Cyclic process for production of alkylene oxide using electrolysis of brine

Claim 2

In a process integrating an electrolytic process for the production of chlorine with a chlorohydrin process for producing an epoxy compound wherein a chlorohydrin is converted to a corresponding epoxy compound by contact with an aqueous solution of sodium chloride and sodium hydroxide from a chlorine producing electrolytic cell, the improvement comprising: recovering an expoxy compound and an aqueous brine solution from the chlorohydrin conversion, said aqueous brine solution containing organic impurities; contacting said aqueous brine solution with gaseous chlorine to oxidize the organic impurities to move volatile organic compounds; stripping volatile organic compounds from the aqueous brine solution; and introducing the aqueous brine solution into the electrolytic cell.

Claim 3

The process of claim 1 wherein the organic impurities are converted to volatile organic compounds having a boiling point no greater than 150° C.

Claim 4

The process of claim 2 wherein the chlorine is employed in an amount less than the stoichiometric amount for converting the organic impurities to carbon dioxide.

Claim 5

The process of claim 1 wherein the brine solution is contacted with chlorine at a temperature of from 120° F. to 240° F.

Claim 6

The process of claim 1 wherein the contacting and stripping are effected simultaneously.

Claim 7

The process of claim 1 wherein the chlorohydrin is propylene chlorohydrin.

Claim 8

In a process integrating an electrolytic process for the production of chlorine with a chlorohydrin process for producing an epoxy compound wherein a tertiary alkanol is contacted with gaseous chlorine and an aqueous solution of sodium chloride and sodium hydroxide from an electrolytic cell to produce tertiary alkyl hypochlorite, said hypochlorite is contacted with an olefinically unsaturated compound and water to produce a chlorohydrin, and chlorohydrin is contacted with an aqueous solution of sodium chloride and sodium hydroxide from the electrolytic cell to produce an epoxy compound, the improvement comprising: recovering a first brine solution from the hypochlorite production, said first brine solution including organic impurities; recovering a second brine solution from the epoxy production, said second brine solution including organic impurities; contacting combined first and second brine solution with gaseous chlorine to oxidize organic impurities to more volatile organic compounds; stripping volatile organic compounds from the combined aqueous brine solution; and introducing combined aqueous brine solution into the electrolytic cell.

Claim 9

In a process integrating an electrolytic process for the production of chlorine with a chlorohydrin process for producing an epoxy compound wherein a tertiary alkanol is contacted with gaseous chlorine and an aqueous solution of sodium chloride and sodium hydroxide from an electrolytic cell to produce tertiary alkyl hypochlorite, said hypochlorite is contacted with an olefinically unsaturated compound and water to produce a chlorohydrin, and chlorohydrin is contacted with an aqueous solution of sodium chloride and sodium hydroxide from the electrolytic cell to produce an epoxy compound, the improvement comprising: recovering a first brine solution from the hypochlorite production, said first brine solution including organic impurities; recovering a second brine solution from the epoxy production, said second brine solution including organic impurities; contacting combined first and second brine solution with gaseous chlorine to oxidize organic impurities to more volatile organic compounds; stripping volatile organic compounds from the combined aqueous brine solution; and introducing combined aqueous brine solution into the electrolytic cell.

Claim 10

The process of claim 7 wherein the organic impurities are converted to volatile organic compounds having a boiling point no greater than 150° C.

Claim 11

The process of claim 8 wherein the chlorine is employed in an amount less than the stoichiometric amount for converting the organic impurities to carbon dioxide.

Claim 12

The process of claim 9 wherein the brine solution is contacted with chlorine at a temperature of from 120° F. to 240° F.

Claim 13

The process of claim 10 wherein the olefin is propylene and the organic impurities include tertiary alkanol and propylene glycol.

Claim 14

The process of claim 10 wherein the contacting and stripping are effected simultaneously.