Foamed thermoplastic resin comprising a mixture of ionomer and polyolefin

Claim 2

A thermoplastic foamed resin product characterized by low density, high thermal resistance, good adhesion properties and uniform cell size which comprises a mixture containing from 35% to 95% ionomer characterized by the presence of a monomer unit based on an unsaturated carboxylic acid and 5% to 65% polyolefin polymer or copolymer, based on the total weight of resin; the ethylene monomer unit and unsaturated carboxylic acid ester monomer unit values of the ionomer being from 50 to 97 mol% and up to 30 mol%; respectively, the neutrality value of the ionomer being up to 50%, the saponification value of the ionomer being at least 50%, and the melt index of the ionomer being from 0.1 to 50 g/10 min.; the melt index of the polyolefin being from 0.1 to 30 g/10 min.

Claim 3

A product as in claim 1 wherein the neutrality value of the ionomer is up to 10% and the saponification value is at least 70%.

Claim 4

A product as in claim 1 wherein the melt index of the ionomer is from 0.3 to 10 g/10 min., and of the polyolefin is from 0.5 to 20 g/10 min.

Claim 5

A product as in claim 1 wherein the polyolefin is selected from the group consisting of high pressure, medium pressure and low pressure process polyethylene homopolymers, and isotactic polypropylene.

Claim 6

A product as in claim 1 wherein the carboxylic acid of the ionomer contains from 4 to 10 carbon atoms.

Claim 7

A product as in claim 1 wherein the polyolefin is a copolymer selected from the group consisting of copolymers of ethylene with a comonomer selected from the group consisting of propylene, vinyl acetate and methyl methacrylate.

Claim 8

A product as in claim 1 wherein the mixture consists of 80 to 40 percent by weight of the ionomer and 20 to 60 percent by weight of polyolefin selected from the group consisting of medium pressure and low pressure process polyethylene homopolymers and isotactic polypropylene.

Claim 9

A product as in claim 1 wherein the bulk density is from 15 to 45 kg/m 3 .

Claim 10

A process for the production of a thermoplastic foamed resin product characterized by low density, high thermal resistance, good adhesion properties and uniform cell size which comprises a mixture containing 35% to 95% ionomer characterized by the presence of a monomer unit based on an unsaturated carboxylic acid and 5% to 65% polyolefin homopolymer or copolymer, based on the total weight of resin; ethylene monomer unit and unsaturated carboxylic acid ester monomer unit values of the ionomer being from 50 to 97 mol% and up to 30 mol%, respectively, the neutrality value of the ionomer being up to 50%, the saponification value of the ionomer being from 0.1 to 50 g/10 min.; the melt index of the polyolefin being from 0.1 to 30 g/10 min.: which process comprises the steps of: 1. mixing the ionomer with a volatile blowing agent and the polyolefin at a temperature of from 100° C to 250° C and a pressure of from 50 to 250 kg/cm 2 , weight ratio of the blowing agent to polyolefin being at least 5 parts to 100 parts, and 2. extruding the mixture at a temperature of from 60° C to 150° C and a pressure of 20 to 150 kg/cm 2 into a region of reduced pressure thereby to cause volatilization of the blowing agent and foaming of the mixture.

Claim 11

A process for the production of a thermoplastic foamed resin product characterized by low density, high thermal resistance, good adhesion properties and uniform cell size which comprises a mixture containing 35% to 95% ionomer characterized by the presence of a monomer unit based on an unsaturated carboxylic acid and 5% to 65% polyolefin homopolymer or copolymer, based on the total weight of resin; ethylene monomer unit and unsaturated carboxylic acid ester monomer unit values of the ionomer being from 50 to 97 mol% and up to 30 mol%, respectively, the neutrality value of the ionomer being up to 50%, the saponification value of the ionomer being from 0.1 to 50 g/10 min.; the melt index of the polyolefin being from 0.1 to 30 g/10 min.: which process comprises the steps of: 1. mixing the ionomer with a volatile blowing agent and the polyolefin at a temperature of from 100° C to 250° C and a pressure of from 50 to 250 kg/cm 2 , weight ratio of the blowing agent to polyolefin being at least 5 parts to 100 parts, and 2. extruding the mixture at a temperature of from 60° C to 150° C and a pressure of 20 to 150 kg/cm 2 into a region of reduced pressure thereby to cause volatilization of the blowing agent and foaming of the mixture.

Claim 12

A process as in claim 9 wherein the volatile blowing agent is a hydrocarbon or halogenated hydrocarbon, with a boiling point from 30° C below zero to 100° C at normal pressure.

Claim 13

A process as in claim 9 wherein the neutrality value of the ionomer is up to 10% and the saponification value is at least 70%.

Claim 14

A process as in claim 9 wherein the melt index of the ionomer is from 0.3 to 10 g/10 min., and of the polyolefin is from 0.5 to 20 g/10 min.

Claim 15

A process as in claim 9 wherein the polyolefin is selected from the group consisting of medium pressure and low pressure process polyethylene polymers, and isotactic polypropylene.

Claim 16

A process as in claim 9 wherein the polyolefin is a copolymer selected from the group consisting of copolymers of ethylene with a comonomer selected from the group consisting of propylene, vinyl acetate and methyl methacrylate.

Claim 17

A process as in claim 9 wherein the unsaturated carboxylic acid contains from 4 to 10 carbon atoms.