US4413150A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Two product process for methyl tertiary butyl ether production
Assignee: Honeywell UOP LLC
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Filing: 1981-12-18
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Granted: 1983-11-01
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Expires: 2001-12-18
Abstract
Abstract A hydrocarbon conversion process which net high purity isobutane feed streams into two product streams containing an ether such as methyl tertiary butyl ether (MTBE) by reaction with methanol or ethanol. The isobutylene, alcohol and a recycle stream containing C 4 hydrocarbons, alcohol and the product ether are passed through an etherification zone. The total etherification zone effluent stream is separated in a single fractionation column. Preferably the new overhead of the fractionation column is divided into the recycle stream and a second portion which is combined with a portion of the bottoms of this column to produce a gasoline grade MTBE product stream. The remainder of the fractionation column bottoms is a second product stream of chemical grade MTBE.
Inventors
- 👤 Bruce A. Briggs
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 03:29
CPC Classifications
C; C07; C07C; C07C41/00; C07C41/01; C07C41/05; C07C41/06; C07C41/34; C07C41/40; C07C41/42; Y; Y10; Y10S; Y10S203/00; Y10S203/14
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
160 words
A hydrocarbon conversion process which comprises the steps of: (a) reacting isobutylene with a C 1 to C 3 aliphatic alcohol in an etherification zone and producing an etherification zone effluent stream which comprises C 4 hydrocarbons, unconverted alcohol and a reaction product ether; (b) separating the entire etherification zone effluent stream in a single fractionation column into a net overhead stream comprising C 4 hydrocarbons, the unconverted alcohol and a portion of the reaction product ether and a net bottoms stream comprising the remainder of the reaction product ether and which is substantially free of the alcohol; (c) passing between about 70 to 90 weight percent of said net overhead stream into the etherification zone; (d) admixing between 5 to 40 weight percent of said net overhead stream with a first portion of said net bottoms stream to form a first product stream; and, (e) removing a second portion of said net bottoms stream as a second product stream.
Claim 2
Dependent Claim
160 words
A hydrocarbon conversion process which comprises the steps of: (a) reacting isobutylene with a C 1 to C 3 aliphatic alcohol in an etherification zone and producing an etherification zone effluent stream which comprises C 4 hydrocarbons, unconverted alcohol and a reaction product ether; (b) separating the entire etherification zone effluent stream in a single fractionation column into a net overhead stream comprising C 4 hydrocarbons, the unconverted alcohol and a portion of the reaction product ether and a net bottoms stream comprising the remainder of the reaction product ether and which is substantially free of the alcohol; (c) passing between about 70 to 90 weight percent of said net overhead stream into the etherification zone; (d) admixing between 5 to 40 weight percent of said net overhead stream with a first portion of said net bottoms stream to form a first product stream; and, (e) removing a second portion of said net bottoms stream as a second product stream.
Claim 3
Dependent Claim
23 words
The process of claim 2 further characterized in that the etherification zone effluent stream contains less than 10 mole percent C 4 hydrocarbons.
Claim 4
Dependent Claim
13 words
The process of claim 2 further characterized in that the alcohol is ethanol.
Claim 5
Dependent Claim
13 words
The process of claim 2 further characterized in that the alcohol is methanol.
Claim 6
Dependent Claim
25 words
The process of claim 4 further characterized in that the mole ratio of methanol to isobutylene which enters the etherification zone is greater than 1.15:1.0.
Claim 7
Dependent Claim
220 words
A hydrocarbon conversion process which comprises the steps of: (a) passing a first feed stream comprising at least 85 mole percent isobutylene and a small amount of other C 4 hydrocarbons, a recycle stream comprising methanol, methyl tertiary butyl ether and C 4 hydrocarbons and a second feed stream comprising methanol into an etherification zone operated at etherification conditions and thereby producing an etherification zone effluent stream which comprises methanol, C 4 hydrocarbons and methyl tertiary butyl ether; (b) separating the etherification zone effluent stream in a fractionation column into a net bottoms stream which comprises methyl tertiary butyl ether and a net overhead stream which comprises substantially all of the methanol and isobutane present in the etherification zone effluent stream and which also comprises methyl tertiary butyl ether; (c) passing between about 70 to 90 weight percent of said net overhead stream into the etherification zone as the previously referred to recycle stream; (d) combining between 5 to 40 weight percent of said net overhead stream with a first portion of said net bottoms stream and thereby forming a first product stream comprising methanol and methyl tertiary butyl ether; and (e) removing a second portion of said net bottoms stream as a second product stream containing a higher concentration of methyl tertiary butyl ether than the first product stream.
Claim 8
Dependent Claim
220 words
A hydrocarbon conversion process which comprises the steps of: (a) passing a first feed stream comprising at least 85 mole percent isobutylene and a small amount of other C 4 hydrocarbons, a recycle stream comprising methanol, methyl tertiary butyl ether and C 4 hydrocarbons and a second feed stream comprising methanol into an etherification zone operated at etherification conditions and thereby producing an etherification zone effluent stream which comprises methanol, C 4 hydrocarbons and methyl tertiary butyl ether; (b) separating the etherification zone effluent stream in a fractionation column into a net bottoms stream which comprises methyl tertiary butyl ether and a net overhead stream which comprises substantially all of the methanol and isobutane present in the etherification zone effluent stream and which also comprises methyl tertiary butyl ether; (c) passing between about 70 to 90 weight percent of said net overhead stream into the etherification zone as the previously referred to recycle stream; (d) combining between 5 to 40 weight percent of said net overhead stream with a first portion of said net bottoms stream and thereby forming a first product stream comprising methanol and methyl tertiary butyl ether; and (e) removing a second portion of said net bottoms stream as a second product stream containing a higher concentration of methyl tertiary butyl ether than the first product stream.
Claim 9
Dependent Claim
20 words
The process of claim 6 further characterized in that the first feed stream comprises at least 93 mole percent isobutylene.
Claim 10
Dependent Claim
23 words
The process of claim 7 further characterized in that the etherification zone effluent stream contains less than 20 mole percent C 4 hydrocarbons.
Claim 11
Dependent Claim
35 words
The process of claim 6 further characterized in that the flow rate of the second portion of said net overhead stream is between about 10 and about 30 weight percent of said net overhead stream.
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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) | 1986-10-31 | 1987-05-02 | 1987-11-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-10-31 | 1991-05-02 | 1991-11-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-10-31 | 1995-05-02 | 1995-11-01 | $7700.00 | Window Closed / Lapsed |