Polymerization process for cis-1,4-polybutadiene using cycloalkane solvents and an aromatic polymerization regulator

Claim 2

An improved process of polymerizing butadiene-1,3 to produce primarily linear, gel-free cis-1,4-polybutadiene which is carried out in the presence of a catalyst comprising a cobalt compound, at least one organo-aluminum compound and water, the improvement which comprises carrying out the polymerization reaction in a cycloalkane having 5 to 8 carbon atoms containing 0 to 80 percent, based on the weight of cycloalkane, of a secondary solvent selected from the group consisting of a saturated aliphatic hydrocarbon and an α-monoolefin having 4 to 10 carbon atoms and from 0.1 to 2 percent, based on the weight of total solvent, of an alkyl substituted benzene having 1 to 4 alkyl substituents of 1 to 4 carbon atoms.

Claim 3

A process of claim 1 wherein the cycloalkane is cyclohexane.

Claim 4

A process of claim 1 wherein the alkyl substituted benzene has two or three methyl or ethyl groups.

Claim 5

A process of claim 3 wherein the cyclic aliphatic solvent is cyclohexane.

Claim 6

A process of claim 4 wherein the alkyl substituted benzene is o-, m-, or p-xylene, mesitylene diethylbenzene, or any mixture thereof.

Claim 7

A process of claim 4 wherein the ratio of aluminum to cobalt is in the range of from 50:1 to 300:1, and the ratio of water to aluminum is in the range of from 0.25:1 to 0.55:1.

Claim 8

A process of claim 6 wherein the alkyl substituted benzene is o-, m-, or p-xylene, mesitylene, 1,2-, 1,3- or 1,4-diethylbenzene, or any mixture thereof, employing additionally 20 to 50 percent of an α-monoolefin having 4 to 10 carbons as a secondary solvent and 0.1 to 2.0 percent of a non-conjugated dienes or a cyclic diene as a molecular weight modifier.

Claim 9

A process of claim 1 which comprises the steps of (a) dissolving a cobalt compound in wet butadiene-1,3 such that the aluminum to cobalt ratio is 50-800:1, the chlorine to aluminum ratio is 0.7-1.5:1 and the water to aluminum ratio is 0.1 to 0.8:1, (b) adding dry butadiene-1,3 to the wet butadiene which contains the pre-dissolved cobalt, (c) adding to the previous mixture solvent which contains 0.1 to 2.0 percent of an alkyl substituted benzene, 20 to 50 percent, based on the weight of cyclohexane, of an α-monoolefin having 4 to 10 carbon atoms and 0.1 to 2.0 percent, based on the weight of cyclohexane, of a non-conjugated diene or a cyclic diene, (d) adding to the above reaction mixture an organo-aluminum compound, and (e) polymerizing said butadiene-1,3 to a conversion of 30 to 90% thereby producing the substantially linear polymer.

Claim 10

A process of claim 8 wherein the solvent is a mixture of cyclohexane and butene-1, alkyl substituted benzene is o-, m-, or p-xylene, mesitylene, 1,2-, 1,3- or 1,4-diethylbenzene or any mixture thereof and the molecular weight modifier is 1,5-cyclooctadiene.

Claim 11

A process of claim 9 wherein the ratio of aluminum to cobalt is in the range of from 100:1 to 200:1, and the ratio of water to aluminum is in the range of from 0.20:1 to 0.55:1.

Claim 12

A process of claim 1 wherein the secondary solvent is an α-monoolefin which is used in the amount of from 20 to 50 percent.

Claim 13

A process of claim 1 employing additionally from 0.1 to 2.0 percent, based on the weight of total solvent, of a non-conjugated diene or a cyclic diene as a molecular weight modifier.