Tellurium catalyzed decomposition of peroxide intermediates resulting from the autoxidation of unsaturated aldehydes

Claim 2

A process for the preparation of acrylic acid or methacrylic acid which comprises catalytically decomposing the corresponding unsaturated intermediate peroxide compounds peracrylic acid and acrolein monoperacrylate or permethacrylic acid and monopermethacrylate contained in an oxidate solution in the presence of from about 0.01 to about 10.0 per cent by weight of the oxidate reaction mixture of a tellurium catalyst selected from the group consisting of elemental tellurium tellurium nitrate, sulfate, sulfide, disulfide, dichloride, tetrachloride, tetrafluoride, hexafluoride, dibromide, tetrabromide, tetraiodide, dioxide, and trioxide, tellurium oxychloride, tellurium oxybromide, tellurous acid, telluric acid, methyl telluride, dimethyl telluride, diphenyltelluride, tetraphenyl telluride, diphenyl ditelluride, diethyl ditelluride, dimethyl tellurium dichloride, dibromide, diiodide and difluoride, diphenyl telluroxide, phenyl tellurols, 2-chlorocyclohexyltellurium trichloride, aluminum telluride, zinc telluride, bismuth telluride, copper telluride, lithium telluride, palladium telluride and lead telluride, at a temperature of from about ambient to about 100° C., said oxidate solution being derived from the liquid phase autoxidation of acrolein or methacrolein, and recovering the acrylic or methacrylic acid.

Claim 3

A process according to claim 1 wherein the tellurium compounds are selected from diphenyl telluride, tellurium dioxide, tellurium tetrabromide, tellurium tetrachloride, diphenyl ditelluride, diethyl telluride, tellurous acid, bismuth telluride, lead telluride or 2-chlorocyclohexyltellurium trichloride.

Claim 4

A process according to claim 1 wherein from about 0.10 to about 1.0 per cent by weight of catalyst is employed in the oxidate.

Claim 5

A process according to claim 1 wherein an inert organic solvent is employed in the oxidate at concentrations of from about 10 to about 95 weight per cent of the solvent-oxidate mixture and is selected from the group consisting of aliphatic, cycloaliphatic and aromatic hydrocarbons, halogenated hydrocarbons, ethers, esters, carboxylic acids, amides or alcohols or mixtures thereof.

Claim 6

A process according to claim 4 wherein the concentration of solvent is from about 20 to 80 weight per cent of the solvent-oxidate mixture.

Claim 7

A process according to claim 4 wherein the solvent is selected from the group consisting of n-hexane, cyclohexane, n-pentane, xylene, benzene, carbon tetrachloride, dioxane and tertiary butyl alcohol.

Claim 8

A process according to claim 1 wherein the decomposition temperature is in the range of from about 30° C. to 60° C.

Claim 9

A process according to claim 1 wherein the tellurium catalyst is supported.

Claim 10

A process for the preparation of acrylic acid which comprises the steps of: oxidizing acrolein with oxygen or an oxygen-containing gas in the liquid phase to produce a reaction product oxidate containing unreacted acrolein, peracrylic acid, acrolein monoperacrylate, acrylic acid and other by-products; adding from about 20 to 80 weight per cent of an aliphatic, cycloaliphatic or aromatic hydrocarbon, ether, carboxylic acid, amide, alcohol or ester solvent to said oxidate to form a solvent-oxidate mixture; subjecting the solvent-oxidate mixture to a temperature in the range of from about 30° C. to 60° C. in the presence of from about 0.10 to 1.0 per cent by weight of a tellurium catalyst selected from the group consisting of elemental tellurium, tellurium nitrate, sulfate, sulfide, disulfide, dichloride, tetrachloride, tetrafluoride, hexafluoride, dibromide, tetrabromide, tetraiodide, dioxide and trioxide, tellurium oxychloride, tellurium oxybromide, tellurous acid, telluric acid, methyl telluride, dimethyl telluride, diphenyl telluride, tetraphenyl telluride, diphenyl ditelluride, diethyl ditelluride, dimethyl tellurium dichloride, dibromide, diiodide and difluoride, diphenyl telluroxide, phenyl tellurols, 2-chlorocyclohexyltellurium trichloride, aluminum telluride, zinc telluride, bismuth telluride, copper telluride, lithium telluride, palladium telluride and lead telluride, to catalytically decompose peracrylic acid and acrolein monoperacrylate to acrylic acid; and recovering said acrylic acid produced by said oxidation and catalytic decomposition.

Claim 11

A process for the preparation of acrylic acid which comprises the steps of: oxidizing acrolein with oxygen or an oxygen-containing gas in the liquid phase to produce a reaction product oxidate containing unreacted acrolein, peracrylic acid, acrolein monoperacrylate, acrylic acid and other by-products; adding from about 20 to 80 weight per cent of an aliphatic, cycloaliphatic or aromatic hydrocarbon, ether, carboxylic acid, amide, alcohol or ester solvent to said oxidate to form a solvent-oxidate mixture; subjecting the solvent-oxidate mixture to a temperature in the range of from about 30° C. to 60° C. in the presence of from about 0.10 to 1.0 per cent by weight of a tellurium catalyst selected from the group consisting of elemental tellurium, tellurium nitrate, sulfate, sulfide, disulfide, dichloride, tetrachloride, tetrafluoride, hexafluoride, dibromide, tetrabromide, tetraiodide, dioxide and trioxide, tellurium oxychloride, tellurium oxybromide, tellurous acid, telluric acid, methyl telluride, dimethyl telluride, diphenyl telluride, tetraphenyl telluride, diphenyl ditelluride, diethyl ditelluride, dimethyl tellurium dichloride, dibromide, diiodide and difluoride, diphenyl telluroxide, phenyl tellurols, 2-chlorocyclohexyltellurium trichloride, aluminum telluride, zinc telluride, bismuth telluride, copper telluride, lithium telluride, palladium telluride and lead telluride, to catalytically decompose peracrylic acid and acrolein monoperacrylate to acrylic acid; and recovering said acrylic acid produced by said oxidation and catalytic decomposition.

Claim 12

A process according to claim 9 wherein unreacted acrolein in the reaction product oxidate is removed by distillation prior to or during the decomposition step.

Claim 13

A process for the preparation of methacrylic acid which comprises the steps of: oxidizing methacrolein with oxygen or an oxygen-containing gas in the liquid phase to produce a reaction product oxidate containing unreacted methacrolein, permethacrylic acid, methacrolein monopermethacrylate, methacrylic acid and other by-products; adding from about 20 to 80 weight per cent of an aliphatic, cycloaliphatic or aromatic hydrocarbon, ether, carboxylic acid, amide, alcohol or ester solvent to said oxidate to form a solvent-oxidate mixture; subjecting the solvent-oxidate mixture to a temperature in the range of from about 30° C. to 60° C. in the presence of from about 0.10 to 1.0 per cent by weight of a tellurium catalyst selected from the group consisting of elemental tellurium, tellurium nitrate, sulfate, sulfide, disulfide, dichloride, tetrachloride, tetrafluoride, hexafluoride, dibromide, tetrabromide, tetraiodide, dioxide and trioxide, tellurium oxychloride, tellurium oxybromide, tellurous acid, telluric acid, methyl telluride, dimethyl telluride, diphenyl telluride, tetraphenyl telluride, diphenyl ditelluride, diethyl ditelluride, dimethyl tellurium dichloride, dibromide, diiodide and difluoride, diphenyl telluroxide, phenyl tellurols, 2-chlorocyclohexyltellurium trichloride, aluminum telluride, zinc telluride, bismuth telluride, copper telluride, lithium telluride, palladium telluride and lead telluride, to catalytically decompose permethacrylic acid and methacrolein monopermethacrylate to methacrylic acid; and recovering said methacrylic acid produced by said oxidation and catalytic decomposition.

Claim 14

A process for the preparation of methacrylic acid which comprises the steps of: oxidizing methacrolein with oxygen or an oxygen-containing gas in the liquid phase to produce a reaction product oxidate containing unreacted methacrolein, permethacrylic acid, methacrolein monopermethacrylate, methacrylic acid and other by-products; adding from about 20 to 80 weight per cent of an aliphatic, cycloaliphatic or aromatic hydrocarbon, ether, carboxylic acid, amide, alcohol or ester solvent to said oxidate to form a solvent-oxidate mixture; subjecting the solvent-oxidate mixture to a temperature in the range of from about 30° C. to 60° C. in the presence of from about 0.10 to 1.0 per cent by weight of a tellurium catalyst selected from the group consisting of elemental tellurium, tellurium nitrate, sulfate, sulfide, disulfide, dichloride, tetrachloride, tetrafluoride, hexafluoride, dibromide, tetrabromide, tetraiodide, dioxide and trioxide, tellurium oxychloride, tellurium oxybromide, tellurous acid, telluric acid, methyl telluride, dimethyl telluride, diphenyl telluride, tetraphenyl telluride, diphenyl ditelluride, diethyl ditelluride, dimethyl tellurium dichloride, dibromide, diiodide and difluoride, diphenyl telluroxide, phenyl tellurols, 2-chlorocyclohexyltellurium trichloride, aluminum telluride, zinc telluride, bismuth telluride, copper telluride, lithium telluride, palladium telluride and lead telluride, to catalytically decompose permethacrylic acid and methacrolein monopermethacrylate to methacrylic acid; and recovering said methacrylic acid produced by said oxidation and catalytic decomposition.

Claim 15

A process according to claim 11 wherein the unreacted methacrolein in the reaction product oxidate is removed and recovered by distillation prior to or during the decompostion step.