US4232177A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Catalytic distillation process
Assignee: Catalytic Distillation Technologies
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Filing: 1979-02-21
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Granted: 1980-11-04
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Expires: 1999-02-21
Abstract
Abstract A method for conducting chemical reactions and fractionation of the reaction mixture comprising feeding reactants to a distillation column reactor into a feed zone and concurrently contracting the reactants with a fixed bed catalytic packing to concurrently carry out the reaction and fractionate the reaction mixture. For example, a method for preparing methyl tertiary butyl ether in high purity from a mixed feed stream of isobutene and normal butene comprising feeding the mixed feed stream to a distillation column reactor into a feed zone at the lower end of a distillation reaction zone, and methanol into the upper end of said distillation reaction zone, which is packed with a properly supported cationic ion exchange resin, contacting the C4 feed and methanol with the catalytic distillation packing to react methanol and isobutene, and concurrently fractionating the ether from the column below the catalytic zone and removing normal butene overhead above the catalytic zone.
Inventors
- 👤 Lawrence A. Smith, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 19:47
CPC Classifications
B; B01; B01D; B01D3/00; B01D3/009; B01J; B01J8/00; B01J8/02; C; C07; C07C; C07C1/00; C07C1/20; C07C2/00; C07C2/02; C07C2/04; C07C2/06; C07C2/08; C07C2/26; C07C2/28; C07C41/00; C07C41/01; C07C41/05; C07C41/06; C07C41/34; C07C41/40; C07C41/42; C07C7/00; C07C7/148; C07C7/177; B01J2208/00; B01J2208/00008; B01J2208/00017; B01J2208/00026; B01J2208/00035; B01J2208/0007; B01J2208/00106; B01J2208/00168; B01J2208/00247; B01J2208/00539; B01J2208/00548; B01J2208/00557; C07C2531/00; C07C2531/02; C07C2531/06; C07C2531/08; Y; Y02; Y02P; Y02P20/00; Y02P20/10; Y10; Y10S; Y10S203/00; Y10S203/06; Y10S585/00; Y10S585/949; Y10S585/954
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
120 words
A method of producing isobutene comprising: (a) feeding methyl tertiary butyl ether to a distillation column reactor into a feed zone said feed zone being at the upper end of a fixed bed acid cation exchange resin packing, (b) concurrently in said distillation column reactor: (1) contacting said methyl tertiary butyl ether with a fixed bed cation exchange resin packing in a distillation reaction zone thereby catalytically dissociating methyl tertiary butyl ether into methanol and isobutene, (2) fractionating the resulting mixture in said fixed bed ion exchange resin packing, (c) withdrawing isobutene from the distillation column reactor at a point above said feed zone, and (d) withdrawing methanol from the distillation column reactor at a point below said feed zone.
Claim 2
Independent Claim
120 words
A method of producing isobutene comprising: (a) feeding methyl tertiary butyl ether to a distillation column reactor into a feed zone said feed zone being at the upper end of a fixed bed acid cation exchange resin packing, (b) concurrently in said distillation column reactor: (1) contacting said methyl tertiary butyl ether with a fixed bed cation exchange resin packing in a distillation reaction zone thereby catalytically dissociating methyl tertiary butyl ether into methanol and isobutene, (2) fractionating the resulting mixture in said fixed bed ion exchange resin packing, (c) withdrawing isobutene from the distillation column reactor at a point above said feed zone, and (d) withdrawing methanol from the distillation column reactor at a point below said feed zone.
Claim 3
Independent Claim
114 words
A method of producing diisobutene comprising: (a) feeding methyl tertiary butyl ether to a distillation column reactor into a feed zone, said feed zone being at the lower end of a fixed bed acid cation exchange resin packing, (b) concurrently in said distillation column reactor: (1) contacting said methyl tertiary butyl ether with a fixed bed cation exchange resin packing in a distillation reaction zone thereby catalytically dissociating methyl tertiary butyl ether into methanol and isobutene, (2) contacting said isobutene with said packing to form diisobutene, (3) fractionating the resulting mixture in said fixed bed ion exchange resin packing, (c) withdrawing diisobutene from the distillation column reactor at a point below said feed zone.
Claim 4
Independent Claim
114 words
A method of producing diisobutene comprising: (a) feeding methyl tertiary butyl ether to a distillation column reactor into a feed zone, said feed zone being at the lower end of a fixed bed acid cation exchange resin packing, (b) concurrently in said distillation column reactor: (1) contacting said methyl tertiary butyl ether with a fixed bed cation exchange resin packing in a distillation reaction zone thereby catalytically dissociating methyl tertiary butyl ether into methanol and isobutene, (2) contacting said isobutene with said packing to form diisobutene, (3) fractionating the resulting mixture in said fixed bed ion exchange resin packing, (c) withdrawing diisobutene from the distillation column reactor at a point below said feed zone.
Claim 5
Dependent Claim
23 words
The method according to claim 1 or 2 wherein the feed into the distillation column reactor contains less than 1 mole % water.
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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) | 1983-11-04 | 1984-05-05 | 1984-11-04 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-11-04 | 1988-05-05 | 1988-11-04 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-11-04 | 1992-05-05 | 1992-11-04 | $7700.00 | Window Closed / Lapsed |