Styrenic impact polymers

Claim 2

A graft copolymer composition having improved toughness consisting essentially of: (a) from about 8.0 to about 16.0 parts by weight of a mixture of an ABA block copolymer and an A'B'A' tapered block copolymer in a weight ratio of the ABA copolymer to the A'B'A' copolymer of between about 25:75 and about 75:25 where each A segment is an essentially pure polymer block of styrene having a number average molecular weight of between about 14,000 and about 18,000, the B segment is an essentially pure polymer block of butadiene having a number average molecular weight of between about 60,000 and about 80,000, the B block having a glass transition temperature of about -105° C.±5° C., the weight ratio of total A to B being between about 1:1.8 and about 1:2.7, and wherein each A' segment represents essentially polymerized styrene, the balance of the A' segment being polymerized butadiene, the B' segment represents essentially polymerized butadiene, the balance of the B' segment being polymerized styrene, the weight ratio of total A' to B' being from about 1:2.6 to about 1:3.6, the number average molecular weight of said A'B'A' block copolymers being between about 400,000 and about 660,000, and said B' block having a glass transition temperature of about -90° C.±5° C.: and (b) from about 92.0 to about 84.0 parts by weight of monomeric styrene polymerized in the presence of said ABA and said A'B'A' copolymers.

Claim 3

The composition of claim 1 wherein the number average molecular weight of the A block is between about 15,000 and about 17,000.

Claim 4

The composition of claim 2 wherein the number average molecular weight of the B block is between about 65,000 and about 75,000.

Claim 5

The composition of claim 1 wherein the number average molecular weight of the A'B'A' tapered copolymer is between about 400,000 and about 500,000.

Claim 6

The composition of claim 1 wherein the relative amount of B' monomer in the A' block is about 20 weight percent and wherein the relative amount of A' monomer in the B' block is about 20 weight percent.

Claim 7

The composition of claim 1 wherein the morphology consists of polygon-shaped subparticles of polystyrene in a dispersed particulate polybutadiene phase.

Claim 8

In the process for preparing an impact modified poly(vinyl aromatic) composition comprising bulk thermal polymerizing of from about 2 to about 25 parts of rubber dissolved in about 98 to about 75 parts of a feed in which the sole polymerizable monomer component consists essentially of one or more monovinyl aromatic compounds at a temperature in the range from about 90° to about 200° C., with agitation until the reaction mixture has undergone phase inversion, for a time sufficient to polymerize substantially all of the monovinyl aromatic compound and removing residual monomers to form an interpolymer containing discrete gelled rubber particles, which improvement comprises using as the rubber a mixture of ABA block copolymer and A'B'A' tapered block copolymer in a weight ratio of the ABA copolymer to the A'B'A' copolymer of between about 25:75 and 75:25 where each A segment is an essentially pure polymer block of styrene having a number average molecular weight of between about 14,000 and about 18,000, the B segment is an essentially pure polymer block of butadiene having a number average molecular weight of between about 60,000 and about 80,000, the B block having a glass transition temperature of about -105° C.±5° C., the weight ratio of total A to B being between about 1:1.8 and about 1:2.7, and wherein each A' segment represents essentially polymerized styrene, the balance of the A' segment being polymerized butadiene, the B' segment represents essentially polymerized butadiene, the balance of the B' segment being polymerized styrene, the weight ratio of total A' to B' being from about 1:2.6 to about 1:3.6, the number average molecular weight of said A'B'A' block copolymers being between about 400,000 and about 660,000, and said B' block having a glass transition temperature of about -90° C.±5° C.

Claim 9

In the process for preparing an impact modified poly(vinyl aromatic) composition comprising bulk thermal polymerizing of from about 2 to about 25 parts of rubber dissolved in about 98 to about 75 parts of a feed in which the sole polymerizable monomer component consists essentially of one or more monovinyl aromatic compounds at a temperature in the range from about 90° to about 200° C., with agitation until the reaction mixture has undergone phase inversion, for a time sufficient to polymerize substantially all of the monovinyl aromatic compound and removing residual monomers to form an interpolymer containing discrete gelled rubber particles, which improvement comprises using as the rubber a mixture of ABA block copolymer and A'B'A' tapered block copolymer in a weight ratio of the ABA copolymer to the A'B'A' copolymer of between about 25:75 and 75:25 where each A segment is an essentially pure polymer block of styrene having a number average molecular weight of between about 14,000 and about 18,000, the B segment is an essentially pure polymer block of butadiene having a number average molecular weight of between about 60,000 and about 80,000, the B block having a glass transition temperature of about -105° C.±5° C., the weight ratio of total A to B being between about 1:1.8 and about 1:2.7, and wherein each A' segment represents essentially polymerized styrene, the balance of the A' segment being polymerized butadiene, the B' segment represents essentially polymerized butadiene, the balance of the B' segment being polymerized styrene, the weight ratio of total A' to B' being from about 1:2.6 to about 1:3.6, the number average molecular weight of said A'B'A' block copolymers being between about 400,000 and about 660,000, and said B' block having a glass transition temperature of about -90° C.±5° C.

Claim 10

The process of claim 7 wherein the number average molecular weight of the A block is between about 15,000 and about 17,000.

Claim 11

The process of claim 8 wherein the number average molecular weight of the B block is between about 65,000 and about 75,000.

Claim 12

The process of claim 7 wherein the number average molecular weight of the A'B'A' tapered copolymer is between about 400,000 and about 500,000.

Claim 13

The process of claim 7 wherein the relative amount of B' monomer in the A' block is about 20 weight percent and wherein the relative amount of A' monomer in the B' block is about 20 weight percent.

Claim 14

The process of claim 7 wherein the morphology consists of polygon-shaped subparticles of polystyrene in a dispersed particulate polybutadiene phase.