Block copolymers of alkadienes and monovinyl arenes

Claim 2

A copolymer having the structure D-E-C, wherein D is a hydrogenated block of low vinyl poly-1,3-butadiene, E is a hydrogenated polyisoprene block, and C is a polystyrene block.

Claim 3

A copolymer in accordance with claim 1 wherein the weight percentages of the three blocks in the entire copolymer before hydrogenation are in the range of 5 to 50 weight percent of low vinyl poly-1,3-butadiene, 10 to 90 weight percent of polyisoprene, and 1 to 50 weight percent of polystyrene.

Claim 4

A process for producing a copolymer comprising a. introducing 1,3-butadiene into a reactor and polymerizing the 1.3-butadiene in the presence of a polymerization catalyst and under polymerization conditions and essentially in the absence of vinyl promoting agents until essentially all the 1,3-butadiene has polymerized, b. adding isoprene to the reaction product of the first polymerization step, and polymerizing essentially all the monomers introduced in step b under polymerization conditions, c. adding styrene to the reactor and polymerizing this styrene under polymerizing conditions until essentially all of this monomer has polymerized, with the further provision that the process steps are either carried out in the sequence a--b--c or in the sequence c--b--a, d. hydrogenating essentially all the olefinic unsaturation of the polymer produced leaving the aromatic unsaturation essentially unchanged, and e. recovering the polymer as the product of the process.

Claim 5

A process for producing a copolymer comprising a. introducing 1,3-butadiene into a reactor and polymerizing the 1.3-butadiene in the presence of a polymerization catalyst and under polymerization conditions and essentially in the absence of vinyl promoting agents until essentially all the 1,3-butadiene has polymerized, b. adding isoprene to the reaction product of the first polymerization step, and polymerizing essentially all the monomers introduced in step b under polymerization conditions, c. adding styrene to the reactor and polymerizing this styrene under polymerizing conditions until essentially all of this monomer has polymerized, with the further provision that the process steps are either carried out in the sequence a--b--c or in the sequence c--b--a, d. hydrogenating essentially all the olefinic unsaturation of the polymer produced leaving the aromatic unsaturation essentially unchanged, and e. recovering the polymer as the product of the process.

Claim 6

A process in accordance with claim 3 wherein the first polymerization step is carried out in the presence of an organomonolithium initiator and an inert organic diluent.

Claim 7

A process in accordance with claim 4 wherein the organomonolithium initiator has the formula RLi, where R is a hydrocarbyl radical having 1 to about 20 carbon atoms and is selected from the group consisting of alkyl, cycloalkyl, and aryl radicals which can be unsubstituted or substituted by alkyl, cycloalkyl, and aryl radicals.

Claim 8

A process in accordance with claim 3 where 5 to 50 wt. % of 1,3-butadiene are added to the reactor during step a, 10 to 90 wt. % of the monomers defined in step b are added during step b and 1 to 50 wt. % of monovinyl arene are added during the step c.

Claim 9

A process in accordance with claim 3 wherein the hydrogenation is carried out with the reaction mixture obtained by the steps a, b and c, without prior isolation of the polymer, and wherein the hydrogenated polymer is thereafter isolated.

Claim 10

A process in accordance with claim 3 wherein the hydrogenation is carried out in the presence of a catalyst system consisting essentially of the reaction product of alkyl aluminum with a compound selected from the group consisting of the carboxylates and alkoxides of cobalt nickel and iron.

Claim 11

A process in accordance with claim 3 wherein the hydrogenation is carried out in the presence of the triethylaluminum/nickel octanoate catalyst system.