Purification, impregnation and foaming of polymer particles with carbon dioxide

Claim 2

A process for foaming polymers and copolymers, comprising the steps of (a) placing the desired polymer or copolymer particles in a pressure vessel extractor-impregnator; (b) continuously extracting the polymer particles with a fluid at liquid or supercritical conditions to remove low molecular weight compounds while impregnating the polymer particles with the extracting fluid; (c) separating the purified, impregnated polymer particles from the extractor-impregnator; (d) pre-expanding the purified, impregnated particles at a temperature above the glass transition temperature of the polymer-fluid blend; and (e) molding the expanded particles by heating in a foam molding machine.

Claim 3

The process of claim 1 wherein the polymer is polystyrene.

Claim 4

The process of claim 1, wherein the copolymer is a copolymer of styrene and 5 to 35 mole-% of maleic anhydride, maleimide, N-alkylmaleimide, N-phenylmaleimide, esters and half esters of maleic acid, and mixtures thereof.

Claim 5

The process of claim 1 wherein the reimpregnation is accomplished with a mixture of carbon dioxide and a minor amount of a hydrocarbon blowing agent, with or without halogen substituents.

Claim 6

The process of claim 1 wherein the polymer is a blend of two or more polymers.

Claim 7

The process of claim 1 wherein the mixture of extracting fluid and low molecular weight compounds is continuously removed from the extractor-impregnator to a recovery chamber wherein the mixture is vented to a condenser to separate the extracting fluid from the low molecular weight compounds, and wherein the resulting purified extracting fluid is then continuously returned to the extractor-impregnator.

Claim 8

The process of claim 1 wherein the purified, expanded particles are reimpregnated with gaseous, liquid, or solid carbon dioxide, air, nitrogen, or other pneumatogens prior to molding the particles.

Claim 9

The process of claim 1 wherein the polymer is copolymer is selected from the group consisting of polystyrene, styrene-acrylonitrile, acrylonitrile-butadiene-styrene, styrene-maleic anhydride, styrene-methyl methacrylate, styrene-methacrylic acid, styrene-acrylic acid, high-impact rubber-modified styrene copolymers, poly(methyl methacrylate), methyl methacrylate copolymers, poly(vinyl chloride), poly(oxymethylene), poly(phenylene oxide), polypropylene, polyethylene, ethylene-propylene copolymers, polystyrene-poly(phenylene oxide) blends, cross-linked variations thereof, rubber-modified variations thereof, and interpenetrating networks thereof.

Claim 10

A process for foaming polymers and copolymers, comprising the steps of (a) placing the desired polymer or copolymer particles in a pressure vessel extractor-impregnator; (b) continuously extracting the polymer particles with carbon dioxide at liquid or supercritical conditions to remove low molecular weight compounds while impregnating the polymer particles with the carbon dioxide, wherein the mixture of carbon dioxide and low molecular weight compounds is continuously removed from the extractor-impregnator to a recovery chamber wherein the mixture is vented to a condenser to separate the carbon dioxide from the low molecular weight compounds, and wherein the resulting purified carbon dioxide is then continuously returned to the extractor-impregnator; (c) separating the purified, impregnated polymer particles from the extractor-impregnator; (d) pre-expanding the purified, impregnated particles at a temperature above the glass transition temperature of the polymer-carbon dioxide blend; (e) reimpregnating the expanded particles in gas, liquid, or solid carbon dioxide, air, nitrogen, or other pneumatogens, and (f) molding said reimpregnated expanded particles by heating in a foam molding machine.

Claim 11

A process for foaming polymers and copolymers, comprising the steps of (a) placing the desired polymer or copolymer particles in a pressure vessel extractor-impregnator; (b) continuously extracting the polymer particles with carbon dioxide at liquid or supercritical conditions to remove low molecular weight compounds while impregnating the polymer particles with the carbon dioxide, wherein the mixture of carbon dioxide and low molecular weight compounds is continuously removed from the extractor-impregnator to a recovery chamber wherein the mixture is vented to a condenser to separate the carbon dioxide from the low molecular weight compounds, and wherein the resulting purified carbon dioxide is then continuously returned to the extractor-impregnator; (c) separating the purified, impregnated polymer particles from the extractor-impregnator; (d) pre-expanding the purified, impregnated particles at a temperature above the glass transition temperature of the polymer-carbon dioxide blend; (e) reimpregnating the expanded particles in gas, liquid, or solid carbon dioxide, air, nitrogen, or other pneumatogens, and (f) molding said reimpregnated expanded particles by heating in a foam molding machine.

Claim 12

The process of claim 9 wherein the polymer is polystyrene.

Claim 13

The process of claim 9 wherein the copolymer is a copolymer of styrene and 5 to 35 mole-% of maleic anhydride, maleimide, N-alkylmaleimide, N-phenylmaleimide, esters and half esters of maleic acid, and mixtures thereof.

Claim 14

The process of claim 9 wherein the polymer is a blend of two or more polymers.

Claim 15

The process of claim 9 wherein the reimpregnation is accomplished with a mixture of carbon dioxide and a minor amount of a hydrocarbon blowing agent, with or without halogen substituents.

Claim 16

The process of claim 9 wherein the polymer or copolymer is selected from the group consisting of polystyrene, styrene-acrylonitrile, acrylonitrile-butadiene-styrene, styrene-maleic anhydride, styrene-methyl methacrylate, styrene-methacrylic acid, styrene-acrylic acid, high-impact rubber-modified styrene copolymers, poly(methyl methacrylate), methyl methacrylate copolymers, poly(vinyl chloride), poly(oxymethylene, poly(phenylene oxide), polypropylene, polyethylene, ethylene-propylene copolymers, polystyrene-poly(phenylene oxide) blends, cross-linked variations thereof, rubber-modified variations thereof, and interpenetrating networks thereof.

Claim 17

A process for making foamed, molded polystyrene, comprising the steps of: (a) placing expandable polystyrene beads in a pressure vessel extractor-impregnator; (b) continuously extracting the beads with carbon dioxide at supercritical conditions to remove low molecular weight compounds while impregnating the beads with carbon dioxide, wherein the mixture of carbon dioxide and low molecular weight compounds is continuously removed from the extractor-impregnator to a recovery chamber wherein the mixture is vented to a condenser to separate the carbon dioxide from the low molecular weight compounds, and wherein the resulting purified carbon dioxide is then continuously returned to the extractor-impregnator; (c) separating the purified; impregnated polystyrene beads from the extractor-impregnator; (d) pre-expanding the beads at a temperature above the glass transition temperature of the polystyrene-carbon dioxide blend; (e) reimpregnating the expanded beads in gaseous, liquid, or solid carbon dioxide, air, nitrogen, or other pneumatogens; and (f) molding said reimpregnated, expanded beads by heating in a foam molding machine.

Claim 18

A process for making foamed, molded polystyrene, comprising the steps of: (a) placing expandable polystyrene beads in a pressure vessel extractor-impregnator; (b) continuously extracting the beads with carbon dioxide at supercritical conditions to remove low molecular weight compounds while impregnating the beads with carbon dioxide, wherein the mixture of carbon dioxide and low molecular weight compounds is continuously removed from the extractor-impregnator to a recovery chamber wherein the mixture is vented to a condenser to separate the carbon dioxide from the low molecular weight compounds, and wherein the resulting purified carbon dioxide is then continuously returned to the extractor-impregnator; (c) separating the purified; impregnated polystyrene beads from the extractor-impregnator; (d) pre-expanding the beads at a temperature above the glass transition temperature of the polystyrene-carbon dioxide blend; (e) reimpregnating the expanded beads in gaseous, liquid, or solid carbon dioxide, air, nitrogen, or other pneumatogens; and (f) molding said reimpregnated, expanded beads by heating in a foam molding machine.