Coupling of alkali metal-terminated polymers

Claim 2

A process for the production of a polymer comprising reacting an alkali metal-terminated polymer having the formula M-Z, wherein M represents an alkali metal and Z is a homopolymer or copolymer chain of one or more alkadienes of 4 to 12 carbon atoms per molecule or a copolymer chain of at least one alkadiene of 4 to 12 carbon atoms and at least one monovinylsubstituted arene radical of 8 to 18 carbon atoms per molecule, the vinyl radical being attached to a carbon atom of the arene ring with a coupling agent having the formula ##STR5## wherein the radicals R, which can be the same or different, are hydrocarbyl radicals with 1 to 7 carbon atoms, and wherein the coupling agent is employed in such a quantity that about 0.1 to about 0.25 mole of coupling agent is present per gram atom of alkali metal M at the beginning of the coupling reaction mixture.

Claim 3

A process in accordance with claim 1 wherein M is lithium.

Claim 4

A process in accordance with claim 1 wherein the coupling agent used is acetic anhydride.

Claim 5

A process in accordance with claim 1 wherein an alkali metal-terminated polymer having the structure M-B-A is used in which M is an alkali metal, A is a polystyrene block and B is a rubbery block obtained by polymerizing or copolymerizing an alkadiene selected from the group consisting of butadiene, isoprene or mixtures thereof.

Claim 6

A process according to claim 1 comprising a. polymerizing under polymerization conditions in a hydrocarbon diluent and in contact with a monofunctional alkali metal polymerization initiator system, at least one alkadiene monomer having 4 to 12 carbon atoms or at least one alkadiene monomer having 4 to 12 carbon atoms and at least one monovinyl-substituted arene, the vinyl substituent being attached to a ring carbon atom of the arene ring, to obtain a solution containing an alkali metal-terminated polymer having the structure M-Z, b. mixing this solution and the coupling agent such as to produce a solution containing a coupled polymer, and c. recovering a coupled polymer from the reaction mixture of step b.

Claim 7

A process in accordance with claim 5 wherein said alkadiene monomer is selected from the group consisting of butadiene, isoprene, piperylene, and mixtures thereof, and wherein said monovinyl-substituted arene is styrene, a methyl styrene or a mixture of these monovinyl-substituted arenes.

Claim 8

A process in accordance with claim 5 wherein the alkali metal-terminated polymer M-Z is produced by incremental addition of at least two different monomers such as to form an alkali metal-terminated block copolymer of at least two polymer blocks in the polymer chain Z.

Claim 9

A process in accordance with claim 7 wherein styrene is first polymerized with said monofunctional alkali metal initiator system to form an alkali metal-terminated polystyrene block in the first polymer mixture, wherein alkadiene monomer selected from the group consisting of butadiene, isoprene and mixtures thereof, alone or in admixture with a monovinyl arene selected from the group consisting of styrene, the methyl styrenes and mixtures thereof, is blended with said first polymer mixture to form a second polymer mixture consisting of an alkali metal-terminated polymer having a rubbery block attached to said styrene block, said alkali metal M being attached to the rubbery block, and wherein the second polymer mixture thereafter is blended with said coupling agent such as to form a third polymer mixture comprising a coupled polymer with polystyrene blocks at the free ends of the coupled polymer chains.

Claim 10

A process in accordance with claim 5 wherein the monofunctional alkali metal initiator system comprises a lithium compound having the formula R"Li, wherein R" is a hydrocarbyl radical of 1 to about 20 carbon atoms.

Claim 11

A process in accordance with claim 4 wherein said diluent is selected from the group consisting of n-hexane, cyclohexane, n-heptane, 2,2,4-trimethylpentane, benzene and toluene.

Claim 12

A process in accordance with claim 5 wherein about 0.1 to about 100 gram millimoles of monofunctional alkali metal initiator are used per 100 grams of total monomers.

Claim 13

A process in accordance with claim 1 further comprising the steps of a. reacting the mixture obtained during the coupling step in the presence of a hydrogenation catalyst and in the presence of free hydrogen to obtain an at least partially hydrogenated polymer, and b. recovering the thus obtained at least partially hydrogenated polymer as the product of the process.