Process and apparatus for the production of elongated structures

Claim 1

A method of continuously coating an elongated core with a plastic comprising: introducing said core into the bore of an elongated heated guide tube having an inside diameter greater than the outside diameter of said core; introducing said plastic in liquid condition into a heated mixing chamber in communication with and surrounding the exit end of said guide tube to cause intimate contact of said plastic with said core in heated condition; introducing a flowing stream of heated plastic containing said core from said mixing chamber into a mold tube having an elongated bore in substantial axial alignment with the bore of said guide tube; the velocity of said flowing stream of plastic and its frictional forces on said core being sufficient to convey and simultaneously center said core therein; maintaining said mold tube at a temperature sufficient to initiate solidification of said plastic whereby to encapsulate said core with a solid plastic coating; and continuously recovering said plastic coated core.

Claim 2

A method of continuously coating an elongated core with a plastic comprising: introducing said core into the bore of an elongated heated guide tube having an inside diameter greater than the outside diameter of said core; introducing said plastic in liquid condition into a heated mixing chamber in communication with and surrounding the exit end of said guide tube to cause intimate contact of said plastic with said core in heated condition; introducing a flowing stream of heated plastic containing said core from said mixing chamber into a mold tube having an elongated bore in substantial axial alignment with the bore of said guide tube; the velocity of said flowing stream of plastic and its frictional forces on said core being sufficient to convey and simultaneously center said core therein; maintaining said mold tube at a temperature sufficient to initiate solidification of said plastic whereby to encapsulate said core with a solid plastic coating; and continuously recovering said plastic coated core.

Claim 3

A method of continuously coating an elongated core with a plastic comprising: introducing a liquid polymerizable monomer of said plastic into a heated mixing zone communicating on one side with an elongated mold tube having a diameter greater than the diameter of said core to provide a flowing liquid stream of polymerizing monomer therein; introducing said core into the bore of a heated guide tube communicating with said mixing chamber on its other side and extending coaxially with said mold tube; maintaining said mixing zone at the polymerization temperature of said monomer with a residence time sufficient to initiate polymerization and intimately contact said plastic with said core; introducing said core into said flowing liquid stream of polymerizing monomer the velocity of said stream and its frictional forces on said core being sufficient to convey and simultaneously center said core therethrough; maintaining said mold tube at a temperature sufficient to complete the polymerization of said monomer; and continuously recovering said plastic coated core.

Claim 4

A method of continuously coating an elongated core with a plastic comprising: introducing a liquid polymerizable monomer of said plastic into a heated mixing zone communicating on one side with an elongated mold tube having a diameter greater than the diameter of said core to provide a flowing liquid stream of polymerizing monomer therein; introducing said core into the bore of a heated guide tube communicating with said mixing chamber on its other side and extending coaxially with said mold tube; maintaining said mixing zone at the polymerization temperature of said monomer with a residence time sufficient to initiate polymerization and intimately contact said plastic with said core; introducing said core into said flowing liquid stream of polymerizing monomer the velocity of said stream and its frictional forces on said core being sufficient to convey and simultaneously center said core therethrough; maintaining said mold tube at a temperature sufficient to complete the polymerization of said monomer; and continuously recovering said plastic coated core.

Claim 9

An apparatus for continuously coating an elongated core including: a housing member having an inlet end and an outlet end; a mixing zone defined by said housing intermediate said inlet and outlet ends; pump means for introducing liquid plastic into said mixing zone; at least one guide tube supported within said housing having a bore with its inlet port in communication with said inlet end of said housing and its exit port in communication with said mixing zone; at least one mold tube supported within said housing having its inlet port in communication with the outlet end of said housing; said mixing zone having a volume larger than said guide and mold tubes and defined by a continuing wall having an off-center convolution about the exit port of said guide tube and a coaxial conical exit port converging into the inlet port of said mold tube; and heat transfer means for said housing member for heating said guide tube and cooling said mold tube; whereby an elongated core having an outside diameter less than the inside diameters of said tubes is drawn through said guide tube and said mixing zone by the flow of plastic in said mold tube and is simultaneously coated with a plastic layer.

Claim 10

An apparatus for continuously coating an elongated core including: a housing member having an inlet end and an outlet end; a mixing zone defined by said housing intermediate said inlet and outlet ends; pump means for introducing liquid plastic into said mixing zone; at least one guide tube supported within said housing having a bore with its inlet port in communication with said inlet end of said housing and its exit port in communication with said mixing zone; at least one mold tube supported within said housing having its inlet port in communication with the outlet end of said housing; said mixing zone having a volume larger than said guide and mold tubes and defined by a continuing wall having an off-center convolution about the exit port of said guide tube and a coaxial conical exit port converging into the inlet port of said mold tube; and heat transfer means for said housing member for heating said guide tube and cooling said mold tube; whereby an elongated core having an outside diameter less than the inside diameters of said tubes is drawn through said guide tube and said mixing zone by the flow of plastic in said mold tube and is simultaneously coated with a plastic layer.

Claim 13

An apparatus for continuously coating an elongated core including: a housing member having an inlet and an outlet end; a mixing zone defined by said housing intermediate said inlet and outlet ends; pump means for introducing liquid plastic into said mixing zone; at least one mold tube supported within said housing having its inlet port in communication with said mixing zone and an exit port in communication with the outlet end of said housing; said mixing zone having a volume larger than said mold tube and defined by a continuous smooth wall having an off-center convolution opposed to the inlet port of said mold tube and a coaxial conical exit port converging into the inlet port of said mold tube; and heat transfer means for said housing member for heating said mixing zone and cooling said mold tube; whereby an elongated core having an outside diameter less than the inside diameters of said tubes is coated with a plastic layer upon passage through said mixing zone and into the inlet port of said mold tube for recovery at said outlet end.

Claim 14

An apparatus for continuously coating an elongated core including: a housing member having an inlet and an outlet end; a mixing zone defined by said housing intermediate said inlet and outlet ends; pump means for introducing liquid plastic into said mixing zone; at least one mold tube supported within said housing having its inlet port in communication with said mixing zone and an exit port in communication with the outlet end of said housing; said mixing zone having a volume larger than said mold tube and defined by a continuous smooth wall having an off-center convolution opposed to the inlet port of said mold tube and a coaxial conical exit port converging into the inlet port of said mold tube; and heat transfer means for said housing member for heating said mixing zone and cooling said mold tube; whereby an elongated core having an outside diameter less than the inside diameters of said tubes is coated with a plastic layer upon passage through said mixing zone and into the inlet port of said mold tube for recovery at said outlet end.