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US4071567A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the production of methyl tert-butyl ether

Assignee: SnamProgetti SpA
•
Filing: 1976-08-12
•
Granted: 1978-01-31
•
Expires: 1996-08-12
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Abstract

Abstract Methyl tert-butyl ether of high purity is prepared by reacting methanol with isobutylene in the presence of an acid ion exchange resin in two stages by feeding methanol and isobutylene mixed with other hydrocarbons to the respective members of a pair of interconnected reactors so that the quantity of alcohol present in one of the reactors is in excess of the stoichiometric equivalent of the quantity of isobutylene therein, while the quantity of isobutylene present in the other reactor is in excess of the stoichiometric equivalent of the quantity of methanol therein, and the methyl tert-butyl ether so formed is recovered through distillation.

Inventors

  • 👤 Francesco Ancillotti
  • 👤 Gianni Oriani
  • 👤 Ermanno Pescarollo

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 01:38
CPC Classifications
C; C07; C07C; C07C41/00; C07C41/01; C07C41/05; C07C41/06

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 238 words
In a process for the production of methyl tert-butyl ether by reacting isobutylene with methanol at a pressure sufficient to maintain the liquid phase in the presence of a catalyst consisting of an acid ion exchange resin, the improvement which comprises the steps of: (a) reacting in a first reactor in the presence of the catalyst at a temperature of from 60°-70° C (i) methanol and (ii) a mixture comprised of isobutylene, linear olefins, and methanol, the total quantity of methanol being in stoichiometric excess of the quantity of isobutylene; (b) subjecting the product of step (a) to distillation to obtain an off gas comprised of linear olefins and less than 2 percent of isobutylene and a bottoms product comprised of methanol and tert-butyl ether; (c) reacting in a second reactor in the presence of the catalyst at a temperature of from 60° to 70° C the bottoms product of step (b) with a mixture comprised of isobutylene and linear olefins, the space velocity of the mixture being in the range of 20 to 50 LHSV and the respective total quantities of methanol and isobutylene reacted in steps (a) and (c) being stoichiometrically equivalent; and (d) subjecting the product of step (c) to distillation to produce an off gas comprised of isobutylene, linear olefins, and methanol, and a bottoms product comprised of methyl tert-butyl ether, the off gas being recycled as feed to the reactor in step (a).
Claim 2
Dependent Claim 238 words
In a process for the production of methyl tert-butyl ether by reacting isobutylene with methanol at a pressure sufficient to maintain the liquid phase in the presence of a catalyst consisting of an acid ion exchange resin, the improvement which comprises the steps of: (a) reacting in a first reactor in the presence of the catalyst at a temperature of from 60°-70° C (i) methanol and (ii) a mixture comprised of isobutylene, linear olefins, and methanol, the total quantity of methanol being in stoichiometric excess of the quantity of isobutylene; (b) subjecting the product of step (a) to distillation to obtain an off gas comprised of linear olefins and less than 2 percent of isobutylene and a bottoms product comprised of methanol and tert-butyl ether; (c) reacting in a second reactor in the presence of the catalyst at a temperature of from 60° to 70° C the bottoms product of step (b) with a mixture comprised of isobutylene and linear olefins, the space velocity of the mixture being in the range of 20 to 50 LHSV and the respective total quantities of methanol and isobutylene reacted in steps (a) and (c) being stoichiometrically equivalent; and (d) subjecting the product of step (c) to distillation to produce an off gas comprised of isobutylene, linear olefins, and methanol, and a bottoms product comprised of methyl tert-butyl ether, the off gas being recycled as feed to the reactor in step (a).
Claim 3
Dependent Claim 27 words
The process of claim 1 wherein the mixture comprised of isobutylene, linear olefins, and methanol in step (a) consists essentially of the off gas from step (d).
Claim 4
Dependent Claim 48 words
The process of claim 1 wherein the mixture comprised of isobutylene, linear olefins, and methanol in step (a) consists essentially of the off gas from step (d) and a portion of a mixture comprising isobutylene and linear olefins, the remainder of said mixture being introduced in step (c).
Claim 5
Dependent Claim 23 words
The process of claim 1 wherein the ratio by weight of isobutylene to methanol in step (a) is from about 0.62 to 0.72.
Claim 6
Dependent Claim 23 words
The process of claim 1 wherein the ratio by weight of isobutylene to methanol in step (c) is from about 2.35 to 2.8.
Claim 7
Dependent Claim 18 words
The process of claim 1 wherein the space velocity of the mixture in step (a) is 5 LHSV.

References Cited (Backward Citations)

US1968601A Cited
US2480940A Cited
US3119766A Cited
GB957000A Cited
GB1176620A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-01-30 1981-08-01 1982-01-31 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-01-30 1985-08-01 1986-01-31 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-01-30 1989-08-01 1990-01-31 $7700.00 Window Closed / Lapsed

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