US4906788A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Combined dehydrogenation etherification process
Assignee: Honeywell UOP LLC
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Filing: 1988-10-26
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Granted: 1990-03-06
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Expires: 2008-10-26
Abstract
Abstract A combined process for the dehydrogenation of C 4 -C 5 paraffins in a first zone and the etherification of olefins in a second zone improves efficiency by directly charging all but the lightest components of the dehydrogenation zone effluent to the etherification zone. This process is particularly suited for the production of gasoline boiling range ethers where an isoparaffin is dehydrogenated in a first zone to produce isoolefins. After separation of hydrogen and methane, the dehydrogenation zone effluent is charged along with methanol to an etherification zone for the production of MTBE. The etherification zone effluent is separated into at least three component streams comprising light ends, isoparaffins, and the ether product. Isoparaffins, separated from the etherification zone effluent, are recycled and combined with the feed to dehydrogenation zone. The particular arrangement of this invention uses an etherification zone for the production of MTBE and a single fractionation column to yield an overhead stream of light ends, a sidecut stream of recycle isoparaffins and methanol, and a bottoms product stream of MTBE.
Inventors
- 👤 Norman H. Scott
- 👤 Bipin V. Vora
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 13:24
CPC Classifications
C; C07; C07C; C07C41/00; C07C41/01; C07C41/34; C07C41/40; C07C41/42; C07C41/05; C07C41/06
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
227 words
A method of preparing ethers from a feed stream comprising C 4 -C 5 isoalkane hydrocarbons which comprises: (a) dehydrogenating said feed stream in a dehydrogenation zone at dehydrogenation conditions including a temperature in the range of 500° C. (930° F.) to 700° C. (1290° F.), a pressure of from 0.1 to 3 bars and in the presence of a dehydrogenation catalyst to produce a dehydrogenation effluent comprising C 4 -C 5 isoolefins and isoalkanes, and light gases, said light gases including hydrocarbons having at least as few as 3 carbon atoms per molecule: (b) passing at least all C 3 and higher hydrocarbons in said dehydrogenation effluent to an etherification zone; (c) combining at least all C 3 and higher hydrocarbons and a C 1 -C 5 alcohol in said etherification zone at etherification conditions to obtain essentially complete conversion of said isoolefins and an etherification effluent comprising isoalkanes, alcohol, light gases, and ether; (d) separating said etherification effluent into at least a product stream comprising ether, a recycle stream comprising isoalkanes and a light gas stream comprising said light gases in a single fractionation column and recovering said product stream, recycle stream, and light gas stream from said column as a bottoms stream, sidecut stream, and an overhead stream, respectively; and (e) returning at least a portion of said recycle stream to said dehydrogenation zone.
Claim 2
Independent Claim
227 words
A method of preparing ethers from a feed stream comprising C 4 -C 5 isoalkane hydrocarbons which comprises: (a) dehydrogenating said feed stream in a dehydrogenation zone at dehydrogenation conditions including a temperature in the range of 500° C. (930° F.) to 700° C. (1290° F.), a pressure of from 0.1 to 3 bars and in the presence of a dehydrogenation catalyst to produce a dehydrogenation effluent comprising C 4 -C 5 isoolefins and isoalkanes, and light gases, said light gases including hydrocarbons having at least as few as 3 carbon atoms per molecule: (b) passing at least all C 3 and higher hydrocarbons in said dehydrogenation effluent to an etherification zone; (c) combining at least all C 3 and higher hydrocarbons and a C 1 -C 5 alcohol in said etherification zone at etherification conditions to obtain essentially complete conversion of said isoolefins and an etherification effluent comprising isoalkanes, alcohol, light gases, and ether; (d) separating said etherification effluent into at least a product stream comprising ether, a recycle stream comprising isoalkanes and a light gas stream comprising said light gases in a single fractionation column and recovering said product stream, recycle stream, and light gas stream from said column as a bottoms stream, sidecut stream, and an overhead stream, respectively; and (e) returning at least a portion of said recycle stream to said dehydrogenation zone.
Claim 3
Dependent Claim
34 words
The method of claim 1 wherein said dehydrogenation zone effluent includes hydrogen, hydrogen is recovered from said dehydrogenation zone effluent and at least a portion of said hydrogen is admixed with said feed stream.
Claim 4
Dependent Claim
44 words
The method of claim 1 wherein said dehydrogenation zone effluent includes hydrogen, methane and C 2 hydrocarbons, hydrogen and methane are separated from said dehydrogenation effluent and essentially all C 2 and higher hydrocarbons from said dehydrogenation effluent are passed to said etherification zone.
Claim 5
Dependent Claim
37 words
The process of claim 1 wherein said sidecut stream contains unreacted alcohol from said etherification effluent and at least a portion of said unreacted alcohol from said sidecut stream is recovered and recycled to said etherification zone.
Claim 6
Independent Claim
232 words
A method of preparing ethers from a feed stream comprising C 4 -C 5 isoalkane hydrocarbons which comprises: (a) dehydrogenating said feed stream in a dehydrogenation zone at dehydrogenation conditions including a temperature in the range of 500° C. (930° F.) to 700° C. (1290° F.), a pressure of from 0.1 to 3 bars and in the presence of a dehydrogenation catalyst to produce a dehydrogenation effluent comprising C 4 -C 5 isoolefins and isoalkanes and light gases, said light gases including hydrocarbons having at least as few as 2 carbon atoms per molecule; (b) passing C 2 hydrocarbons and essentially all C 3 and higher hydrocarbons in said dehydrogenation effluent to an etherification zone; (c) combining C 2 hydrocarbons and essentially all C 3 and higher hydrocarbons and a C 1 -C 5 alcohol in said etherification zone at etherification conditions to obtain essentially complete conversion of said isoolefin and an etherification effluent comprising isoalkanes, alcohol, light gases, and ether; (d) separating said etherification effluent into at least a product stream comprising ether, a recycle stream comprising isoalkanes and a light gas stream comprising said light gases in a single fractionation column and recovering said product stream, recycle stream, and light gas stream from said column as a bottoms stream, sidecut stream, and overhead stream, respectively; and (e) returning at least a portion of said recycle stream to said dehydrogenation unit.
Claim 7
Independent Claim
232 words
A method of preparing ethers from a feed stream comprising C 4 -C 5 isoalkane hydrocarbons which comprises: (a) dehydrogenating said feed stream in a dehydrogenation zone at dehydrogenation conditions including a temperature in the range of 500° C. (930° F.) to 700° C. (1290° F.), a pressure of from 0.1 to 3 bars and in the presence of a dehydrogenation catalyst to produce a dehydrogenation effluent comprising C 4 -C 5 isoolefins and isoalkanes and light gases, said light gases including hydrocarbons having at least as few as 2 carbon atoms per molecule; (b) passing C 2 hydrocarbons and essentially all C 3 and higher hydrocarbons in said dehydrogenation effluent to an etherification zone; (c) combining C 2 hydrocarbons and essentially all C 3 and higher hydrocarbons and a C 1 -C 5 alcohol in said etherification zone at etherification conditions to obtain essentially complete conversion of said isoolefin and an etherification effluent comprising isoalkanes, alcohol, light gases, and ether; (d) separating said etherification effluent into at least a product stream comprising ether, a recycle stream comprising isoalkanes and a light gas stream comprising said light gases in a single fractionation column and recovering said product stream, recycle stream, and light gas stream from said column as a bottoms stream, sidecut stream, and overhead stream, respectively; and (e) returning at least a portion of said recycle stream to said dehydrogenation unit.
Claim 8
Dependent Claim
30 words
The process of claim 5 wherein said dehydrogenation zone effluent includes hydrogen, hydrogen is recovered from said dehydrogenation effluent at least a portion of hydrogen is admixed with said feed.
Claim 9
Dependent Claim
23 words
The process of claim 5 wherein essentially all C 2 and higher hydrocarbons from said dehydrogenation effluent are passed to said etherification zone.
Claim 10
Independent Claim
293 words
A method for preparing ethers from a feed stream comprising isobutane which comprises: (a) combining said feed stream with a hydrogen stream and an isobutane recycle stream to obtain a combined feed stream; (b) passing said combined feed stream to a dehydrogenation zone and dehydrogenating said combined feed stream in said dehydrogenation zone at dehydrogenation conditions including a temperature in the range of 500° C. (930° F.) to 700° C. (1290° F.), a pressure of from 0.1 to 3 bars and in the presence of a dehydrogenation catalyst to obtain a dehydrogenation effluent comprising isobutene, isobutane, and light gases, said light gases including hydrocarbons having at least as few as 2 carbon atoms per molecule; (c) removing hydrogen from said dehydrogenation zone effluent and recovering at least a portion of said hydrogen in said hydrogen stream; (d) passing essentially all C 2 and higher hydrocarbons in said dehydrogenation effluent to an etherification zone; (e) combining said essentially all C 2 and higher hydrocarbons and a C 1 -C 5 alcohol in said etherification zone at etherification conditions including a temperature of 50° C. (120° F.) to 80° C. (175° F.), a pressure of 10 bars to 15 bars and in the presence of an etherification catalyst to obtain essentialy complete conversion of isobutene and produce an etherification effluent stream comprising a tertiary butyl ether, isobutane, alcohol, and light gases having less than 4 carbon atoms per molecule; and (f) separating said etherification effluent into at least a product stream comprising ether, said isobutane recycle stream, and a light gas stream comprising said light gases in a single fractionation column and recovering said product stream, recycle stream, and light gas stream from said column as a bottoms stream, sidecut stream, and overhead stream, respectively.
Claim 11
Independent Claim
293 words
A method for preparing ethers from a feed stream comprising isobutane which comprises: (a) combining said feed stream with a hydrogen stream and an isobutane recycle stream to obtain a combined feed stream; (b) passing said combined feed stream to a dehydrogenation zone and dehydrogenating said combined feed stream in said dehydrogenation zone at dehydrogenation conditions including a temperature in the range of 500° C. (930° F.) to 700° C. (1290° F.), a pressure of from 0.1 to 3 bars and in the presence of a dehydrogenation catalyst to obtain a dehydrogenation effluent comprising isobutene, isobutane, and light gases, said light gases including hydrocarbons having at least as few as 2 carbon atoms per molecule; (c) removing hydrogen from said dehydrogenation zone effluent and recovering at least a portion of said hydrogen in said hydrogen stream; (d) passing essentially all C 2 and higher hydrocarbons in said dehydrogenation effluent to an etherification zone; (e) combining said essentially all C 2 and higher hydrocarbons and a C 1 -C 5 alcohol in said etherification zone at etherification conditions including a temperature of 50° C. (120° F.) to 80° C. (175° F.), a pressure of 10 bars to 15 bars and in the presence of an etherification catalyst to obtain essentialy complete conversion of isobutene and produce an etherification effluent stream comprising a tertiary butyl ether, isobutane, alcohol, and light gases having less than 4 carbon atoms per molecule; and (f) separating said etherification effluent into at least a product stream comprising ether, said isobutane recycle stream, and a light gas stream comprising said light gases in a single fractionation column and recovering said product stream, recycle stream, and light gas stream from said column as a bottoms stream, sidecut stream, and overhead stream, respectively.
Claim 12
Dependent Claim
22 words
The method of claim 8 wherein said dehydrogenation catalyst comprises Pt on alumina and said etherification catalyst is a sulfonic acid resin.
Claim 13
Dependent Claim
21 words
The process of claim 9 wherein said C 1 -C 5 alcohol consists of methanol and said etherification zone produces MTBE.
Claim 14
Dependent Claim
36 words
The process of claim 10 wherein said sidecut stream contains unreacted methanol, said sidecut stream is further processed to recover unreacted methanol, and at least a portion of said methanol is returned to said etherification zone.
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) | 1993-03-05 | 1993-09-04 | 1994-03-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1997-03-05 | 1997-09-04 | 1998-03-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2001-03-05 | 2001-09-04 | 2002-03-06 | $7700.00 | Window Closed / Lapsed |