Process for separating dimethyl ether from a hydrocarbon mixture containing the same

Claim 2

A process for separating dimethyl ether from a hydrocarbon mixture containing the same which comprises contacting said hydrocarbon mixture with an aqueous solution containing a polar oxygenated hydrocarbon having a polarity of about 1.4 to about 2.0 Debyes.

Claim 3

The process of claim 1 wherein said polar oxygenated hydrocarbon has a polarity of about 1.4 to about 1.7 Debyes.

Claim 4

The process of claim 1 wherein said polar oxygenated hydrocarbon is selected from the group consisting of alcohols having 1 to 3 carbon atoms.

Claim 5

The process of claim 3 wherein said polar oxygenated hydrocarbon is an alcohol having from 1 to 2 carbon atoms.

Claim 6

The process of claim 4 wherein said polar oxygenated hydrocarbon is methanol.

Claim 7

The process of claim 4 wherein said hydrocarbon mixture contains from about 10 to 2000 ppm of dimethyl ether.

Claim 8

The process of claim 6 wherein said hydrocarbon mixture contains from about 200 to about 600 ppm dimethyl ether.

Claim 9

The process of claim 1 wherein said hydrocarbon mixture contains hydrocarbons having from 3 to 6 carbon atoms.

Claim 10

The process of claim 8 wherein said hydrocarbon mixture contains hydrocarbons having from 3 to 5 carbon atoms.

Claim 11

The process of claim 8 wherein said hydrocarbon mixture is composed of a stream containing at least one olefin, methanol and dimethyl ether.

Claim 12

The process of claim 10 wherein said olefin is isobutylene.

Claim 13

The process of claim 1 wherein said aqueous solution contains from about 0.5 to about 40 weight percent of said polar oxygenated hydrocarbon.

Claim 14

The process of claim 12 wherein said aqueous solution contains from about 2 to about 10 weight percent of said polar oxygenated hydrocarbon.

Claim 15

The process of claim 1 wherein the weight ratio of said aqueous solution to said hydrocarbon mixture is in the range of about 1:1 to about 5:1.

Claim 16

The process of claim 14 wherein the weight ratio of said aqueous solution to said hydrocarbon mixture is in the range of about 1.5:1 to about 3:1.

Claim 17

The process of claim 1 wherein said contact is carried out of a temperature of about 35° to about 180° F. and a pressure higher than about 65 psia.

Claim 18

The process of claim 16 wherein said contact is carried out at a temperature of about 70° to about 100° F. and a pressure of about 100 to about 200 psia.

Claim 19

The process of claim 1 wherein said hydrocarbon mixture contains hydrocarbons having from 3 to 6 carbon atoms and from about 10 to about 2000 ppm of dimethyl ether, said aqueous solution contains from about 0.5 to about 40 weight percent of said polar oxygenated hydrocarbon and weight ratio of said aqueous solution to said hydrocarbon mixture is in the range of about 1:1 to about 5:1.

Claim 20

The process of claim 18 wherein said hydrocarbon mixture contains hydrocarbons having from 3 to 5 carbon atoms and from about 200 to about 600 ppm of dimethyl ether, said polar oxygenated compound has a polarity of about 1.4 to about 1.7 Debyes, said aqueous solution contains from about 2 to about 10 weight percent of said polar oxygenated hydrocarbon and the weight ration of said aqueous solution to said hydrocarbon mixture is in the range of about 1.5:1 to about 3:1.

Claim 21

The process of claim 18 wherein said polar oxygenated compound is an alcohol.

Claim 22

The process of claim 19 wherein said polar oxygenated compound is an alcohol.

Claim 23

The process of claim 20 wherein said alcohol is methanol.

Claim 24

The process of claim 21 wherein said alcohol is methanol.

Claim 25

In a process wherein a hydrocarbon stream containing from 3 to 6 carbon atoms, including isobutylene, is treated with methanol, to obtain a product mixture containing unreacted hydrocarbons, methyl tertiary butyl ether, unreacted methanol, and dimethyl ether, and wherein methyl tertiary butyl ether is separated from said product mixture, the improvement which comprises contacting the remainder of said product mixture, after said separation, with an aqueous solution containing a polar oxygenated hydrocarbon having a polarity of about 1.4 to about 2.0 Debyes to remove dimethyl ether therefrom and thereafter subjecting the remaining product to extraction with water to remove methanol therefrom.

Claim 26

In a process wherein a hydrocarbon stream containing from 3 to 6 carbon atoms, including isobutylene, is treated with methanol, to obtain a product mixture containing unreacted hydrocarbons, methyl tertiary butyl ether, unreacted methanol, and dimethyl ether, and wherein methyl tertiary butyl ether is separated from said product mixture, the improvement which comprises contacting the remainder of said product mixture, after said separation, with an aqueous solution containing a polar oxygenated hydrocarbon having a polarity of about 1.4 to about 2.0 Debyes to remove dimethyl ether therefrom and thereafter subjecting the remaining product to extraction with water to remove methanol therefrom.

Claim 27

The process of claim 24 wherein said polar oxygenated hydrocarbon has a polarity of about 1.4 to about 1.7 Debyes.

Claim 28

The process of claim 25 wherein said polar oxygenated hydrocarbon is methanol.

Claim 29

The process of claim 24 wherein the remainder of said product after removal of methanol therefrom is passed to a hydrofluoric acid alkylation unit.