarbon stream is fed into said fixed bed acidic cation exchange resin packing.
Claim 4
Dependent Claim
110 words
The method according to claim 1 wherein steps (f-i) are carried out by feeding said depolymerized stream and an alcohol stream to a distillation column reactor containing a fixed bed acidic cation exchange resin packing; concurrently in said distillation column reactor: (1) contacting said depolymerized stream and said alcohol stream in said fixed bed to catalytically and selectively react said alcohol and isobutene to form ether, (2) fractionating the resulting mixture of ether and n-butene in said fixed bed, and (3) withdrawing ether from the distillation column reactor at a point below said fixed bed and withdrawing n-butene from the distillation column reactor at a point above said fixed bed.
Claim 5
Dependent Claim
19 words
The method according to claim 3 wherein said acidic catalyst in step (k) is an acidic cation exchange resin.
Claim 6
Dependent Claim
13 words
The method according to claim 4 wherein said alcohol is methanol or ethanol.
Claim 7
Dependent Claim
18 words
The method according to claim 4 wherein said alcohol is a C 3 to C 6 monohydric alcohol.
References Cited (Backward Citations)
US3629473A
Cited
US4039590A
Cited
US4198530A
Cited
US4242530A
Cited
US4302356A
Cited
US4250052A
Cited
US4215011A
Cited
US4232177A
Cited
US4307254A
Cited
US4336407A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-11-13 | 1988-05-14 | 1988-11-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-11-13 | 1992-05-14 | 1992-11-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-11-13 | 1996-05-14 | 1996-11-13 | $7700.00 | Window Closed / Lapsed |