twin screw extruder

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According to the invention there is provided a twin screw extruder comprising a cylinder having twin bores therein to receive the twin screw of the extruder and a circular casing, with at least one passage to permit heating or cooling fluid to flow between the cylinder and the casing, in which the cylinder has a generally circular outside contour with a first set of grooves and a second set of grooves forming parts of said at least one passage, extending obliquely to the longitudinal axis of the cylinder and formed in the outer surface of the cylinder, the bottom walls of the grooves extending parallel to a plane which includes the two longitudinal axes of the twin bores with the first set of grooves lying on one side of said plane, and the second set of grooves lying on the other side of said plane, the inclination of said first set of grooves to said axis being opposite to the inclination of said second set of grooves to said axis, and the inside of the casing containing spaced recesses forming further parts of said at least one passage and, except for end ones of said recesses, each connecting one end of a respective one of the grooves of the first set of grooves to one end of a respective one of the grooves of the second set of grooves.

   A pipe extrusion line plant for producing pipes with different diameter, comprising:an extruder for plasticizing a starting material to produce a melt strand;an adjustable calibration device sizing the melt strand to shape for forming a molten tube;a cooling device for cooling the tube; anda roll assembly for guiding the tube during advance through the calibration device and the cooling device, said roll assembly including a plurality of rolls arranged behind one another in a travel direction and constructed to have at least two different roll geometries, and adjustment means for automatically positioning the rolls in vertical direction in dependence on a diameter of a pipe being produced.

According to the invention there is provided a twin screw extruder comprising a cylinder having twin bores therein to receive the twin screw of the extruder and a circular casing, with at least one passage to permit heating or cooling fluid to flow between the cylinder and the casing, in which the cylinder has a generally circular outside contour with a first set of grooves and a second set of grooves forming parts of said at least one passage, extending obliquely to the longitudinal axis of the cylinder and formed in the outer surface of the cylinder, the bottom walls of the grooves extending parallel to a plane which includes the two longitudinal axes of the twin bores with the first set of grooves lying on one side of said plane, and the second set of grooves lying on the other side of said plane, the inclination of said first set of grooves to said axis being opposite to the inclination of said second set of grooves to said axis, and the inside of the casing containing spaced recesses forming further parts of said at least one passage and, except for end ones of said recesses, each connecting one end of a respective one of the grooves of the first set of grooves to one end of a respective one of the grooves of the second set of grooves.

   A pipe extrusion line plant for producing pipes with different diameter, comprising:an extruder for plasticizing a starting material to produce a melt strand;an adjustable calibration device sizing the melt strand to shape for forming a molten tube;a cooling device for cooling the tube; anda roll assembly for guiding the tube during advance through the calibration device and the cooling device, said roll assembly including a plurality of rolls arranged behind one another in a travel direction and constructed to have at least two different roll geometries, and adjustment means for automatically positioning the rolls in vertical direction in dependence on a diameter of a pipe being produced.

A twin screw extruder comprising a cylinder, having twin bores therein to receive the twin screw of the extruder, and a circular casing, with a passage to permit temperature control fluid to flow between the cylinder and the casing, in which said cylinder has its outer surface of a generally circular contour but formed to present a first set of grooves and a second set of grooves, forming parts of said passage and extending obliquely to the longitudinal axis of said cylinder, the bottom wall of said grooves extending parallel to a plane which includes the longitudinal axes of said twin  bores with said first set of grooves lying on one side of said plane, and said second set of grooves lying on the other side of said plane, the inclination of said first set of grooves to said axis being opposite to the inclination of said second set of grooves to said axis, and the inside of said casing being formed to present spaced recesses forming further parts of said passage and, except for end ones of said recesses, each connecting one end of a respective one of the grooves of said first set of grooves to one end of a respective one of the grooves of said second set of grooves.
   Pipe extrusion line plants are generally known. The production of plastic pipes involves initial melting of a plastic starting material in an extruder and discharge via a pipe die. The exiting thermoplastic molten tube from the pipe die is cooled under shape constraint and calibrated. Calibration is of great importance as far as pipe dimensions and tensions in the pipe wall are concerned. Plastic pipes are calibrated predominantly on the outside, whereby a vacuum calibration device is typically employed.

   The still soft molten tube is drawn shortly after discharge from the die through a calibrator which is mounted in the vacuum tank. This calibrator can be configured as sleeve-type calibrator or disk-type calibrator depending on the thermoplastic material. The required contact pressure upon the calibrator is realized by the pressure differential between the normal pressure inside the pipe and the vacuum in the vacuum tank. The vacuum calibration device includes a vessel which can be sealed vacuum-tight and may be equipped preferably as cooling basin with spray nozzles. In and following the calibration path, the extruded pipes must be cooled down to such a degree as to be sufficiently stable in shape for subsequent loads (for example take-off device, winder). Cooling of the pipes may hereby be carried out in tanks with water baths or spray nozzles.

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