Patent US4504687A successfully refreshed from Google Patents.
US4504687A
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US
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Method for etherifications
Assignee: Catalytic Distillation Technologies
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Filing: 1983-09-07
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Granted: 1985-03-12
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Expires: 2003-09-07
Abstract
Abstract A method for producing tertiary ethers from C 4 or C 5 streams containing isobutene and isoamylene respectively in a process wherein a acidic cation exchange resin is used as the catalyst and as a distillation structure in a distillation reactor column, wherein the improvement is the operation of the catalytic distillation in two zones at different pressures, the first zone containing the catalyst packing and operated a higher pressure in the range of 100 to 200 psig in the case of C 4 's and 15 to 100 psig in the case of C 5 's which favors the etherification reaction and the second zone being a distillation operated at a lower pressure in the range of 0 to 100 psig in the case of C 4 's and 0 to 15 psig in the case of C 5 's wherein a first overhead from the first zone is fractionated to remove a portion of the unreacted alcohol from the first overhead and to return a condensed portion containing said alcohol to the first zone and to produce a second overhead having less alcohol than said first overhead.
Inventors
- 👤 Edward M. Jones, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 09:01
CPC Classifications
C; C07; C07C; C07C41/00; C07C41/01; C07C41/05; C07C41/06; B; B01; B01D; B01D3/00; B01D3/009; C07C41/34; C07C41/40; C07C41/42; Y; Y02; Y02P; Y02P20/00; Y02P20/10; Y10; Y10S; Y10S203/00; Y10S203/06
Claims Analysis
Total Claims: 15
Claim 1
Independent Claim
260 words
A method for producing C 1 or C 2 alkyl tertiary C 4 ether comprising: (a) feeding: (1) a C 4 hydrocarbon stream containing isobutene, and (2) an alcohol selected from methanol or ethanol, to a first zone of a distillation column reactor having two separated zones independently operated at different pressures, said first zone containing a fixed bed acidic cation exchange resin, (b) concurrently: (1) contacting said C 4 hydrocarbon stream and said alcohol with said fixed bed acidic cation exchange resin packing in said first zone at a pressure in the range of 140 to 185 psig, thereby catalytically reacting isobutene with said alcohol to form C 1 or C 2 tertiary C 4 ether, and; (2) distilling the resulting mixture comprising said ether and unreacted materials in said first zone, (3) removing from said first zone a first overhead fraction comprising principally unreacted C 4 hydrocarbons and containing minor amounts of ether and alcohol as an azeotrope into a second zone, said second zone being a distillation zone operated at a pressure in the range of 0 to 100 psig thereby producing a second overhead having a reduced amount of alcohol therein from said first overhead, condensing a portion of said first overhead, said condensed portion containing substantially all of said ether and a portion of said alcohol of said first overhead and returning said condensed portion to said first zone, (4) withdrawing said second overhead from said second zone and, (5) withdrawing an ether product substantially free of alcohol from the bottom of said first zone.
Claim 2
Independent Claim
260 words
A method for producing C 1 or C 2 alkyl tertiary C 4 ether comprising: (a) feeding: (1) a C 4 hydrocarbon stream containing isobutene, and (2) an alcohol selected from methanol or ethanol, to a first zone of a distillation column reactor having two separated zones independently operated at different pressures, said first zone containing a fixed bed acidic cation exchange resin, (b) concurrently: (1) contacting said C 4 hydrocarbon stream and said alcohol with said fixed bed acidic cation exchange resin packing in said first zone at a pressure in the range of 140 to 185 psig, thereby catalytically reacting isobutene with said alcohol to form C 1 or C 2 tertiary C 4 ether, and; (2) distilling the resulting mixture comprising said ether and unreacted materials in said first zone, (3) removing from said first zone a first overhead fraction comprising principally unreacted C 4 hydrocarbons and containing minor amounts of ether and alcohol as an azeotrope into a second zone, said second zone being a distillation zone operated at a pressure in the range of 0 to 100 psig thereby producing a second overhead having a reduced amount of alcohol therein from said first overhead, condensing a portion of said first overhead, said condensed portion containing substantially all of said ether and a portion of said alcohol of said first overhead and returning said condensed portion to said first zone, (4) withdrawing said second overhead from said second zone and, (5) withdrawing an ether product substantially free of alcohol from the bottom of said first zone.
Claim 3
Dependent Claim
22 words
The method according to claim 1 wherein the pressure in the second zone is in the range of 65 to 85 psig.
Claim 4
Dependent Claim
22 words
The method according to claim 1 wherein the pressure in the first zone is in the range of 150 to 180 psig.
Claim 5
Dependent Claim
22 words
The method according to claim 3 wherein the pressure in the second zone is in the range of 70 to 75 psig.
Claim 6
Dependent Claim
12 words
The method according to claim 1 or 4 wherein alcohol is methanol.
Claim 7
Dependent Claim
13 words
The method according to claim 1 or 4 wherein the alcohol is ethanol.
Claim 8
Dependent Claim
19 words
The method according to claim 1 wherein said second overhead is condensed and further treated to remove alcohol therefrom.
Claim 9
Independent Claim
260 words
A method of producing C 1 or C 2 alkyl tertiary C 5 ether comprising: (a) feeding: (1) a C 5 hydrocarbon stream containing isoamylene, and, (2) an alcohol selected from methanol or ethanol, to a first zone of a distillation column reactor having two separated zones independently operated at different pressures, said first zone containing a fixed bed acidic cation exchange resin, (b) concurrently: (1) contacting said C 5 hydrocarbon stream and said alcohol with said fixed bed acidic cation exchange resin packing in said first zone at a pressure in the range of 30 to 70 psig, thereby catalytically reacting isoamylene with said alcohol to form C 1 to C 2 tertiary C 5 ether, and; (2) distilling the resulting mixture comprising said ether and unreacted materials in said first zone, (3) removing from said first zone a first overhead fraction comprising principally unreacted C 5 hydrocarbons and containing minor amounts of ether and alcohol as an azeotrope into a second zone, said second zone being a distillation zone operated at a pressure in the range of 0 to 15 psig thereby producing a second overhead having a reduced amount of alcohol therein from said first overhead, condensing a portion of said first overhead, said condensed portion containing substantially all of said ether and a portion of said alcohol of said first overhead and returning said condensed portion to said first zone, (4) withdrawing said second overhead from said second zone, and (5) withdrawing an ether product substantially free of alcohol from the bottom of said first zone.
Claim 10
Independent Claim
260 words
A method of producing C 1 or C 2 alkyl tertiary C 5 ether comprising: (a) feeding: (1) a C 5 hydrocarbon stream containing isoamylene, and, (2) an alcohol selected from methanol or ethanol, to a first zone of a distillation column reactor having two separated zones independently operated at different pressures, said first zone containing a fixed bed acidic cation exchange resin, (b) concurrently: (1) contacting said C 5 hydrocarbon stream and said alcohol with said fixed bed acidic cation exchange resin packing in said first zone at a pressure in the range of 30 to 70 psig, thereby catalytically reacting isoamylene with said alcohol to form C 1 to C 2 tertiary C 5 ether, and; (2) distilling the resulting mixture comprising said ether and unreacted materials in said first zone, (3) removing from said first zone a first overhead fraction comprising principally unreacted C 5 hydrocarbons and containing minor amounts of ether and alcohol as an azeotrope into a second zone, said second zone being a distillation zone operated at a pressure in the range of 0 to 15 psig thereby producing a second overhead having a reduced amount of alcohol therein from said first overhead, condensing a portion of said first overhead, said condensed portion containing substantially all of said ether and a portion of said alcohol of said first overhead and returning said condensed portion to said first zone, (4) withdrawing said second overhead from said second zone, and (5) withdrawing an ether product substantially free of alcohol from the bottom of said first zone.
Claim 11
Dependent Claim
22 words
The method according to claim 8 wherein the pressure in the second zone is in the range of 5 to 15 psig.
Claim 12
Dependent Claim
22 words
The method according to claim 11 wherein the pressure in the second zone is in the range of 10 to 15 psig.
Claim 13
Dependent Claim
12 words
The method according to claim 8 or 10 wherein alcohol is methanol.
Claim 14
Dependent Claim
13 words
The method according to claim 8 or 10 wherein the alcohol is ethanol.
Claim 15
Dependent Claim
19 words
The method according to claim 11 wherein said second overhead is condensed and further treated to remove alcohol therefrom.
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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) | 1988-03-11 | 1988-09-10 | 1989-03-12 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-03-11 | 1992-09-10 | 1993-03-12 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-03-11 | 1996-09-10 | 1997-03-12 | $7700.00 | Window Closed / Lapsed |