Method and apparatus for extrusion of thermoplastic foam

Claim 3

The method of claim 1 wherein said blowing agent is a member selected from the group consisting of carbon dioxide, air, nitrogen, steam, helium, methane, ammonia and any mixtures thereof.

Claim 4

The method of claim 1 wherein said foam structure is a styrene polymer.

Claim 5

The method of claim 3 wherein said styrene polymer is a member selected from the group consisting of polystyrene, poly-p-methylstyrene and mixtures thereof.

Claim 6

A continuous process for thermoplastic resin foam production comprising: (a) feeding a foamable thermoplastic resin charge to a screw type extruder and heating the charge, under pressure, to a first temperature above the melting temperature thereof; (b) injecting a gas blowing agent into the molten resin charge, said injecting being by means of discrete uniform volumetric charges of said gas into said resin from a supply gas source of comparatively higher pressure, wherein said discrete volumetric charges are introduced by means of a free piston-cylinder combination given motive power by said supply gas source; (c) uniformly mixing said gas and resin; (d) cooling the mixture to a second temperature below the first temperature and above the melting temperature of said resin; and (e) extruding a foamed sheet of thermoplastic resin into a zone of lower pressure.

Claim 7

A continuous process for thermoplastic resin foam production comprising: (a) feeding a foamable thermoplastic resin charge to a screw type extruder and heating the charge, under pressure, to a first temperature above the melting temperature thereof; (b) injecting a gas blowing agent into the molten resin charge, said injecting being by means of discrete uniform volumetric charges of said gas into said resin from a supply gas source of comparatively higher pressure, wherein said discrete volumetric charges are introduced by means of a free piston-cylinder combination given motive power by said supply gas source; (c) uniformly mixing said gas and resin; (d) cooling the mixture to a second temperature below the first temperature and above the melting temperature of said resin; and (e) extruding a foamed sheet of thermoplastic resin into a zone of lower pressure.

Claim 8

The method of claim 5 wherein said atmospheric blowing agent is a member selected from the group consisting of carbon dioxide, air, nitrogen, steam, helium, methane, ammonia and any mixtures thereof.

Claim 9

The process of claim 5 wherein said resin charge is a styrene polymer.

Claim 10

The process of claim 7 wherein said styrene polymer is a member selected from the group consisting of polystyrene, poly-p-methylstyrene and mixtures thereof.

Claim 11

An extrusion apparatus adapted for the production of thermoplastic resin foam from a mixture comprising molten resin and a gas blowing agent in gas form, said apparatus comprising: (a) a pressurizable melting and mixing zone having an elongated screw disposed within an elongated barrel, said barrel having an inlet end and an outlet end; (b) gas blowing agent injection system communicating with said barrel between the ends of said barrel, said system comprising (1) a pressurized gas source, (2) a free piston and cylinder combination in communication with and powered by said gas source, (3) means in association with said free piston-cylinder combination for cycling said piston, (4) a gas conduit in communication with said cylinder and said elongated barrel to accommodate introduction of gas into said barrel on each stroke of said piston, and (5) means for controlling said piston cycling rate; (c) a resin cooling zone having an elongated screw disposed within an elongated barrel, said cooling zone barrel in communication with said melting and mixing zone; (d) means for turning said screws; and (e) an extrusion zone having an extrusion die in communication with said cooling zone.

Claim 12

An extrusion apparatus adapted for the production of thermoplastic resin foam from a mixture comprising molten resin and a gas blowing agent in gas form, said apparatus comprising: (a) a pressurizable melting and mixing zone having an elongated screw disposed within an elongated barrel, said barrel having an inlet end and an outlet end; (b) gas blowing agent injection system communicating with said barrel between the ends of said barrel, said system comprising (1) a pressurized gas source, (2) a free piston and cylinder combination in communication with and powered by said gas source, (3) means in association with said free piston-cylinder combination for cycling said piston, (4) a gas conduit in communication with said cylinder and said elongated barrel to accommodate introduction of gas into said barrel on each stroke of said piston, and (5) means for controlling said piston cycling rate; (c) a resin cooling zone having an elongated screw disposed within an elongated barrel, said cooling zone barrel in communication with said melting and mixing zone; (d) means for turning said screws; and (e) an extrusion zone having an extrusion die in communication with said cooling zone.

Claim 13

The apparatus of claim 9 wherein said means for cycling said piston includes proximity sensor means at each end of said cylinder causing cycling of control valve means to open and close, at each end of said cylinder, conduits which are each alternately a gas inlet conduit for gas powering said piston and a gas outlet conduit for accommodating outlet gas from said cylinder.

Claim 14

The apparatus of claim 10 including piston cycle rate control means to cause continuous injection of a programmed ratio of gas to molten resin.

Claim 15

The apparatus of claim 11 wherein said control valve means is a spool valve.

Claim 16

The apparatus of claim 11 wherein said rate control means includes programmed microelectronic control means.