Patent GB-774681-A (GB)
Title: Improvements in or relating to thermoplastic polymeric materials
Inventor: FARR JOHN WILLIAM FREDERICK
IPC: B29B9/06
Filed: 1953-09-01
Abstract: 774,681. Making thermoplastic moulding granules. IMPERIAL CHEMICAL INDUSTRIES, Ltd. Aug. 16, 1954 [Sept. 1, 1953; March 19, 1954; March 19, 1954], Nos. 24147/53. 8061/54 and 8062/54. Class 87(2). Thermoplastic polymeric material, e.g. polythene, is converted into granular form by a process which comprises extruding the material in a molten state directly from an extrusion orifice into a cooling lquid and cutting the extruded thread into fragments while it is immersed in the liquid and before it has cooled throughout to the solid state. The freshly cut ends of the fragments, being softer than the surface already in contact with the cooling liquid, are pushed out to a small extent by the molten material at the centre and the ends tend to assume a hemispherical shape, resulting in approximately spherical granules and a freeflowing material. A spherical shape may be approximated to by adjusting the rate of cutting to the diameter of the extruded thread. Between the die 2 and the liquid container 11 is a heat insulating gasket 3, of e.g. asbestos or polytetrafluoroethylene and at the face of the orifice is a hard metal wear plate 1. As the material issues from the orifices of the extrusion channels 4, which may be arranged in a ring or in rings, it is severed by knives 9 supported by members 7 through leaf springs 10. The members 7 project from a circular plate 6 carried by a rotating shaft 5. The inlet 16 for the water or other cooling liquid is arranged to direct the incoming liquid towards the freshly extruded material. The liquid containing the cut granules flows along the outlet 15 to a screen which collects the granules and on which they may be dried. The liquid, which drains off through the screen may be recirculated. If the temperature of the liquid is raised to a point below the temperature at which the cut fragments would stick together the back pressure at the die is reduced and output is increased. When the material is polythene the temperature of the cooling water is advantageously in the range 40‹C.-65‹C. The shaft 5 may be hollow and serve as an inlet for the cooling liquid. The heat of extrusion is sufficient to maintain the temperature, or it may be so great that a cooling coil is necessary. The extrusion orifices may be of any desired cross-section, but a circular or elliptical shape is preferred. If, in the apparatus shown in Fig. 1, the material is such that the cut granules are heavier than the cooling liquid the outlet is at the bottom of the container. The centrifugal pumping action of the rotating cutter, which may be increased by mounting the knives on curved fins, is used in the volute container shown in Fig. 2 and produces a spiral flow of the liquid containing the cut granules which emerges from the outlet 13 and flows to the collecting screen. The front of the container may be of transparent plastic material. The screen is preferably vibrated and warm air may be blown on it, though, if the time of immersion of the granules is kept to a minimum, their residual heat is sufficient to dry off the liquid. A moving belt may be used instead of a vibrating screen. In a modification the material may be extruded vertically upwards or downwards, or at an angle. In another modification an oscillating, instead of a rotating, cutter may be used. The cooling liquid may contain surface active agents to increase the drying efficiency or to reduce the tendency of the granules to accumulate electrostatic charges. Three numerical examples are given, two relating to polythene and one to polyvinyl chloride. Specifications 533,306 and 638,992 are referred to in the first Provisional Specification.