Process for preparing glycols from their ester precursors

Claim 2

In a process for preparing vicinal glycol mono- and diesters of olefins which comprises contacting an olefin containing 2 to 30 carbon atoms and a molecular oxygen containing gas in an oxidation zone with a carboxylic acid containding 2 to 6 carbon atoms in the liquid phase in the presence of a halogen selected from the group consisting of bromine, and a bromine-containing compound capable of producing bromide ions in solution in the oxidation zone, and a variable metal cation selected from the group consisting of tellurium, cerium, antimony, manganese, vanadium, gallium, arsenic, cobalt, copper, selenium, chromium and silver, and a liquid effluent is continuously removed from said oxidation zone, the improvement which comprises separating from said effluent a residue having a higher boiling point than said mono- and diesters, and contacting said residue with water to produce additional vicinal glycol of said olefin.

Claim 3

In a process for preparing vicinal glycol mono- and diesters of olefins which comprises contacting an olefin containing 2 to 30 carbon atoms and a molecular oxygen containing gas in an oxidation zone with a carboxylic acid containing 2 to 6 carbon atoms in the liquid phase in the presence of a halogen selected from the group consisting of bromine and a bromine-containing compound capable for producing bromide ions in solution in the oxidation zone, and a variable valent metal cation selected from the group consisting of tellurium, cerium, antimony, manganese, vanadium, gallium, arsenic, cobalt, copper, selenium, chromium and silver, and a liquid effluent is continuously removed from said oxidation zone, the improvement which comprises separating from said effluent a stream comprising precursor light components contained in said effluent and having lower boiling points than said mono- and diesters, and contacting said precursor light components with water to produce additional vicinal glycol of said olefin.

Claim 4

In a process for preparing vicinal glycol mono- and diesters of olefins which comprises contacting an olefin containing 2 to 30 carbon atoms and a molecular oxygen containing gas in an oxidation zone with a carboxylic acid containing 2 to 6 carbon atoms in the liquid phase in the presence of a halogen selected from the group consisting of bromine and a bromine-containing compound capable for producing bromide ions in solution in the oxidation zone, and a variable valent metal cation selected from the group consisting of tellurium, cerium, antimony, manganese, vanadium, gallium, arsenic, cobalt, copper, selenium, chromium and silver, and a liquid effluent is continuously removed from said oxidation zone, the improvement which comprises separating from said effluent a stream comprising precursor light components contained in said effluent and having lower boiling points than said mono- and diesters, and contacting said precursor light components with water to produce additional vicinal glycol of said olefin.

Claim 5

A process for preparing vicinal glycol mono- and diesters of olefins by contacting a vapor feed of an olefin containing 2 to 30 carbon atoms and a molecular oxygen containing gas in an oxidation zone with a carboxylic acid containing 2 to 6 carbon atoms in the liquid phase in the presence of a halogen selected from the group consisting of bromine and bromine-containing compound capable of producing bromide ions in solution in the oxidation zone and a variable valent metal cation selected from the group consisting of tellurium, cerium, antimony, manganese, vanadium, gallium, arsenic, cobalt, copper, selenium, chromium, and silver, and a liquid effluent is continuously removed from said oxidation zone, the improvement which comprises: separating from said effluent a residue having a higher boiling point than said mono- and diesters, separating from said effluent said carboxylic acid contained in said effluent, separating from said effluent the glycol mono- and diesters, separating from said effluent a stream comprising precursor light components contained in said effluent and having a lower boiling point than said mono- and diesters, and contacting at least one of said residue and said precursor light components with water at an elevated temperature to produce vicinal glycol of said olefin.

Claim 6

A process for preparing vicinal glycol mono- and diesters of olefins by contacting a vapor feed of an olefin containing 2 to 30 carbon atoms and a molecular oxygen containing gas in an oxidation zone with a carboxylic acid containing 2 to 6 carbon atoms in the liquid phase in the presence of a halogen selected from the group consisting of bromine and bromine-containing compound capable of producing bromide ions in solution in the oxidation zone and a variable valent metal cation selected from the group consisting of tellurium, cerium, antimony, manganese, vanadium, gallium, arsenic, cobalt, copper, selenium, chromium, and silver, and a liquid effluent is continuously removed from said oxidation zone, the improvement which comprises: separating from said effluent a residue having a higher boiling point than said mono- and diesters, separating from said effluent said carboxylic acid contained in said effluent, separating from said effluent the glycol mono- and diesters, separating from said effluent a stream comprising precursor light components contained in said effluent and having a lower boiling point than said mono- and diesters, and contacting at least one of said residue and said precursor light components with water at an elevated temperature to produce vicinal glycol of said olefin.

Claim 7

In a process for preparing ethylene glycol diacetate and ethylene glycol monoacetate which comprises contacting ethylene and a molecular oxygen containing gas in an oxidation zone with acetic acid in the liquid phase in the presence of a bromine containing compound capable of producing bromide ions in solution in the oxidation zone and tellurium cation, and a liquid effluent is continuously removed from said oxidation zone, the improvement which comprises: separating from said effluent a residue having a higher boiling point than said ethylene glycol monoacetate and diacetate, separating from said effluent said carboxylic acid contained in said effluent, separating from said effluent said ethylene glycol monoacetate and diacetate, separating from said effluent a stream comprising precursor light components contained in said effluent, and having lower boiling points than said monoacetate and diacetate, and contacting at least one of said residue and said precursor light components with water to produce the ethylene glycol.

Claim 8

In a process for preparing ethylene glycol diacetate and ethylene glycol monoacetate which comprises contacting ethylene and a molecular oxygen containing gas in an oxidation zone with acetic acid in the liquid phase in the presence of a bromine containing compound capable of producing bromide ions in solution in the oxidation zone and tellurium cation, and a liquid effluent is continuously removed from said oxidation zone, the improvement which comprises: separating from said effluent a residue having a higher boiling point than said ethylene glycol monoacetate and diacetate, separating from said effluent said carboxylic acid contained in said effluent, separating from said effluent said ethylene glycol monoacetate and diacetate, separating from said effluent a stream comprising precursor light components contained in said effluent, and having lower boiling points than said monoacetate and diacetate, and contacting at least one of said residue and said precursor light components with water to produce the ethylene glycol.

Claim 9

In a process for preparing vicinal glycol mono- and diesters of olefins which comprises contacting an olefin containing 2 to 30 carbon atoms and a molecular oxygen containing gas in an oxidation zone with a carboxylic acid containing 2 to 6 carbon atoms in the liquid phase in the presence of a halogen selected from the group consisting of bromine, chlorine, a bromine-containing compound and a chlorine-containing compound, said compounds being capable of producing, respectively, bromide ions and chloride ions in solution in the oxidation zone, and a variable valent cation selected from the group consisting tellurium, cerium, antimony, manganese, vanadium, gallium, arsenic, cobalt, copper, selenium, chromium and silver, and a liquid effluent is continuously removed from said oxidation zone, the improvement which comprises: separating from said effluent a residue having a higher boiling point than said mono- and diesters, and contacting said residue with water to produce additional vicinal glycol of said olefin.

Claim 10

In a process for preparing vicinal glycol mono- and diesters of olefins which comprises contacting an olefin containing 2 to 30 carbon atoms and a molecular oxygen containing gas in an oxidation zone with a carboxylic acid containing 2 to 6 carbon atoms in the liquid phase in the presence of a halogen selected from the group consisting of bromine, chlorine, a bromine-containing compound and a chlorine-containing compound, said compounds being capable of producing, respectively, bromide ions and chloride ions in solution in the oxidation zone, and a variable valent cation selected from the group consisting tellurium, cerium, antimony, manganese, vanadium, gallium, arsenic, cobalt, copper, selenium, chromium and silver, and a liquid effluent is continuously removed from said oxidation zone, the improvement which comprises: separating from said effluent a residue having a higher boiling point than said mono- and diesters, and contacting said residue with water to produce additional vicinal glycol of said olefin.

Claim 11

The process of claim 5 wherein said oxidation is maintained at from about 90° C. to about 180° C.

Claim 12

The process of claim 5 wherein the olefin is a lower olefin of from 2 to 5 carbon atoms.

Claim 13

The process of claim 5 wherein said olefin is ethylene.

Claim 14

In a process for preparing vicinal glycol mono- and diesters of olefins which comprises contacting an olefin containing 2 to 30 carbon atoms and a molecular oxygen containing gas in an oxidation zone with a carboxylic acid containing 2 to 6 carbon atoms in the liquid phase in the presence of a halogen selected from the group consisting of bromine, chlorine, a bromine-containing compound and a chlorine-containing compound, said compounds being capable of producing, respectively, bromide ions and chloride ions in solution in the oxidation zone, and a variable valent cation selected from the group consisting of tellurium, cerium, antimony, manganese, vanadium, gallium, arsenic, cobalt, copper, selenium, chromium and silver, and a liquid effluent is continuously removed from said oxidation zone, the improvement which comprises: separating from said effluent a stream a comprising precursor light components contained in said effluent, and having lower boiling points than said mono- and diesters, and contacting said precursor light components with water to produce additional vicinal glycol of said olefin.

Claim 15

In a process for preparing vicinal glycol mono- and diesters of olefins which comprises contacting an olefin containing 2 to 30 carbon atoms and a molecular oxygen containing gas in an oxidation zone with a carboxylic acid containing 2 to 6 carbon atoms in the liquid phase in the presence of a halogen selected from the group consisting of bromine, chlorine, a bromine-containing compound and a chlorine-containing compound, said compounds being capable of producing, respectively, bromide ions and chloride ions in solution in the oxidation zone, and a variable valent cation selected from the group consisting of tellurium, cerium, antimony, manganese, vanadium, gallium, arsenic, cobalt, copper, selenium, chromium and silver, and a liquid effluent is continuously removed from said oxidation zone, the improvement which comprises: separating from said effluent a stream a comprising precursor light components contained in said effluent, and having lower boiling points than said mono- and diesters, and contacting said precursor light components with water to produce additional vicinal glycol of said olefin.

Claim 16

A process for preparing vicinal glycol mono- and diesters of olefins by contacting a vapor feed of an olefin containing 2 to 30 carbon atoms and a molecular oxygen containing gas in an oxidation zone with a carboxylic acid containing 2 to 6 carbon atoms in the liquid phase in the presence of a halogen selected from the group consisting of bromine, chlorine, a bromine-containing compound and a chlorine-containing compound, said compounds being capable fo producing, respectively, bromide ions and chloride ions in solution in the oxidation zone and a variable valent cation selected from the group consisting of tellurium, cerium, antimony, manganese, vanadium, gallium, arsenic, cobalt, copper, selenium, chromium and silver, and a liquid effluent is continuously removed from said oxidation zone, the improvement which comprises: separating from said effluent a residue having a higher boiling point than said mono- and diesters, separating from said effluent said carboxylic acid contained in said effluent, separating from said effluent the vicinal glycol mono- and diesters, separating from said effluent a stream comprising precursor light components contained in said effluent, and having lower boiling points than said mono- and diesters, and contacting at least one of said residue and said precursor light components with water at an elevated temperature to produce vicinal glycol.

Claim 17

A process for preparing vicinal glycol mono- and diesters of olefins by contacting a vapor feed of an olefin containing 2 to 30 carbon atoms and a molecular oxygen containing gas in an oxidation zone with a carboxylic acid containing 2 to 6 carbon atoms in the liquid phase in the presence of a halogen selected from the group consisting of bromine, chlorine, a bromine-containing compound and a chlorine-containing compound, said compounds being capable fo producing, respectively, bromide ions and chloride ions in solution in the oxidation zone and a variable valent cation selected from the group consisting of tellurium, cerium, antimony, manganese, vanadium, gallium, arsenic, cobalt, copper, selenium, chromium and silver, and a liquid effluent is continuously removed from said oxidation zone, the improvement which comprises: separating from said effluent a residue having a higher boiling point than said mono- and diesters, separating from said effluent said carboxylic acid contained in said effluent, separating from said effluent the vicinal glycol mono- and diesters, separating from said effluent a stream comprising precursor light components contained in said effluent, and having lower boiling points than said mono- and diesters, and contacting at least one of said residue and said precursor light components with water at an elevated temperature to produce vicinal glycol.