Method and apparatus for extruding foam polymeric materials involving the use of an extrusion screw having spaced multiple flight mixing means thereon

Claim 2

Method for extruding a cellular polymeric material with an extruder having disposed therein an elongated screw comprising charging a particulate polymeric material into the feed section of the extruder, advancing said material through the melt section of the extruder where said material is progressively converted from a solid to a molten state, injecting a blowing agent into said molten material at the injection section of the extruder to form a mixture of said material and the blowing agent, advancing said mixture through a mixing section of the extruder, agitating said mixture in said mixing section by means of rotating multiple screw flights on the screw, further agitating said mixture in at least one open slot provided on the screw in the mixing section, advancing said mixture from the open slot by means of the multiple flights while agitating same, and extruding said mixture whereby the blowing agent expands to form a cellular product.

Claim 3

Method of claim 1 wherein agitation of said mixture by means of the rotating flights includes the step of mixing the mixture by allowing some of it to pass over the minor flights into adjacent upstream channels in the flights and become comingled with the mixture therein.

Claim 4

Method of claim 2 wherein said polymeric material is CPVC in powder form, said method further including the step of alternating a plurality of times agitation by means of the screw flights and agitation in the open slot as the mixture is advanced through the mixing section, agitation by means of the screw flights includes the step of arresting the upstream advance of a portion of the mixture by means of a major flight.

Claim 5

Method of claim 3 which includes the step of damming the upstream end of the injection section to prevent seepage of said blowing agent upstream, agitating by means of screw flights is carried out 3 to 5 times and agitation in the open slots is carried out alternately 2 to 4 times.

Claim 6

Method of claim 4 wherein temperature in the feed section is about 320° to 360° F., temperature in the melt section is 340° to 400° F., temperature in the injection section is about 200° to 240° F., temperature in the mixing section is about 190° to 240° F., and temperature at the extrusion die is about 290° to 340° F., said blowing agent is used in amount of 5 to 50% by weight of chlorinated polyvinyl chloride and is selected from chlorofluoroalkanes of 1 to 2 carbon atoms.

Claim 7

In an extrusion apparatus for processing a particulate polymeric material comprising a cylinder, an extrusion screw rotatably mounted in said cylinder and longitudinally extending therein for advancing the polymeric material therethrough that is progressively changed from a solid to a molten form, and a die means at the downstream end of said apparatus through which the polymeric material is extruded in a cellular state, said extrusion screw comprising a feed section where the polymeric material is introduced into said apparatus, a melt section where the polymeric material is progressively converted from a solid to a fluid state, injection section for introducing a blowing agent, and a mixing section where the polymeric material and the blowing agent are agitated to make a mixture of the polymeric material and the blowing agent, the improvement comprising said mixing section provided with multiple screw flights disposed on a core of said screw for advancing the mixture and at least one continuous annular open slot that is an annular zone devoid of said flights where further agitation of the mixture is carried out, said slots comprise an unobstructed annular space defined by said multiple flights at both axial extremities of said slots.

Claim 8

In an extrusion apparatus for processing a particulate polymeric material comprising a cylinder, an extrusion screw rotatably mounted in said cylinder and longitudinally extending therein for advancing the polymeric material therethrough that is progressively changed from a solid to a molten form, and a die means at the downstream end of said apparatus through which the polymeric material is extruded in a cellular state, said extrusion screw comprising a feed section where the polymeric material is introduced into said apparatus, a melt section where the polymeric material is progressively converted from a solid to a fluid state, injection section for introducing a blowing agent, and a mixing section where the polymeric material and the blowing agent are agitated to make a mixture of the polymeric material and the blowing agent, the improvement comprising said mixing section provided with multiple screw flights disposed on a core of said screw for advancing the mixture and at least one continuous annular open slot that is an annular zone devoid of said flights where further agitation of the mixture is carried out, said slots comprise an unobstructed annular space defined by said multiple flights at both axial extremities of said slots.

Claim 9

Apparatus of claim 6 wherein said multiple flights comprise 2 to 6 flights, at least one of which is a major flight and remaining being minor flights; the polymeric material is chlorinated polyvinyl chloride; the blowing agent is selected from chlorofluoroalkanes containing 1 to 2 carbon atoms; and said slots are defined in radial extent by the core of said screw that has an increasing cross-section through said feed section and melt section but has a constant cross-section through said injection section and mixing section.

Claim 10

Apparatus of claim 2 wherein said open slots are about 1/3 L/D in axial extent.

Claim 11

Apparatus of claim 8 wherein there are three spaced open slots in said mixing section, and there are four flights in said mixing section.

Claim 12

Appartus of claim 7 which includes a dam on the upstream end of said injection section for preventing seepage of a gaseous blowing agent upstream from the injection section, said mixing section being about 6 to 16 L/D in length and comprises 3 to 5 screw flights and at least 2 open slots.