Compositions having high impact at low rubber levels

Claim 2

A process for graft polymerizing a mixture containing styrene and acrylonitrile onto polybutadiene in the form of a latex by effecting the polymerization in the presence of a catalyst and an effective amount of suspending agent wherein the improvement consists essentially of using a polybutadiene latex which has a particle size of about 1500-2500 A, a gel content of about 26-37 % by weight and a swell index of about 85-105.

Claim 3

The process of claim 1 wherein the polybutadiene used was prepared by polymerization at a temperature of about 5°-15° C., said polymerization being terminated at 50-80% conversion.

Claim 4

The process of claim 1 wherein the catalyst is a compound of the formula: ##STR4## wherein R is an alkyl group having 1-8 carbon atoms and R' is a tertiary alkyl group having up to 8 carbon atoms.

Claim 5

The process of claim 3 wherein the catalyst is at least one of tertiarybutyl peroxy isobutyrate, tertiarybutyl peroxy actoate, or tertiarybutyl peroxy pivalate.

Claim 6

The process of claim 1 wherein the suspending agent is a mixture of a water-soluble polyalkylene oxide and a second polymeric water-soluble organic compound.

Claim 7

The process of claim 5 wherein said polyalkylene oxide is selected from the group consisting of polyethylene oxide, polypropylene oxide, polyethylene oxide-polypropylene oxide copolymers and mixtures of these and is present in an amount of about 0.005 to about 0.4 part per 100 parts of water in the polymerization system and wherein said second polymeric water-soluble organic compound is selected from the group consisting of partially hydrolyzed polyvinylesters of monocarboxylic acids, polyglycols, solubilized cellulose derivatives, gelatins, water-soluble alginates and mixtures of these and is present in an amount of about 0.05 to 2.0 parts per 100 parts of water.

Claim 8

The process of claim 6 wherein the polyalkylene oxide is polyethylene oxide and the second polymeric water-soluble organic compound is polyvinyl alcohol.

Claim 9

A process for preparing a styrene-acrylontrile grafted polybutadiene polymeric composition, which composition consists essentially of about 12 to about 19% by weight polybutadiene based on the total weight of polymer in the composition and about 81 to about 88% by weight styrene-acrylonitrile copolymer based on the total polymer in the composition, said polymeric composition having an Izod Impact Strength in foot pounds per inch of notch determined by ASTM D-256 of at least about 8 and a ratio of Shear Stress at 868 -1 second to Izod Impact Strength in foot pounds per inch of notch of less than about 4, by:

Claim 10

A process for preparing a styrene-acrylontrile grafted polybutadiene polymeric composition, which composition consists essentially of about 12 to about 19% by weight polybutadiene based on the total weight of polymer in the composition and about 81 to about 88% by weight styrene-acrylonitrile copolymer based on the total polymer in the composition, said polymeric composition having an Izod Impact Strength in foot pounds per inch of notch determined by ASTM D-256 of at least about 8 and a ratio of Shear Stress at 868 -1 second to Izod Impact Strength in foot pounds per inch of notch of less than about 4, by:

Claim 11

adding to an aqueous emulsion medium a suitable reaction vessel a. about 12 to 19 parts by weight polybutadiene, said polybutadiene being in latex form and said latex having a polybutadiene particle size of about 1500-2500 A, a gel content of about 26-37% by weight and a swell index of about 85-105. b. about 88 to 81 parts by weight of a mixture of about 15 to about 40 parts by weight of acrylonitrile and about 60 to about 85 parts by weight of styrene. c. about 0.2-0.5% by weight of water in the reaction mixture of total suspending agent. d. about 0.1 to about 0.5% by weight of a free radical polymerization catalyst. 2. heating the contents of said reaction vessel to about 50° to about 100° C. and maintaining the temperature in this range for about 4-8 hours, and 3. recovering the product from the reaction vessel.

Claim 12

adding to an aqueous emulsion medium a suitable reaction vessel a. about 12 to 19 parts by weight polybutadiene, said polybutadiene being in latex form and said latex having a polybutadiene particle size of about 1500-2500 A, a gel content of about 26-37% by weight and a swell index of about 85-105. b. about 88 to 81 parts by weight of a mixture of about 15 to about 40 parts by weight of acrylonitrile and about 60 to about 85 parts by weight of styrene. c. about 0.2-0.5% by weight of water in the reaction mixture of total suspending agent. d. about 0.1 to about 0.5% by weight of a free radical polymerization catalyst. 2. heating the contents of said reaction vessel to about 50° to about 100° C. and maintaining the temperature in this range for about 4-8 hours, and 3. recovering the product from the reaction vessel.

Claim 13

The process of claim 8 wherein about 16 to 18 parts polybutadiene are added; wherein the suspending agent is a mixture of about 0.005-0.4% by weight, based on weight of water in the reaction vessel, polyethylene oxide and about 0.007 to about 0.05% by weight polyvinyl alcohol and wherein the catalyst is tertiarybutyl peroxy isobutyrate, tertiarybutyl peroxy octoate, or tertiarybutyl peroxy pivalate and mixtures of these.

Claim 14

The process of claim 1 wherein the reaction mixture contains about 12 to 19 parts by weight polybutadiene and about 88 to 81 parts by weight of a mixture of about 15-40 parts by weight acrylonitrile and about 60-85 parts by weight styrene, wherein the catalyst is selected from the group of tertiarybutyl peroxy isobutyrate, tertiarybutyl peroxy octoate or tertiary butyl peroxy pivalate and wherein the suspending agent is a mixture of a water soluble polyalkylene oxide and polyvinyl alcohol.

Claim 15

The process of claim 10 wherein the catalyst is a mixture of teriary butyl peroctoate and tertiary butyl peroxy pivalate and wherein the suspending agent is a mixture of polyethylene oxide and polyvinyl alcohol.

Claim 16

The process of claim 11 wherein the latex is a polybutadiene latex prepared by polymerization at about 5°-15° C.

Claim 17

The process of claim 1 wherein the polybutadiene latex has a particle size of 1500°-2500° A, a swell index of 85-105, a gel content of 26-37% by weight, a solids content of about 59-62% by weight, a pH of 10-11 and a Mooney (ML-4) of about 110-145, wherein the catalyst is selected from tertiary butyl peroxy isobutyrate tertiary butyl peroxy octoate, or tertiary butyl peroxy pivalate, and wherein the suspending agent is a mixture of a water soluble polyalkylene oxide and polyvinyl alcohol.