Aqueous emulsion of multi-component synethetic resin and process for production thereof

Claim 2

An aqueous emulsion of a multicomponent synthetic resin containing 10 to 60% by weight of solids resulting from the polymerization of (A) 1 to 50% by weight of ethylene, (B) 4 to 95% by weight of a styrene monomer or a mixture of a styrene monomer and a monomer copolymerizable therewith, and (C) 4 to 95% by weight of a vinyl ester or a mixture of a vinyl ester and a monomer copolymerizable therewith, said emulsion being obtained by emulsion-polymerization of ethylene and component (C) in the presence of an aqueous emulsion obtained by the emulsion-polymerization of ethylene and component (B).

Claim 3

A process for producing an aqueous emulsion of a multicomponent synthetic resin containing 10 to 60% by weight of solids resulting from the polymerization of (A) 1 to 50% by weight of ethylene, (B) 4 to 95% by weight of a styrene monomer or a mixture of a styrene monomer and a monomer copolymerizable therewith, and (C) 4 to 95% by weight of a vinyl ester or a mixture of a vinyl ester and a monomer copolymerizable therewith, which comprises a first step of emulsion-polymerizing ethylene and component (B) to form an aqueous emulsion substantially free from monomer (B), and a second step of emulsion polymerizing ethylene and component (C) in the presence of the aqueous emulsion obtained in the first step.

Claim 4

A process for producing an aqueous emulsion of a multicomponent synthetic resin containing 10 to 60% by weight of solids resulting from the polymerization of (A) 1 to 50% by weight of ethylene, (B) 4 to 95% by weight of a styrene monomer or a mixture of a styrene monomer and a monomer copolymerizable therewith, and (C) 4 to 95% by weight of a vinyl ester or a mixture of a vinyl ester and a monomer copolymerizable therewith, which comprises a first step of emulsion-polymerizing ethylene and component (B) to form an aqueous emulsion substantially free from monomer (B), and a second step of emulsion polymerizing ethylene and component (C) in the presence of the aqueous emulsion obtained in the first step.

Claim 5

The process of claim 2 wherein said styrene monomer is selected from the group consisting of styrene, alpha-methylstyrene, 2-chlorostyrene, 4-chlorostyrene, 2,5-dichlorostyrene and 4-methoxystyrene, and said monomer copolymerizable with the styrene monomer is selected from the group consisting of methyl (meth)acrylates, ethyl (meth)acrylates, propyl (meth)acrylates, butyl (meth)acrylates, 2-ethylhexyl (meth)acrylates, acrylic acid, methacrylic acid, maleic acid, maleic acid esters, (meth)acrylonitriles, (meth)acrylamides, vinylpyridine and vinylpyrrolidone.

Claim 6

The process of claim 2 wherein said vinyl ester is selected from vinyl esters of linear or branched carboxylic acids containing 1 to 25 carbon atoms, and said monomer copolymerizable with the vinyl ester is selected from the group consisting of vinyl chloride, vinyl bromide, acrylate esters, crotonic acid, and fumaric acid esters.

Claim 7

The process of claim 2 wherein the weight ratio of the styrene monomer to the monomer copolymerizable therewith in component (B) is from 1:0 to 1:3, and the weight ratio of the vinyl ester to the monomer copolymerizable therewith in component (C) is from 1:0 to 1:3.

Claim 8

The process of claim 2 wherein said styrene monomer in component (B) is styrene, and said vinyl ester in component (C) is vinyl acetate.

Claim 9

The process of claim 2 wherein the emulsion polymerization in the first step is carried out until the amount of the unreacted monomer (B) in the resulting aqueous emulsion is less than about 300 ppm.

Claim 10

The process of claim 2 wherein the emulsion polymerization in the first and second steps is carried out in the presence of a radical-forming catalyst at a temperature of 0° to 100° C. and a pressure of 5 to 200 kg/cm 2 .