초록 ▼

The invention relates to an extruder for the preparation of rubber mixtures for elastomeric products and comprises a cylinder, an endless screw rotatably mounted in the cylinder for uptake transport and homogenization of the rubber mixture, and an extrusion tool; wherein the endless screw is configu

The invention relates to an extruder for the preparation of rubber mixtures for elastomeric products and comprises a cylinder, an endless screw rotatably mounted in the cylinder for uptake transport and homogenization of the rubber mixture, and an extrusion tool; wherein the endless screw is configured with zones of multiple treads in dependence of varying helix angle and depth of thread so that the rubber mixture transported through the zones undergoes a temperature increase through heat dissipation to such an extent that the temperature of the extrudate approaches the vulcanization temperature thereof.

대표청구항 ▼

1. An extruder for processing a rubber mixture, comprising:a cylinder; a screw rotatably supported in the cylinder for uptake, transport, mixing and extruding a rubber mixture; and a head with incorporated extrusion tool, wherein the screw for advancing a rubber mixture to the extrusion tool has a l

1. An extruder for processing a rubber mixture, comprising:a cylinder; a screw rotatably supported in the cylinder for uptake, transport, mixing and extruding a rubber mixture; and a head with incorporated extrusion tool, wherein the screw for advancing a rubber mixture to the extrusion tool has a longitudinal dimension extending from a screw entry zone to a screw exit zone and defined by a helix angle and a thread depth, wherein the dimension varies from the screw entry zone to the screw exit zone so that a rise of the helix angle and the depth of thread are decreasing across the longitudinal dimension from the screw entry zone to the screw exit zone thereby increasing pressure on the advancing rubber mixture near the entry zone, wherein the increased pressure on the advancing rubber mixture has a heat dissipation effect so that the rubber mixture is subjected to a temperature rise during advance to the extrusion tool as a consequence of the heat dissipation and at a constant or decreasing pressure, whereby an extrudate can be obtained at a temperature which approximates a vulcanizing temperature for the extrudate. 2. The extruder of claim 1, wherein the screw is a multithread screw with the number of threads increasing as a root diameter of the screw increases along the longitudinal dimension from the entry zone to the exit zone.3. The extruder of claim 1, wherein the screw in the exit zone is configured as a screw of minimum output with a helix angle φ below 14°.4. The extruder of claim 3, wherein the helix angle φ in the exit zone is about 7°-14°.5. The extruder of claim 1, wherein the screw exhibits a thread depth in the exit zone which is less than 0.15×a root diameter of the screw in the exit zone.6. The extruder of claim 1, and further comprising an insulation ring, wherein the cylinder includes at least two subassemblies which are separated from each other by the insulation ring to thermal de-coupling of the subassemblies.7. The extruder of claim 1, and further comprising a pressure piece inserted in the head for reducing a free volume and for optional pressure increase.8. A method for processing a rubber mixture in a screw extruder for production of elastomeric products for subsequent plasticizing and shaping into a desired extrudate, comprising the steps of:feeding the rubber mixture to an extruder for subsequent exposure to a vulcanizing process, by advancing the rubber mixture in the extruder by an extruder screw extending from a screw entry zone under increasing pressure in a direction of a screw exit zone in which the rubber mixture is advanced at a constant or decreasing pressure, wherein the dimension of the screw includes a helix angle and a depth of thread of the screw selected in such a way that the helix angle and the depth of thread are decreasing over an extension form the entry zone to the exit zone to thereby continuously increase the temperature of the rubber mixture; so that the extrudate exits the extruder at a temperature which approximates a vulcanizing temperature of the extrudate. 9. The method of claim 8, and further comprising the step of increasing the screw speed to increase the temperature of the rubber mixture while retaining a low output of extrudate.10. An extruder for processing a rubber mixture, comprising:a cylinder; a screw rotatably supported in the cylinder for uptake, transport, mixing and extruding a rubber mixture; and a head with incorporated extrusion tool, wherein the screw for advancing a rubber mixture to the extrusion tool has a longitudinal dimension extending from a screw entry zone to a screw exit zone and defined by a helix angle and a thread depth, wherein the dimension varies from the screw entry zone to the screw exit zone so that a rise of the helix angle and the depth of thread are decreasing across the longitudinal dimension from the screw entry zone to the screw exit zone thereby causing an increase in pressure on the advancing rubber mixture, wherein the increased pressure on the advancing rubber mixture has a heat dissipation effect so that the rubber mixture is subjected to a temperature rise during advance to the extrusion tool as a consequence of the heat dissipation, whereby an extrudate can be obtained at a temperature which approximates a vulcanizing temperature for the extrudate, wherein a pressure piece is inserted in the head for reducing a free extrudate volume and for optional pressure increase.