Abstract Methyl tert-butyl ether is prepared, and a stream of hydrocarbons containing isobutylene is freed therefrom, by reacting the isobutylene with methanol in a two stage process wherein, in the first stage, a stream of hydrocarbons containing isobutylene and methanol is fed to a primary reaction zone where the isobutylene and methanol partially react in the temperature range of from 50° to 90°C and at a pressure of from 10 to 30 atmospheres in the presence of a catalyst to form methyl tert-butyl ether which is separated by distillation from the residue of isobutylene and methanol and all other hydrocarbons in the feed stream, and, in a second stage, the residue of isobutylene and methanol and other hydrocarbons is fed to a secondary reaction zone where the residue of isobutylene and methanol react in the vapor phase, at a temperature in the range of 60° to 100°C and a pressure of from 15 to 40 atmospheres in the presence of a catalyst consisting of an acid ion exchange resin, to form the balance of methyl tert-butyl ether which is recovered by distillation to leave a balance of other hydrocarbons practically free from isobutylene.
In a process of preparing methyl tert-butyl ether by reacting isobutylene with methanol, the improvement which comprises carrying out said reaction in two stages by feeding a hydrocarbon stream containing isobutylene and methanol to a primary reaction zone at a temperature in the range of from 50° to 90°C and at a pressure in the range of from 10 to 30 atmospheres wherein the isobutylene partially reacts with the methanol in the presence of a catalyst consisting of an acid ion exchange resin to form methyl tert-butyl ether, separating said methyl tert-butyl ether by distillation from the residue of isobutylene and methanol and all other hydrocarbons in the feed stream, feeding said residue and other hydrocarbons to a secondary reaction zone where the residue of isobutylene and methanol are caused to react in the liquid phase in the temperature range of from 60° to 100°C and in the pressure range of from 15 to 40 atmospheres in the presence of a catalyst consisting of an acid ion exchange resin to form additional methyl tert-butyl ether, and then recovering said additional methyl tert-butyl ether by distillation to leave a balance of said other hydrocarbons practically free from isobutylene.
Claim 2
Dependent Claim
197 words
In a process of preparing methyl tert-butyl ether by reacting isobutylene with methanol, the improvement which comprises carrying out said reaction in two stages by feeding a hydrocarbon stream containing isobutylene and methanol to a primary reaction zone at a temperature in the range of from 50° to 90°C and at a pressure in the range of from 10 to 30 atmospheres wherein the isobutylene partially reacts with the methanol in the presence of a catalyst consisting of an acid ion exchange resin to form methyl tert-butyl ether, separating said methyl tert-butyl ether by distillation from the residue of isobutylene and methanol and all other hydrocarbons in the feed stream, feeding said residue and other hydrocarbons to a secondary reaction zone where the residue of isobutylene and methanol are caused to react in the liquid phase in the temperature range of from 60° to 100°C and in the pressure range of from 15 to 40 atmospheres in the presence of a catalyst consisting of an acid ion exchange resin to form additional methyl tert-butyl ether, and then recovering said additional methyl tert-butyl ether by distillation to leave a balance of said other hydrocarbons practically free from isobutylene.
Claim 3
Dependent Claim
19 words
A process as claimed in claim 1, wherein said hydrocarbon stream containing isobutylene is a C 4 olefinic stream.