Preparation of esters of unsaturated alcohols

Claim 2

A process for the production of esters of monoolefinically unsaturated alcohols which comprises reacting a conjugated diolefin with an organic acid reactant under reaction conditions in the substantial absence of oxygen and employing catalytic amounts of a catalyst system consisting essentially of a copper ion, an alkali metal ion, and a halide, wherein said conjugated diolefin is an acyclic conjugated diolefin represented by the formula ##STR4## or a cyclic conjugated diolefin represented by the formula ##STR5## wherein each R is individually selected from hydrogen, halogen, cyano, --COOR', and the monovalent hydrocarbyl radicals, wherein R' is hydrogen, or alkyl or aryl hydrocarbon radical, and n has the value of 1 to 12, and wherein said organic acid reactant is a monocarboxylic acid R"COOH, a dicarboxylic acid R"'(COOH) 2 , a corresponding anhydride, or both; wherein R" is an alkyl, cycloalkyl, aryl, or combination radical, or the halogen, cyano, or -COOR' derivative thereof, wherein the R" radical can contain up to 4 such substituents; wherein said R"' is a valence bond, or an alkylene, cycloalkylene, arylene, or combination radical, wherein R"' further can contain up to 4 substituents selected from the group consisting of halogen, cyano, and --COOR', and employing a catalyst concentration expressed in terms of the amount of copper ion:conjugated diolefin charged in the range of about 0.01 mol percent up to an equimolar amount.

Claim 3

The process according to claim 1 wherein said acyclic conjugated diolefin contains 4 to 16 carbon atoms per molecule, and said cyclic conjugated diolefins contain 5 to 16 carbon atoms per molecule, such that the total number of carbon atoms in all R substituents does not exceed 12.

Claim 4

The process according to claim 2 wherein said conjugated diolefin is a said acyclic conjugated diolefin and is selected from the group consisting of 1,3-butadiene, 2-methyl-1,3-butadiene, 2-chloro-1,3-butadiene, 2-ethyl-1,3-butadiene, 2-chloro-3-methyl-1,3-butadiene, 1,4-diphenyl-1,3-butadiene, 1,3-hexadiene, 1,3-pentadiene, 1,3-octadiene, 2-cyano-1,3-butadiene, 2-carbethoxy-1,3-butadiene, 2-cyclohexyl-1,3-butadiene, 2-methylene-3-butenoic acid, and 2,4-pentadienenitrile.

Claim 5

The process according to claim 2 wherein said conjugated diolefin is a said cyclic conjugated diolefin and is selected from the group consisting of 1,3-cyclohexadiene, 1,3-cyclooctadiene, 1,3-cyclododecadiene, cyclopentadiene, 5-methyl-1,3-cyclohexadiene, 2,4-cyclohexadiene-1,2-dicarboxylic acid, and 5,6,7,8-tetrabromo-1,3-cyclooctadiene.

Claim 6

The process according to claim 4 wherein said organic acid reactant is said monocarboxylic acid, or said monocarboxylic acid plus the corresponding anhydride, said monocarboxylic acid contains up to 18 carbon atoms per molecule, and is selected from the group consisting of acetic acid, propanoic acid, butanoic acid, pentanoic acid, hexanoic acid, octanoic acid, dodecanoic acid, octadecanoic acid, cyclopentanecarboxylic acid, cyclohexanecarboxylic acid, benzoic acid, chloroacetic acid, cyanoacetic acid, trichloroacetic acid, 2-bromododecanoic acid, 2-ethylhexanoic acid, 2-bromobutanoic acid, ethyl hydrogen adipate, 4-chlorobenzoic acid, 4-cyanobenzoic acid, 2,3,4,5-tetrachlorobenzoic acid, and ethyl hydrogen-o-phthalate.

Claim 7

The process according to claim 2 wherein said organic acid reactant is said dicarboxylic acid, said dicarboxylic acid contains up to 18 carbon atoms per molecule, and is selected from the group consisting of oxalic acid, succinic acid, hexanedioic acid, and terephthalic acid.

Claim 8

The process according to claim 1 wherein said copper ion is cuprous or cupric, and is supplied by a copper compound selected from the group consisting of copper halides, oxides, hydroxides, nitrates, carbonates, sulfates, orthophosphates, and hydrocarbon carboxylates.

Claim 9

The process according to claim 7 wherein said copper compound is selected from the group consisting of copper acetate, copper bromide, copper benzoate, copper butanoate, copper chloride, copper dodecanoate, copper octadecanoate, copper sulfate, copper nitrate, copper orthophosphate, copper oxide, copper salicylate, copper iodide, and copper carbonate, and wherein said copper in said copper compound is chosen from the group consisting of cuprous and cupric.

Claim 10

The process according to claim 1 wherein said alkali metal ion is selected from the group consisting of lithium, sodium, potassium, rubidium, and cesium, and said alkali metal ion is supplied by an alkali metal compound selected from the group consisting of alkali metal halides, oxides, hydroxides, hydrocarbon carboxylates, nitrates, sulfates, and orthophosphates.

Claim 11

The process according to claim 9 wherein said alkali metal compound is selected from the group consisting of lithium chloride, lithium bromide, lithium iodide, lithium nitrate, lithium hydroxide, lithium orthophosphate, lithium acetate, lithium benzoate, lithium oxide, lithium sulfate, lithium octadecanoate, sodium chloride, sodium nitrate, sodium bromide, sodium sulfate, sodium acetate, potassium chloride, potassium nitrate, potassium acetate, potassium sulfate, potassium benzoate, rubidium nitrate, rubidium chloride, rubidium sulfate, rubidium bromide, rubidium acetate, cessium nitrate, cesium chloride, cesiium acetate, cesium sulfate, and cesium oxide.

Claim 12

The process according to claim 1 wherein said halide is a chloride, bromide, or iodide, supplied by a halide providing compound selected from the group consisting of cuprous or cupric halide, alkali metal halides, alkaline earth metal halides, ammonium halides, or mixtures.

Claim 13

The process according to claim 1 wherein said effective catalyst ratios are represented by a molar ratio of alkali metal ion:copper ion in the range of about 0.1:1 to 100:1, and a molar ratio of halide ion:copper ion in the range of about 0.1:1 to 100:1.

Claim 14

The process according to claim 12 wherein each of said ratios is in the range of about 1:1 to 5:1.

Claim 15

The process according to claim 12 employing a ratio of said organic acid reactant to said conjugated diene is in the molar range of about 1:1 to 500:1.

Claim 16

The process of claim 14 wherein said molar range is about 2:1 to 10:1.

Claim 17

The process according to claim 15 wherein the mol ratio of said copper ion:conjugated diolefin charged is in the range of about 1 to 50 mol percent.

Claim 18

The process according to claim 15 wherein said reaction conditions include a contacting temperature in the range of about 30° to 250° C.

Claim 19

The process according to claim 17 wherein said copper ion is supplied by cupric acetate, said alkali metal is lithium, said halide is bromide, said conjugated diene is butadiene, and said carboxylic acid is acetic acid, wherein said products comprise acetate esters of 3-buten-2-ol and 2-buten-1-ol.

Claim 20

The process according to claim 17 wherein said copper ion is supplied by cuprous chloride, said alkali metal ion is a lithium ion, said halide is chloride, said conjugated diene is butadiene, and said carboxylic acid is acetic acid, wherein said products comprise acetate esters of 3-buten-2-ol and 2-buten-1-ol

Claim 21

The process according to claim 17 wherein said copper ion is supplied by cuprous oxide, said alkali metal ion is a lithium ion, said halide is bromide, said conjugated diene is butadiene, and said carboxylic acid is acetic acid, wherein said products comprise acetate esters of 3-buten-2-ol and 2-buten-1-ol

Claim 22

The process according to claim 17 wherein said copper ion is supplied by cuprous iodide, said alkali metal ion is a lithium ion, said halide is iodide, said conjugated diene is butadiene, and said carboxylic acid is acetic acid, wherein said products comprise acetate esters of 3-buten-2-ol and 2-buten-1-ol.

Claim 23

The process of claim 1 wherein said catalyst system is a supported catalyst employing a support of silica, zeolite, or diatomaceous earth.

Claim 24

A process for the production of esters of monoolefinically unsaturated alcohols which comprises reacting a conjugated diolefin with an organic acid reactant under reaction conditions in the substantial absence of oxygen, and employing catalytic amounts of a catalyst system consisting essentially of a copper ion, an alkali metal ion, and a halide, wherein said conjugated diolefin is an acyclic conjugated diolefin represented by the formula ##STR6## or a cyclic conjugated diolefin represented by the formula ##STR7## wherein each R is individually selected from hydrogen, halogen, cyano, --COOR', and the monovalent hydrocarbyl radicals, wherein R' is hydrogen, or an alkyl or aryl hydrocarbon radical of up to 10 carbon atoms, and n has the value of 1 to 12, wherein said organic acid reactant is a monocarboxylic acid R"COOH, a dicarboxylic acid R"'(COOH) 2 , a corresponding anhydride, or both; wherein R" is an alkyl, cycloalkyl, aryl, or combination radical, or the halogen, cyano, or --COOR' derivative thereof, wherein the R" radical can contain up to 4 such substituents; wherein said R"' is a valence bond, or an alkylene, cycloalkylene, arylene, or combination radical wherein R"' further can contain up to 4 substitutents selected from the group consisting of halogen, cyano, and --COOR', wherein R' is hydrogen, alkyl, or aryl hydrocarbon radical of up to 10 carbon atoms, and wherein said reaction conditions include a contacting temperature in the range of about 30° C. to 250° C., and employing a catalyst concentration expressed in terms of the amount of copper ion:conjugated diolefin charge in the range of about 0.01 mol percent up to an equimolar amount.

Claim 25

A process for the production of esters of monoolefinically unsaturated alcohols which comprises reacting a conjugated diolefin with an organic acid reactant under reaction conditions in the substantial absence of oxygen, and employing catalytic amounts of a catalyst system consisting essentially of a copper ion, an alkali metal ion, and a halide, wherein said conjugated diolefin is an acyclic conjugated diolefin represented by the formula ##STR6## or a cyclic conjugated diolefin represented by the formula ##STR7## wherein each R is individually selected from hydrogen, halogen, cyano, --COOR', and the monovalent hydrocarbyl radicals, wherein R' is hydrogen, or an alkyl or aryl hydrocarbon radical of up to 10 carbon atoms, and n has the value of 1 to 12, wherein said organic acid reactant is a monocarboxylic acid R"COOH, a dicarboxylic acid R"'(COOH) 2 , a corresponding anhydride, or both; wherein R" is an alkyl, cycloalkyl, aryl, or combination radical, or the halogen, cyano, or --COOR' derivative thereof, wherein the R" radical can contain up to 4 such substituents; wherein said R"' is a valence bond, or an alkylene, cycloalkylene, arylene, or combination radical wherein R"' further can contain up to 4 substitutents selected from the group consisting of halogen, cyano, and --COOR', wherein R' is hydrogen, alkyl, or aryl hydrocarbon radical of up to 10 carbon atoms, and wherein said reaction conditions include a contacting temperature in the range of about 30° C. to 250° C., and employing a catalyst concentration expressed in terms of the amount of copper ion:conjugated diolefin charge in the range of about 0.01 mol percent up to an equimolar amount.