IP Library Granted Patent US 9,636,861
Granted Patent B2
US 9,636,861 · App. 14/112,094 · Granted May 2, 2017

Extrusion device and method for influencing wall thicknesses of an extruded plastic profile

Inventors: Erwin Krumböck (Ansfelden, AT); Leopold Weiermayer (Wartberg/Krems, AT); Karl Gebesmaier (Kirchdorf/Krems, AT)
Assignee: GREINER TOOL.TEC GMBH
B29C47/92B29C47/003B29C47/0023B29C47/0028B29C47/021B29C47/862B29C47/864B29C47/866B29C47/884B29C47/8835B29C47/904B29C47/905B29C2947/926B29C2947/92152B29C2947/92647B29C2947/92666B29C2947/92695B29C2947/92704B29C2947/92904
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Quick Facts
Patent No.
US 9,636,861
App. No.
14/112,094
Granted
May 2, 2017
Kind
B2
Abstract

The invention relates to an extrusion device and an extrusion method for the extrusion of plastic profiles, in particular a nozzle plate, comprising at least one flow channel for plastic melt. At least one wall region of the flow channel can be temperature controlled in a targeted manner with a local temperature control device for setting the flow speed of the plastic melt.

Claims (33)

1. An extrusion device for the extrusion of a plastic profile with at least one single walled profile section, in particular a nozzle plate, the extrusion device comprising:

at least one plastic melt flow channel for the at least one single walled profile section;

one or more other plastic melt flow channels for one or more other profile sections that exclude the at least one single walled profile section; and

at least one local temperature control device positioned proximate to at least one wall region of the at least one plastic melt flow channel for the at least one single walled profile section to temperature control in a targeted manner the at least one wall region of the at least one plastic melt flow channel for the at least one single walled profile section for setting the flow speed of the plastic melt through the at least one plastic melt flow channel for the at least one single walled profile,

wherein the extrusion device is devoid of local temperature control devices positioned proximate to the one or more other plastic melt flow channels.

2. The extrusion device according to claim 1 , wherein the at least one wall region of the at least one plastic melt flow channel for the at least one single walled profile section is temperature controlled up to 30° C. above or below an average temperature of an extrusion nozzle.

3. The extrusion device according to claim 1 , wherein the at least one local temperature control device is arranged in a spatial proximity to the at least one wall region of the at least one plastic melt flow channel for the at least one single walled profile section, in particular in proximity of an outlet opening of an extrusion nozzle.

4. The extrusion device according to claim 1 , wherein the at least one wall region to be temperature controlled is arranged between 0 to 100 millimeters (mm) upstream from an outlet of an extrusion nozzle and/or the at least one wall region has a length dimension of about 20 to 80 mm and/or a width dimension of about 3 to 20 mm.

5. The extrusion device according to claim 1 , wherein the at least one wall region to be temperature controlled is arranged in a nozzle outlet plate directly upstream of an outlet of an extrusion nozzle and the at least one wall region has a dimension in extrusion direction of 5 to 20 mm, and a dimension crosswise to the extrusion direction of about 20 to 150 mm.

6. The extrusion device according to claim 1 , wherein the at least one local temperature control device comprises at least one temperature control channel, at least one electrical heating means, in particular an induction or resistant heating and/or at least one thermoelectric element.

7. The extrusion device according to claim 6 , wherein the at least one local temperature control device comprises the at least one temperature control channel, and the at least one temperature control channel is flown through by a temperature control medium, in particular room air, cold and/or heated air, a gas and/or a liquid, wherein the flow through of a liquid occurs in particular in a closed cycle and the flow through of a gas occurs in an open cycle.

8. The extrusion device according to claim 7 , wherein the cooled temperature control medium has a temperature between −50 to 30° C. in case of a gas and a temperature between 15 and 180° C. in case of a liquid, wherein in particular only an outlet zone of an extrusion nozzle is cooled.

9. The extrusion device according to claim 7 , wherein the heated temperature control medium has a temperature between 250 to 500° C. in case of a gas and a temperature between 200 and 280° C. in case of a liquid, wherein in particular only an outlet zone of an extrusion nozzle is heated.

10. The extrusion device according to the claim 6 , wherein the at least one local temperature control device comprises the at least one temperature control channel, and the at least one temperature control channel comprises a width extension according to a width dimension of an assigned wall region of the flow channel for the single walled profile sections and/or that a gap size of the at least one temperature control channel is between 0.3 to 5 mm.

11. The extrusion device according to claim 1 , wherein the at least one local temperature control device is insulated thermotechnically in respect to an extrusion nozzle, in particular the nozzle plate, by an air gap and/or by means of a heat insulating intermediate layer such that higher temperature differences are effective on a surface of the at least one plastic melt flow channel for the at least one single walled profile section compared to on a surface of the one or more other plastic melt flow channels.

12. The extrusion device according to claim 1 , further comprising an operating or control device for controlling the at least one local temperature control device for influencing a wall thickness of the plastic profile, wherein at least one measured value is the wall thickness, a gap size in a calibration device, a spatial extension of the plastic profile after leaving an extrusion nozzle and/or a measured back pressure in the calibration device.

13. The extrusion device according to claim 1 , wherein at least one of a flow velocity, a rate of flow, a pressure or a temperature of a temperature control medium, in particular air, is set in a targeted manner before being fed into the at least one local temperature control device.

14. The extrusion device according to claim 1 , further comprising an operating or control device for a timely change of a temperature of the at least one wall region of the at least one plastic melt flow channel for the at least one single walled profile section, in particular for setting a temperature transition of 5 to 15 K/min.

15. The extrusion device according to claim 1 , further comprising a throttle device for setting a throughput of a temperature control medium in the at least one local temperature control device in a targeted manner, wherein the throttle device is coupled in particular to an operating or control device.

16. The extrusion device according to claim 1 , further comprising a thermal insulating device for a temperature control medium for at least one sub region in the nozzle plate.

17. The extrusion device according to claim 16 , wherein the insulating device comprises an air gap and/or an insulating material.

18. An extrusion device for the extrusion of a plastic profile with a plurality of single walled profile sections, in particular a nozzle plate, the extrusion device comprising:

a plurality of plastic melt flow channels for the plurality of single walled profile sections;

a main plastic melt flow channel for a main profile section that excludes the plurality of single walled profile sections; and

at least one local temperature control device positioned proximate to:

a single outer wall region of the main plastic melt flow channel for the main profile section;

at least one wall region of a first plastic melt flow channel for a first single walled profile section, wherein the first plastic melt flow channel is positioned at a first end of the single outer wall region of the main plastic melt flow channel; and

at least one wall region of a second plastic melt flow channel for a second single walled profile section, wherein the second plastic melt flow channel is positioned at a second end of the single outer wall region of the main plastic melt flow channel that is opposite the first end,

wherein the at least one local temperature control device is configured to temperature control in a targeted manner the single outer wall region of the main plastic melt flow channel and the at least one wall region of each of the first and second plastic melt flow channels for setting glossiness of portions of the main profile section and the first and second single walled profile sections that pass by the single outer wall region of the main plastic melt flow channel and the at least one region of each of the first and second plastic melt flow channels;

wherein the extrusion device is devoid of local temperature control devices positioned proximate to at least some remaining outer wall regions of the main plastic melt flow channel, the at least some remaining outer wall regions of the main plastic melt flow channel excluding the single outer wall region of the main plastic melt flow channel.

19. The extrusion device according to claim 18 , wherein the single outer wall region of the main plastic melt flow channel for the main profile section and the at least one wall region of each of the first and second plastic melt flow channels for the first and second single walled profile sections are temperature controlled up to 30° C. above or below an average temperature of an extrusion nozzle.

20. The extrusion device according to claim 18 , wherein the at least one local temperature control device comprises a single temperature control device arranged in spatial proximity to an outlet opening of an extrusion nozzle.

21. The extrusion device according to claim 18 , wherein the at least one local temperature control device has a dimension in extrusion direction of less than 10 mm to influence a glossiness of portions of the main profile section and the first and second single walled profile sections that pass by the single outer wall region of the main plastic melt flow channel and the at least one region of each of the first and second plastic melt flow channels without influencing wall thickness.

Assignments (4)
CHANGE OF NAME Recorded Jul 26, 2024
From: GREINER EXTRUSION GROUP GMBH
To: EXELLIQ HOLDING GMBH
Reel/Frame 068100/0374 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 26, 2024
From: EXELLIQ HOLDING GMBH
To: EXELLIQ AUSTRIA GMBH
Reel/Frame 066259/0090 →
CHANGE OF NAME Recorded Aug 6, 2019
From: GREINER TOOL.TEC GMBH
To: GREINER EXTRUSION GROUP GMBH
Reel/Frame 049966/0750 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 16, 2013
From: KRUMBOECK, ERWIN; WEIERMAYER, LEOPOLD; GEBESMAIER, KARL
To: GREINER TOOL.TEC GMBH
Reel/Frame 031421/0298 →
Priority Claims (1)
DE 10 2011 007 618 · Apr 18, 2011 · national
Continuity (1)
Related Publication 20140035189A1 · Feb 6, 2014