Patent US4978807A successfully refreshed from Google Patents.
US4978807A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for the preparation of methyl tertiary butyl ether
Assignee: Catalytic Distillation Technologies
•
Filing: 1989-06-29
•
Granted: 1990-12-18
•
Expires: 2009-06-29
Abstract
Abstract A method and apparatus for conducting a catalytic distillation process is provided which allows for maintaining a liquid level in selected portions of the catalyst bed. Three particular processes disclosed are the production of methyl tertiary butyl ether, tertiary butyl alcohol and cumene. A method for the production of methyl tertiary butyl ether by reaction of isobutene with methanol in a distillation reaction column is disclosed wherein a liquid level maintained in the distillation reaction zone.
Inventors
- 👤 Lawrence A. Smith, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 13:30
CPC Classifications
B; B01; B01D; B01D3/00; B01D3/009; B01D3/14; B01D3/42; C; C07; C07C; C07C41/00; C07C41/01; C07C41/05; C07C41/06; C07C41/34; C07C41/40; C07C41/42; C07C43/00; C07C43/02; C07C43/03; C07C43/04; Y; Y02; Y02P; Y02P20/00; Y02P20/10; Y10; Y10S; Y10S203/00; Y10S203/06
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
220 words
A method of preparing methyl tertiary butyl ether comprising: (a) feeding (1) a mixture containing isobutene and normal butene and (2) methanol to a distillation column reactor into a feed zone, said distillation reactor column having an upper reaction distillation zone filled with a fixed bed cation exchange resin packing and a lower distillation zone. (b) concurrently in said distillation column reactor: (1) contacting said mixture and said methanol with said fixed bed acid cation exchange resin packing in said reaction distillation zone thereby catalytically reacting the isobutene with methanol to form methyl tertiary butyl ether and (2) fractionating the resulting mixture of ether and unreacted methanol, isobutene and normal butene in both said zones, vapor passing from said lower distillation zone into said upper reaction distillation zone and contacting said cation exchange resin packing therein while maintaining a froth level in said fixed bed acid cation exchange resin packing within said upper reaction distillation zone, said froth level being characterized as an increased density of the material in the reaction distillation zone compared to a distillation carried out in the absence of said froth level, (c) withdrawing the ether from the distillation column reactor as bottoms and (d) withdrawing the unreacted methanol, isobutene and normal butene from the upper reaction distillation zone of the distillation column reactor as overheads.
Claim 2
Independent Claim
220 words
A method of preparing methyl tertiary butyl ether comprising: (a) feeding (1) a mixture containing isobutene and normal butene and (2) methanol to a distillation column reactor into a feed zone, said distillation reactor column having an upper reaction distillation zone filled with a fixed bed cation exchange resin packing and a lower distillation zone. (b) concurrently in said distillation column reactor: (1) contacting said mixture and said methanol with said fixed bed acid cation exchange resin packing in said reaction distillation zone thereby catalytically reacting the isobutene with methanol to form methyl tertiary butyl ether and (2) fractionating the resulting mixture of ether and unreacted methanol, isobutene and normal butene in both said zones, vapor passing from said lower distillation zone into said upper reaction distillation zone and contacting said cation exchange resin packing therein while maintaining a froth level in said fixed bed acid cation exchange resin packing within said upper reaction distillation zone, said froth level being characterized as an increased density of the material in the reaction distillation zone compared to a distillation carried out in the absence of said froth level, (c) withdrawing the ether from the distillation column reactor as bottoms and (d) withdrawing the unreacted methanol, isobutene and normal butene from the upper reaction distillation zone of the distillation column reactor as overheads.
Claim 3
Dependent Claim
28 words
The method according to claim 1 wherein the temperature of said column is the boiling point of the mixture and said methanol under the pressure in said column.
Claim 4
Dependent Claim
25 words
The method according to claim 2 wherein said reacting and fractionating are carried out at a pressure in the range of 10 to 300 psig.
Claim 5
Dependent Claim
28 words
The method according to claim 1 wherein isobutene is removed from the mixture in said process thereby producing an overhead having a substantially reduced amount of isobutene therein.
Claim 6
Dependent Claim
14 words
The process according to claim 1 wherein said methyl tertiary butyl ether is recovered.
Claim 7
Dependent Claim
24 words
The method according to claim 1 wherein said feed zone is at the lower end of said fixed bed acid cation exchange resin packing.
Claim 8
Dependent Claim
45 words
The method according to claim 1 wherein any unreacted isobutene and unreacted methanol dissolved in the ether product is separated in said lower distillation zone below said reaction distillation zone thereby distilling said unreacted isobutene and unreacted methanol back up into said distillation reaction zone.
Claim 9
Dependent Claim
42 words
The method according to claim 7 wherein essentially all of said isobutene and methanol is reacted to form methyl tertiary butyl ether producing an overhead stream containing essentially pure normal butene and a bottoms stream containing essentially pure methyl tertiary butyl ether.
Claim 10
Dependent Claim
19 words
The method according to claim 1 wherein said lower distillation zone is contiguous to said upper distillation reaction zone.
Claim 11
Dependent Claim
31 words
The method according to claim 1 wherein said lower distillation zone is separated from said upper distillation reaction zone and is in fluid communication therewith for vapor and liquid flows therebetween.
Claim 12
Dependent Claim
22 words
The method according to claim 1 wherein said liquid level is maintained throughout the entire fixed bed acid cation exchange resin packing.
References Cited (Backward Citations)
US4089752A
Cited
US4302356A
Cited
US4242530A
Cited
US4250052A
Cited
US4307254A
Cited
US4232177A
Cited
US4215011A
Cited
US4336407A
Cited
US4475005A
Cited
US4443559A
Cited
US4439350A
Cited
US4482775A
Cited
US4847431A
Cited
US4847430A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1993-12-17 | 1994-06-18 | 1994-12-18 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1997-12-17 | 1998-06-18 | 1998-12-18 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2001-12-17 | 2002-06-18 | 2002-12-18 | $7700.00 | Window Closed / Lapsed |