Method and apparatus for extruding a cellular product

Claim 3

Method of claim 6 wherein said polymeric resin is selected from thermoplastic resins and said blowing agent is selected from chlorofluoroalkanes of 1 to 2 carbon atoms.

Claim 4

Method of claim 1 wherein said polymeric resin is chlorinated polyvinyl chloride and said blowing agent is a chlorofluoromethane.

Claim 5

Method of claim 3 including the step of heating said mixture of solid particulate resin and blowing agent in the mixing section while mixing same, and then cooling said molten mixture while mixing same in order to lower viscosity thereof and to lower vapor pressure of said blowing agent so that said blowing agent is retained thereby, said particulate resin is a chlorinated polyvinyl chloride powder.

Claim 6

In an extrusion apparatus for processing a particulate polymeric feed comprising a cylinder, an extrusion screw rotatably mounted in said cylinder and longitudinally disposed therein for advancing the feed therethrough and for progressively changing the feed from a solid to a molten form, said apparatus is divided into a feed section where the feed is introduced into said apparatus, a compaction section where the feed is densified, a choke section of reduced cross section formed by said extrusion screw having a core of constant cross-section in said choke section and said cylinder containing compacted feed that is substantially impervious to the passage of a blowing agent, a conical section integral with said screw and being upstream of said choke section providing a gradual transition between the upstream portion of said extrusion screw and said choke section, injection means located downstream of said choke section for introducing a blowing agent into said apparatus whereby the blowing agent is mixed with the feed in a solid state, a mixing section disposed downstream of said choke section where the particulate feed and the blowing agent are mixed and then melted, and an extrusion die at the downstream end of said apparatus through which the molten feed and the admixed blowing agent are forced through into a zone of lower pressure whereupon the blowing agent expands to form a cellular product.

Claim 7

In an extrusion apparatus for processing a particulate polymeric feed comprising a cylinder, an extrusion screw rotatably mounted in said cylinder and longitudinally disposed therein for advancing the feed therethrough and for progressively changing the feed from a solid to a molten form, said apparatus is divided into a feed section where the feed is introduced into said apparatus, a compaction section where the feed is densified, a choke section of reduced cross section formed by said extrusion screw having a core of constant cross-section in said choke section and said cylinder containing compacted feed that is substantially impervious to the passage of a blowing agent, a conical section integral with said screw and being upstream of said choke section providing a gradual transition between the upstream portion of said extrusion screw and said choke section, injection means located downstream of said choke section for introducing a blowing agent into said apparatus whereby the blowing agent is mixed with the feed in a solid state, a mixing section disposed downstream of said choke section where the particulate feed and the blowing agent are mixed and then melted, and an extrusion die at the downstream end of said apparatus through which the molten feed and the admixed blowing agent are forced through into a zone of lower pressure whereupon the blowing agent expands to form a cellular product.

Claim 8

Apparatus of claim 5 wherein said compaction section is characterized by an extrusion screw with a core of increasing cross section.

Claim 9

Apparatus of claim 6 wherein said mixing section includes a heating-mixing section and a downstream cooling-mixing section where the particulate feed in a solid state is initially mixed with the blowing agent and then progressively heated to melt the mixture of the feed and the blowing agent and then cooled to increase viscosity of the molten feed for efficient foaming thereof.

Claim 10

Apparatus of claim 5 wherein said compaction section is defined by said cylinder and a conical surface of increasing cross-section in the downstream direction provided on said screw, said choke section is defined by said cylinder and a surface of enlarged uniform cross-section provided on said screw that merges into said conical surface at the upstream extremity, said injection conduit is positioned downstream of said choke section at a location in said apparatus where the feed is in a solid state.

Claim 11

Apparatus of claim 7 wherein said compaction section is defined by said cylinder and a conical surface of increasing cross-section in the downstream direction provided on said screw, said choke section is defined by an annular section between said cylinder and the core of said screw wherein said annular section is rotatable with said screw and is provided with a plurality of openings providing communication therethrough, said injection conduit is positioned downstream of said choke section at a location in said apparatus where the feed is in a solid state.

Claim 12

Apparatus of claim 8 wherein said feed section is characterized by said screw with a core of uniform cross section; said mixing section is characterized by said screw having a core of uniform cross section of lesser cross section than said choke section that merges into a conical surface of increasing cross section in the downstream direction and then into a surface of enlarged uniform cross section; said feed, compaction and choke sections are about 8 to 10 L/D whereas the remainder of the extruder is about 22 to 24 L/D; and said particulate polymeric feed is in powder form that has a density of about 70 to 80 lbs/ft 3 in said choke section.