US4262146A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Production of aliphatic ethers
Assignee: Phillips Petroleum Co
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Filing: 1980-01-15
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Granted: 1981-04-14
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Expires: 2000-01-15
Abstract
Abstract A process is disclosed for the reaction of alcohols and iso-olefins to produce ethers wherein two reactors connected in series are employed and portions of the iso-olefin feed are diverted from said first reactor to said second as required to assist in maintaining the temperature in the first reactor below a selected valve. A system for achieving that end is also disclosed.
Inventors
- 👤 William V. Childs
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: 16
Claim 1
Independent Claim
142 words
In a process for producing aliphatic ether wherein a first feedstream comprising at least one alcohol selected from the group consisting of primary and secondary aliphatic alcohols containing 1 to 12 carbon atoms and a second feedstream comprising at least one iso-olefin having 4 to 6 carbon atoms are passed through a first reaction zone containing an acid ion exchange resin under conditions such that iso-olefin is converted to aliphatic ether and effluent from said first reaction zone is passed through a second reaction zone containing an acid ion exchange resin under conditions such that iso-olefin is converted to aliphatic ether, the improvement comprising diverting portions of said second feedstream to said second reaction zone in response to the temperature of said first reactor as required to assist in maintaining the maximum temperature in said first reaction zone below a selected value.
Claim 2
Dependent Claim
142 words
In a process for producing aliphatic ether wherein a first feedstream comprising at least one alcohol selected from the group consisting of primary and secondary aliphatic alcohols containing 1 to 12 carbon atoms and a second feedstream comprising at least one iso-olefin having 4 to 6 carbon atoms are passed through a first reaction zone containing an acid ion exchange resin under conditions such that iso-olefin is converted to aliphatic ether and effluent from said first reaction zone is passed through a second reaction zone containing an acid ion exchange resin under conditions such that iso-olefin is converted to aliphatic ether, the improvement comprising diverting portions of said second feedstream to said second reaction zone in response to the temperature of said first reactor as required to assist in maintaining the maximum temperature in said first reaction zone below a selected value.
Claim 3
Dependent Claim
26 words
A process according to claim 1 wherein isobutylene is the predominate iso-olefin in said second feedstream and methanol is the predominate alcohol in said first feedstream.
Claim 4
Dependent Claim
27 words
A process according to claim 2 wherein the temperature of said first reaction zone is maintained in the range of about 50° C. to about 80° C.
Claim 5
Dependent Claim
27 words
A process according to claim 3 wherein the temperature of said second reaction zone is maintained in the range of about 50° C. to about 80° C.
Claim 6
Dependent Claim
22 words
A process according to claim 4 wherein the maximum temperature in said first reaction zone is no greater than about 75° C.
Claim 7
Dependent Claim
34 words
A process according to claim 5 wherein the liquid hourly space velocity of feed to said first and second reaction zones is in the range of about 5 to about 20 hr -1 .
Claim 8
Dependent Claim
25 words
A process according to claim 6 wherein the molar ratio of methanol in said first feedstream to isobutylene in said second feedstream is about 1/1.
Claim 9
Dependent Claim
55 words
A process according to claim 7 wherein effluent from said second reaction zone is passed through a third reaction zone containing an acid ion exchange resin under conditions such that isobutylene is converted to aliphatic ether, said third reaction zone being maintained at temperatures in the range of about 30° C. to about 60° C.
Claim 10
Dependent Claim
22 words
A process according to claim 8 wherein the maximum temperature in said third reaction zone is no greater than about 45° C.
Claim 11
Dependent Claim
20 words
A process according to claim 9 wherein said iso-olefin consists essentially of isobutylene and said alcohol consists essentially of methanol.
Claim 12
Dependent Claim
28 words
A process according to claim 10 wherein said acid ion exchange resin is present in said first, second, and third reaction zones in the form of fixed beds.
Claim 13
Dependent Claim
20 words
A process according to claim 7 wherein said iso-olefin consists essentially of isobutylene and said alcohol consists essentially of methanol.
Claim 14
Dependent Claim
27 words
A process according to claim 7 wherein said acid ion exchange resin is present in said first and second reaction zones in the form of fixed beds.
Claim 15
Dependent Claim
19 words
A process according to claim 7 wherein said second feedstream contains about 10 to about 60 weight percent iso-olefin.
Claim 16
Dependent Claim
19 words
A process according to claim 11 wherein said second feedstream contains about 10 to about 60 weight percent isobutylene.
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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) | 1984-04-13 | 1984-10-13 | 1985-04-14 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-04-13 | 1988-10-13 | 1989-04-14 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-04-13 | 1992-10-13 | 1993-04-14 | $7700.00 | Window Closed / Lapsed |