Block copolymer and process for preparing it

Claim 2

Linear copolymer consisting of four alternating blocks, endowed with a good balance between mechanical properties, rheologic properties and properties of resistance to thermooxidation, having the following general formula: B1-A1-B2-A2 wherein: B1 and B2 are polydienic blocks, and A1 and A2 are polyvinylaromatic blocks, having a weight average molecular weight of from 30,000 to 250,000, and a global content of monomer butadiene units of from 40 to 80% by weight, wherein the weight average molecular weight of B1 block is from 0.1 to 0.5 times the weight average molecular weight of B2 block, and the weight average molecular weight of A1 block is from 0.25 to 2.0 times the weight average molecular weight of A2 block, and which furthermore contains between B1 and A1 blocks a copolymer moiety formed by randomly linked monomer dienic and vinylaromatic units, characterized in that said copolymer moiety represents from 5 to 15% of the weight of the total copolymer.

Claim 3

Process for the preparation of a linear copolymer, constituted by four alternating blocks having the following general formula: B1-A1-B2-A2 wherein B1 and B2 are polydienic blocks, and A1 and A2 are polyvinylaromatic blocks, having a weight average molecular weight of from 30,000 to 250,000, and a global content of monomer butadiene units of from 40 to 80% by weight, wherein the weight average molecular weight of B1 block is from 0.1 to 0.5 times the weight average molecular weight of B2 block, and the weight average molecular weight of A1 block is from 0.25 to 2.0 times the weight average molecular weight of A2 block, and which furthermore contains between B1 and A1 blocks a copolymer moiety formed by randomly linked monomer dienic and vinylaromatic units, characterized in that: in a first step of polymerization, by the living polymer technique, metered amounts of a diene and of a vinylaromatic monomer, mixed together, are polymerized up to at least a substantially complete conversion of the monomers; a metered amount of a diene is added to the product from the first step, and is polymerized, in a second step, by the living polymer technique, up to at least a substantially complete conversion of the diene fed; a metered amount of vinylaromatic monomer is added to the product from the second step, and is polymerized in a third step, up to at least a substantially complete conversion of the vinylaromatic monomer fed; and the copolymer is recovered from the polymerization products of the third step.

Claim 4

Process for the preparation of a linear copolymer, constituted by four alternating blocks having the following general formula: B1-A1-B2-A2 wherein B1 and B2 are polydienic blocks, and A1 and A2 are polyvinylaromatic blocks, having a weight average molecular weight of from 30,000 to 250,000, and a global content of monomer butadiene units of from 40 to 80% by weight, wherein the weight average molecular weight of B1 block is from 0.1 to 0.5 times the weight average molecular weight of B2 block, and the weight average molecular weight of A1 block is from 0.25 to 2.0 times the weight average molecular weight of A2 block, and which furthermore contains between B1 and A1 blocks a copolymer moiety formed by randomly linked monomer dienic and vinylaromatic units, characterized in that: in a first step of polymerization, by the living polymer technique, metered amounts of a diene and of a vinylaromatic monomer, mixed together, are polymerized up to at least a substantially complete conversion of the monomers; a metered amount of a diene is added to the product from the first step, and is polymerized, in a second step, by the living polymer technique, up to at least a substantially complete conversion of the diene fed; a metered amount of vinylaromatic monomer is added to the product from the second step, and is polymerized in a third step, up to at least a substantially complete conversion of the vinylaromatic monomer fed; and the copolymer is recovered from the polymerization products of the third step.

Claim 5

Process according to claim 2, characterized in that the polymerization is carried out by operating in an organic, aliphatic or cycloaliphatic solvent, at temperatures from 30° to 150° C., and under a pressure equal to, or higher than the atmospheric pressure, in the presence of metal-alkyl or metal-aryl catalysts.

Claim 6

Process according to claim 3, characterized in that the solvent is n-hexane or cyclohexane, and the reaction temperature is from 50° to 100° C., the catalyst is lithium-alkyl, containing from 3 to 7 carbon atoms in the alkyl radical, and said catalyst is used in amounts from 0.025 to 0.20 parts by weight per each 100 parts by weight of the diene plus vinylaromatic compound monomers.

Claim 7

Process according to claim 2, characterized in that the diene is butadiene, and the vinylaromatic compound is styrene.

Claim 8

Process according to claim 2, characterized in that the copolymer has a weight average molecular weight from 50,000 to 150,000; a total content of butadiene units from 50% to 70% by weight; and wherein the weight average molecular weight of B1 block varies within the range of from 0.1 to 0.3 times the weight average molecular weight of B2 block, and the weight average molecular weight of A1 block varies within the range of from 0.5 to 1.5 times the weight average molecular weight of A2 block.

Claim 9

Process according to claim 2, characterized in that the copolymeric moiety represents from 5 to 15% of the weight of the total copolymer.

Claim 10

Process according to claim 2, characterized in that the dienic blocks are polybutadiene blocks, and the polyvinyl aromatic blocks are polystyrene blocks.