Process for preparing rigid PVC formulations

Claim 2

In the process of forming shaped objects from a formulation comprising an intimate admixture of a vinyl chloride resin and a plurality of particles of a polyacrylate-modified polyvinyl chloride process aid, the improvement which comprises intimately admixing said process aid particles with said vinyl chloride resin at a temperature in the range of from about 70° to 150° F. after first raising the temperature of said vinyl chloride resin to within the range of from about 180° to 250° F. by subjecting it to mechanical agitation; the particles of said polyacrylate-modified polyvinyl chloride process aid comprising particles of polyvinyl chloride having polyacrylate ester moieties polymerized in and/or on said particles, said polyacrylate ester moieties being selected from the group consisting of polymethyl methacrylate and copolymers of methyl methacrylate with up to about 20%, by weight, of at least one ethylenically unsaturated comonomer; said polyacrylate ester moieties being present in a concentration of from about 10 to 60% as based on the weight of the polyvinyl chloride moieties of said particles.

Claim 3

The process of claim 1, wherein said process aid particles are intimately admixed with said vinyl chloride resin at a temperature in the range of from about 70° to 105° F.

Claim 4

The process of claim 1, wherein the temperature of said vinyl chloride resin has first been raised to within the range of from about 210° to 230° F. prior to being intimately admixed with said process aid particles.

Claim 5

The process of claim 1, wherein said vinyl chloride resin is polyvinyl chloride.

Claim 6

The process of claim 1, wherein said vinyl chloride resin is a copolymer of vinyl chloride and a minor proportion of at least one ethylenically unsaturated comonomer.

Claim 7

The process of claim 1, wherein the polyacrylate ester moieties of said process aid particles comprise polymethyl methacrylate.

Claim 8

The process of claim 1, wherein the polyacrylate ester moieties of said process aid particles comprise copolymers of methyl methacrylate with up to 20%, by weight, of at least one ethylenically unsaturated comonomer selected from the group consisting of the C 2 --C 3 alkyl methacrylates, the C 1 --C 12 alkyl acrylates, the glycidyl esters of acrylic and methacrylic acid and mixtures thereof.

Claim 9

The process of claim 7, wherein said ethylenically unsaturated comonomer is a C 1 --C 12 alkyl acrylate.

Claim 10

The process of claim 8, wherein said ethylenically unsaturated comonomer is n-butyl acrylate.

Claim 11

The process of claim 1, wherein said process aid particles comprise about 70%, by weight, of polyvinyl chloride and about 30%, by weight, of polyacrylate ester moieties which comprise about an 86:14 methacrylate:n-butyl acrylate copolymer.

Claim 12

The process of claim 1, wherein said vinyl chloride resin is intimately admixed with at least one processing adjunct selected from the group consisting of lubricants, stabilizers and pigments prior to its intimate admixture with said polyacrylate-modified polyvinyl chloride process aid.

Claim 13

The process of claim 1, wherein said process aid particles are admixed with said vinyl chloride resin in a concentration of from about 1-10%, as based on the weight of said vinyl chloride resin.

Claim 14

The process of preparing a formulation comprising an intimate admixture of a vinyl chloride resin and a plurality of particles of a polyacrylate-modified polyvinyl chloride process aid, said formulation being especially suited for forming shaped objects whose surfaces are characterized by their high degree of smoothness and gloss, said process comprising first raising the temperature of said vinyl chloride resin to within the range of from about 180° to 250° F. by subjecting it to mechanical agitation, lowering the temperature of said resin to within the range of from about 70° to 150° F. and then intimately admixing said process aid particles with said resin; the particles of said polyacrylate-modified polyvinyl chloride process aid comprising particles of polyvinyl chloride having polyacrylate ester moieties polymerized in and/or on said particles, said polyacrylate ester moieties being selected from the group consisting of polymethyl methacrylate and copolymers of methyl methacrylate with up to about 20%, by weight, of at least one ethylenically unsaturated comonomer; said polyacrylate ester moieties being present in a concentration of from about 10 to 60% as based on the weight of the polyvinyl chloride moieties of said particles.

Claim 15

The process of preparing a formulation comprising an intimate admixture of a vinyl chloride resin and a plurality of particles of a polyacrylate-modified polyvinyl chloride process aid, said formulation being especially suited for forming shaped objects whose surfaces are characterized by their high degree of smoothness and gloss, said process comprising first raising the temperature of said vinyl chloride resin to within the range of from about 180° to 250° F. by subjecting it to mechanical agitation, lowering the temperature of said resin to within the range of from about 70° to 150° F. and then intimately admixing said process aid particles with said resin; the particles of said polyacrylate-modified polyvinyl chloride process aid comprising particles of polyvinyl chloride having polyacrylate ester moieties polymerized in and/or on said particles, said polyacrylate ester moieties being selected from the group consisting of polymethyl methacrylate and copolymers of methyl methacrylate with up to about 20%, by weight, of at least one ethylenically unsaturated comonomer; said polyacrylate ester moieties being present in a concentration of from about 10 to 60% as based on the weight of the polyvinyl chloride moieties of said particles.

Claim 16

The process of claim 13, wherein said process aid particles are intimately admixed with said vinyl chloride resin at a temperature in the range of from about 70° to 105° F.

Claim 17

The process of claim 13, wherein the temperature of said vinyl chloride resin has first been raised to a temperature in the range of from about 210° to 230° F. prior to being intimately admixed with said process aid particles.

Claim 18

The process of claim 13, wherein said vinyl chloride resin is polyvinyl chloride.

Claim 19

The process of claim 13, wherein said vinyl chloride resin is a copolymer of vinyl chloride and a minor proportion of at least one ethylenically unsaturated comonomer.

Claim 20

The process of claim 13, wherein the polyacrylate ester moieties of said process aid particles comprise polymethyl methacrylate.

Claim 21

The process of claim 13, wherein the polyacrylate ester moieties of said process aid particles comprise copolymers of methyl methacrylate with up to 20%, by weight, of at least one ethylenically unsaturated comonomer selected from the group consisting of the C 2 --C 3 alkyl methacrylates, the C 1 --C 12 alkyl acrylates, the glycidyl esters of acrylic and methacrylic acid and mixtures thereof.

Claim 22

The process of claim 19, wherein said ethylenically unsaturated comonomer is a C 2 --C 12 alkyl acrylate.

Claim 23

The process of claim 20, wherein said ethylenically unsaturated comonomer is n-butyl acrylate.

Claim 24

The process of claim 13, wherein said process aid particles comprise about 70%, by weight, of polyvinyl chloride and about 30%, by weight, of polyacrylate ester moieties which comprise about an 86:14 methyl methacrylate:n-butyl acrylate copolymer.

Claim 25

The process of claim 13, wherein said vinyl chloride resin is intimately admixed with at least one processing adjunct selected from the group consisting of lubricants, stabilizers and pigments prior to its intimate admixture with said polyacrylate-modified polyvinyl chloride process aid.

Claim 26

The process of claim 13, wherein said process aid particles are admixed with said vinyl chloride resin in a concentration of from about 1-10%, as based on the weight of said vinyl chloride resin.