Production of mixtures of plastics materials

Claim 2

A process for the production of a pulverulent homogeneous mixture of plastic material which comprises: a. extruding a nonhomogeneous mixture of two or more plastic materials through a nozzle means,

Claim 3

at a temperature between the melting point of the plastic material having the lowest melting point of all components of the mixture and the maximum temperature which may be used without causing a chemical change therein, 2. at a nozzle speed of from 1 to 200 m/sec., 3. in an annular flow which tapers to a cone angle of from 5° to 40° which has an annular gap width of from 0.2 to 3 mm and an angle of twist from 0° to 60° to form a molten tube having an internal diameter of from 1 to 30 mm and a wall thickness of from 0.2 to 3 mm; b. exposing said extruded nonhomogeneous mixture of plastic materials to a gas or steam shearing medium which is divided into inner and outer streams to create a high shear velocity whereby a homogeneous mixture of plastic material is formed, 1. said inner stream of gas or steam shearing medium having a diameter of from 1 to 30 mm and an elevated temperature sufficient to maintain said extruded nonhomogeneous mixture of plastic material in a molten state, said inner stream being so directed that it impinges upon the inner surface of said extruded tube of said nonhomogeneous mixture for a distance of from 2 to 8 mm before reaching the inner edge of the orifice of said product nozzle means, 2. said outer stream of gas or steam shearing medium, flowing in an annular space which tapers to a cone angle of from 15° to 70° and having an annular gap width of from 0.3 to 5 mm at an elevated temperature sufficient to maintain said extruded nonhomogeneous mixture in a molten state so that said outer stream being so directed that it impinges upon the outer surface of said extruded tube for a distance of from 1 to 6 mm before exiting from said nozzle means, the volume of said outer stream to said inner stream being 1.2:1; c. said extruded nonhomogeneous mixture of plastic materials being subject to high shear velocities of from 10 4 to 10 8 sec - 1 for from 10 - 4 to 10 - 6 seconds by said inner and outer streams; and d. spraying the resultant pulverulent homogeneous mixture of plastic material and gas or steam shearing medium from the nozzle means into a cooling and collecting means.

Claim 4

at a temperature between the melting point of the plastic material having the lowest melting point of all components of the mixture and the maximum temperature which may be used without causing a chemical change therein, 2. at a nozzle speed of from 1 to 200 m/sec., 3. in an annular flow which tapers to a cone angle of from 5° to 40° which has an annular gap width of from 0.2 to 3 mm and an angle of twist from 0° to 60° to form a molten tube having an internal diameter of from 1 to 30 mm and a wall thickness of from 0.2 to 3 mm; b. exposing said extruded nonhomogeneous mixture of plastic materials to a gas or steam shearing medium which is divided into inner and outer streams to create a high shear velocity whereby a homogeneous mixture of plastic material is formed, 1. said inner stream of gas or steam shearing medium having a diameter of from 1 to 30 mm and an elevated temperature sufficient to maintain said extruded nonhomogeneous mixture of plastic material in a molten state, said inner stream being so directed that it impinges upon the inner surface of said extruded tube of said nonhomogeneous mixture for a distance of from 2 to 8 mm before reaching the inner edge of the orifice of said product nozzle means, 2. said outer stream of gas or steam shearing medium, flowing in an annular space which tapers to a cone angle of from 15° to 70° and having an annular gap width of from 0.3 to 5 mm at an elevated temperature sufficient to maintain said extruded nonhomogeneous mixture in a molten state so that said outer stream being so directed that it impinges upon the outer surface of said extruded tube for a distance of from 1 to 6 mm before exiting from said nozzle means, the volume of said outer stream to said inner stream being 1.2:1; c. said extruded nonhomogeneous mixture of plastic materials being subject to high shear velocities of from 10 4 to 10 8 sec - 1 for from 10 - 4 to 10 - 6 seconds by said inner and outer streams; and d. spraying the resultant pulverulent homogeneous mixture of plastic material and gas or steam shearing medium from the nozzle means into a cooling and collecting means.

Claim 5

A process as set forth in claim 1, wherein the inhomogeneous mixture consists of polyethylene having a density of from 0.915 to 0.960 g/cm 3 and a polyisobutylene having a viscosity of from 0.3 to 1.5 × 10 13 poises.

Claim 6

A process as set forth in claim 1, wherein the inhomogeneous mixture consists of polypropylene having an intrinsic viscosity of from 1.5 to 8 dl/g and polyisobutylene having a viscosity of from 0.3 to 1.5 × 10 13 poises.

Claim 7

A process as set forth in claim 1, wherein the inhomogeneous mixture consists of polystyrene and a copolymer of ethylene and vinyl acetate.

Claim 8

A process as set forth in claim 1, wherein the inhomogeneous mixture consists of polyethylene having a density of from 0.915 to 0.960 g/cm 3 and a copolymer of isobutylene with up to 10% by weight of a monomer selected from the group consisting of isoprene, styrene, chloroprene, 1,3-pentadiene, 1,3-butadiene, cyclopentadiene and dimethyl butadiene.