Lateral melt feed extrusion nozzle for films or slabs

• US 20050031854A1
• Filed: 11/21/2002
• Published: 02/10/2005
• Est. Priority Date: 12/18/2001
• Status: Abandoned Application

• Current Assignee: Roehm GmbH & Co. KG
• Original Assignee: Roehm GmbH & Co. KG
• Inventors: Schuchmann, Roland, Krohmer, Christoph, Lorenz, Hans
• Application Number:
  US10/494,730
• Publication Number:
  US 20050031854A1
• Time in Patent Office: Days
• US Class Current: 428/332
• CPC Class Codes: B29C 48/07 Flat, e.g. panels
• CPC Class Codes: B29C 48/08 flexible, e.g. films
• CPC Class Codes: B29C 48/313 by positioning the die lips
• CPC Class Codes: B29K 2033/12 Polymers of methacrylic acid esters, e.g. PMMA, i.e. polymethylmethacrylate
• CPC Class Codes: B29K 2105/0032 Pigments, colouring agents or opacifiyng agents
• CPC Class Codes: Y10T 428/26 Web or sheet containing structurally defined element or component, the element or component having a specified physical dimension

Abstract

The invention relates to an extrusion nozzle for shaping extruded melts produced from thermoplastics to webs of film or slabs. Said nozzle substantially comprises a nozzle body (1), at least one opening for feeding the melt (2) to a distributing channel (3) with at least one retaining island (4) and a slit die-type nozzle emergence zone (5). The melt (2) is fed to the distributing channel (3) laterally relative the extrusion direction (E) predetermined by the nozzle emergence zone (5). The invention further relates to a corresponding production method and to films and slabs produced according to the inventive method.

Claims

1. An extrusion die for the shaping of extruded melts of thermoplastic materials into film or sheet webs, substantially comprising the die body (1), at least one orifice for the melt feed (2) into a manifold (3) with at least one restricting island (4) and a slot-shaped die outlet region (5),

characterized in that

the melt feed (2) into the manifold (3) takes place laterally with respect to the direction of extrusion (E) predetermined by the die outlet region (5).

2. The extrusion die as claimed in claim 1, characterized in that, with respect to the plane of a cross section through the die body, the direction of the melt feed (S) into the manifold and the direction of extrusion (E) form an angle of from 30 to 135°

.

3. The extrusion die as claimed in claim 1 or 2, characterized in that the manifold (3) has the shape of a coat-hanger manifold, a fish-tail manifold or a T-shaped manifold.

4. The extrusion die as claimed in one or more of claims 1 to 3, characterized in that the cross section of the manifold (3) is circular, rectangular, oval, elliptical or polygonal or has a transitional form of the cross sections mentioned.

5. The extrusion die as claimed in one or more of claims 1 to 4, characterized in that the manifold cross section has an aspect ratio of manifold width to manifold height of from 3 to 10 to 1.

6. The extrusion die as claimed in one or more of claims 1 to 5, characterized in that it is an extrusion die for the extrusion of a single layer of plastic.

7. The extrusion die as claimed in one or more of claims 1 to 5, characterized in that it is a coextrusion die for the simultaneous extrusion of a number of layers of plastic one on top of the other, the melt feed (2) into the manifold (3) taking place laterally with respect to the direction of extrusion (E) predetermined by the die outlet region (5), at least in the case of one of the layers of plastic.

8. A process for producing films or sheets of thermoplastic material in a way known per se by extrusion or coextrusion, an extrusion die as claimed in one or more of claims 1 to 7 being used for the shaping.

9. Extruded films or sheets of thermoplastic material which can be produced on the basis of a process as claimed in claim 8, containing a particulate filler, characterized in that the concentration of the filler in the layers for which the melt feed (2) into the manifold (3) takes place laterally with respect to the direction of extrusion (E) predetermined by the die outlet region deviates by no more than +/−

15% with respect to the web cross section in the center of the outer thirds of the film or sheet web and in the central region of the extruded web.

10. Coextruded films or sheets of thermoplastic material which can be produced on the basis of a process as claimed in claim 8, characterized in that the layer thickness of the layers for which the melt feed (2) into the manifold (3) takes place laterally with respect to the direction of extrusion (E) predetermined by the die outlet region deviates by no more than +/−

15% with respect to the web cross section in the center of the outer thirds of the film or sheet web and in the central region of the web.

11. Extruded or coextruded films or sheets as claimed in claim 9 or 10, characterized in that they consist of a polymethyl methacrylate plastic, an impact-modified polymethyl methacrylate plastic, a polycarbonate plastic, a polystyrene plastic, a styrene-acrylonitrile plastic, a polyethylene terephthalate plastic, a glycol-modified polyethylene terephthalate plastic, a polyvinyl chloride plastic, a transparent polyolefin plastic, an acrylonitrile-butadiene-styrene (ABS) plastic or combinations or mixtures (blends) of the plastics mentioned.