Impact improved polymers

Claim 2

A graft copolymer composition having a toluene insoluble gel/total rubber weight ratio in the range of from about 1.65 to about 0.39 and a rubber utilization of from about 21 to about 65, consisting essentially of from about 4 to 12 parts by weight of a mixture of (1) polybutadiene elastomer and (2) polyisoprene elastomer in a weight ratio of (1) to (2) between 35:65 and 65:35 and from about 96 to about 88 parts by weight of polymerized styrene.

Claim 3

A composition according to claim 1 wherein the rubber utilization is at least about 29 and said weight ratio of polybutadiene elastomer to polyisoprene elastomer is in the range from 40:60 to 60:40.

Claim 4

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 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, the improvement which comprises using as the rubber a mixture of polybutadiene elastomer and polyisoprene elastomer in a weight ratio of polybutadiene to polyisoprene between 35:65 and 65:35 to form an interpolymer having a toluene insoluble gel/total rubber weight ratio in the range of from about 1.65 to about 0.39.

Claim 5

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 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, the improvement which comprises using as the rubber a mixture of polybutadiene elastomer and polyisoprene elastomer in a weight ratio of polybutadiene to polyisoprene between 35:65 and 65:35 to form an interpolymer having a toluene insoluble gel/total rubber weight ratio in the range of from about 1.65 to about 0.39.

Claim 6

The improved process of claim 3 wherein the feed monomer is styrene and the rubber content is no more than about 6 percent by weight, which comprises the additional step of maintaining the interpolymer at a temperature above about 225° C. for a period of at least about 10 minutes.

Claim 7

The improved process of claim 3 wherein the feed monomer is styrene and the rubber content is greater than 6 percent by weight, which comprises the additional step of mechanically working the interpolymer at a temperature between about 150° and 270° C. for a period of from about five minutes to about ten hours, resulting in interpolymer with a rubber utilization value in the range from about 21 to about 65.

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 a 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 and continuing polymerization without agitation 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, the improvement which comprises using as the rubber a mixture of polybutadiene elastomer and polyisoprene elastomer in a weight ratio of polybutadiene to polyisoprene between 35:65 and 65:35 to form an interpolymer having a toluene insoluble gel/total rubber weight ratio in the range of from about 1.65 to about 0.39.

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 a 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 and continuing polymerization without agitation 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, the improvement which comprises using as the rubber a mixture of polybutadiene elastomer and polyisoprene elastomer in a weight ratio of polybutadiene to polyisoprene between 35:65 and 65:35 to form an interpolymer having a toluene insoluble gel/total rubber weight ratio in the range of from about 1.65 to about 0.39.

Claim 10

The improved process of claim 6 wherein the feed monomer is styrene and the rubber content is no more than about 6 percent by weight which comprises the additional step of maintaining the interpolymer at a temperature above about 225° C. for a period of at least about 10 minutes.

Claim 11

The improved process of claim 6 wherein the feed monomer is styrene and the rubber content is greater than 6 percent by weight, which comprises the additional step of mechanically working the interpolymer at a temperature between about 150° and 270° C. for a period of from about 5 minutes to about ten hours, resulting in an interpolymer with a rubber utilization value in the range from about 21 to about 65.

Claim 12

A process according to claim 5 wherein said feed monomer is styrene, said weight ratio of polybutadiene elastomer to polyisoprene elastomer is in the range from 40:60 to 60:40, and the rubber utilization of the resulting interpolymer is in the range from about 29 to about 65.

Claim 13

A process according to claim 5 wherein said weight ratio of polybutadiene elastomer to polyisoprene elastomer is in the range from 40:60 to 60:40 and the rubber utilization of the resulting interpolymer is at least about 29.

Claim 14

A process according to claim 6 wherein said feed monomer is styrene, said weight ratio of polybutadiene elastomer to polyisoprene elastomer is in the range from 40:60 to 60:40, and the rubber utilization of the resulting interpolymer is in the range from about 29 to about 65.

Claim 15

A process according to claim 5 wherein said weight ratio of polybutadiene elastomer to polyisoprene elastomer is in the range from 40:60 to 60:40 and the rubber utilization of the resulting interpolymer is at least about 29.