Method for producing a multilayer coextrudate and a coextrudate produced according thereto

Information

  • Patent Grant
  • 6777053
  • Patent Number
    6,777,053
  • Date Filed
    Monday, May 7, 2001
    23 years ago
  • Date Issued
    Tuesday, August 17, 2004
    20 years ago
Abstract
Process for the production of a multilayer coextrudate with a plastic layer that has release properties with respect to adhesives, where the materials producing the release properties are located within the plastic layer, where a first web is provided in production of the coextrudate on one side of which a layer of adhesive is located, after which the plastic layer with the release properties follows, which is in turn bonded to a second web. A multilayer coextrudate is characterized by the fact that at least two plastic films are provided, between which a layer of adhesive and a further layer that has release properties with respect to the adhesive are located.
Description




BACKGROUND OF THE INVENTION




Field of the Invention




The invention relates to a process for the production of a multilayer coextrudate with a plastic layer that has release properties with respect to adhesives, where the materials producing the release properties are located within the plastic layer.




SUMMARY OF THE INVENTION




The purpose of the invention is to indicate a process of the kind outlined above with which a composite material consisting of a web, an adhesive, a release layer and a further web for the release layer can be produced in an efficient way.




In the solution to this problem proposed by the invention, a first web is provided in production of the coextrudate on one side of which a layer of adhesive is located, after which the plastic layer with the release properties follows, which is in turn bonded to a second web.




At least the basic structure of the composite material is produced in a single operation by this coextrusion process.




It has proved to be particularly favourable in this context if in accordance with a further development of the invention the layers of the coextrudate are coextruded simultaneously.




Particularly efficient production of the entire layer structure is achieved as a result.




In a particularly advantageous development of the invention, the layers are extruded simultaneously by the blown film process.




It is, however, also possible in accordance with a further development of the invention that the layers are produced by the cast film process.




In accordance with a further advantageous development of the invention, it is possible that a substrate web, to which the other layers are extruded in a single process operation, is provided as the first or second web.




This process is particularly favourable especially when a web is being used that is difficult or impossible to extrude at the same time, as all the other layers can be applied to the web that is acting as the substrate web in a single operation.




It is also very advantageous if in accordance with a further development of the invention a plastic film, to which the other layers are extruded in a single process operation, is provided as the substrate web.




A further advantageous development of the invention is characterised by the fact that at least the substrate web is oriented.




The coextrudate receives favourable strength properties as a result.




It is also possible in accordance with an advantageous development of the invention that the entire coextrudate is oriented.




All the layers that can be oriented can help to increase the strength properties in this case.




In accordance with an advantageous development of the invention, a multilayer coextrudate has at least two plastic films, between which a layer of adhesive and a further layer that has release properties with respect to the adhesive are located.




In a further advantageous development of the invention, further layers are provided that are located on either or both sides of the plastic films. Thus both elastic films are each provided with a further layer bonded to the plastic films.




It has proved to be very advantageous if in accordance with a further development of the invention at least part of the coextrudate structure is oriented.




Considerable increases in strength are achieved by orienting the substrate web or the finished coextrudate.











BRIEF DESCRIPTION OF THE DRAWINGS




Two embodiments of the invention are illustrated in the drawings:





FIG. 1

is a diagrammatic view of the structure of a composite material that consists of four layers and





FIG. 2

shows a further composite material consisting of five layers, again in a diagrammatic view.











DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS






1


in

FIG. 1

is a composite material that consists of four layers and has been produced by the coextrusion process. A layer of adhesive


3


, next to which a further layer


4


that has release properties with respect to the adhesive is located, is provided on one side of a first web


2


. This release layer


4


is in turn bonded to a second web


5


. If both of the webs


2


and


5


are made from a coextrudable plastic, all four layers can be produced simultaneously, not only by the blown film process but also by the cast film process. It is, however, also possible to coat the web


2


or the web


5


with the other layers subsequently by the coextrusion process.





FIG. 2

shows a further composite material


21


that consists of five layers. What is involved here is a web


22


that acts as the substrate layer for a release layer


24


. This release layer


24


faces a layer of adhesive


23


that is bonded to a web


25


made of plastic. This web


25


, which acts as the core layer, has a surface layer


26


on its side facing away from the layer of adhesive


23


. Such a surface layer can also be provided on the web


22


that acts as the substrate layer for the release layer.




Different plastics can be used as the substrate layer for the release layer.




Good properties have, for example, been achieved with LDPE, LLDPE, HDPE, PP, mPE, PETP and PS, in each case 20 to 40 μ thick, while the actual release layer was 5 to 10 μ thick.




PP, OPP, PE, LDPE, LLDPE, mPE, PS and PET have been used very successfully for the web that supports the adhesive, with material thicknesses between 60 and 200 μ, depending on the material used. This web has in some cases been provided with an additional coating on the outside to improve printability.




The webs have in some cases been divided up into several individual layers made from different materials too.




Extrudable, permanently tacky adhesives based on hotmelts and polyolefins with appropriate tackifying additives have been used successfully as adhesives.




EXAMPLE 1




Use of SIS, SBS, SEBS and SEP block copolymers with melt indices of between 8 and 65 g/10 min at 200° C. and 5 kg. The styrene content of the polymers varies between 10 and 35%. The properties of the adhesive layer are controlled by the addition of resins and plasticisers, e.g. by means of aliphatic hydrocarbon resins, polyterpene resins, hydrolysed hydrocarbon resins, aromatic hydrocarbon resins, paraffin waxes, microcrystalline waxes, polyisobutylene and process oils.




Liquid components are processed into an extrudable formn by carrying out a compounding operation first. The extrusion temperatures vary between 100 and 240° C., avoiding excessively high shear forces at the same time.




EXAMPLE 2




Another way to produce the adhesive layer involves the inclusion of UV acrylates or UV-curing PSAs between the coextruded substrate and release layers by using melt transport technology.




The radiation-cured basic materials are, for example, acrylate copolymers with an integrated photoinitiator. UV cross-linking is carried out by the polymer substrate layer for the adhesive.




The acrylate copolymers can be modified by resins and plasticisers, while the tack of the adhesive layer can be regulated via the radiation dose.




Typical radiation wavelengths for cross-linking purposes are in the range between 250 and 260 nm (UVC).




Typical processing temperatures for the acrylate copolymers are between 110 and 150° C.




If a substrate web is used that is coated by the coextrusion process, it is possible to orient not only the substrate web alone but also the finished coextrudate in order to increase the strength properties.




If the entire structure is produced as a coextrudate, this coextrudate can also be oriented subsequently to increase the strength properties.




LDPE=low density polyethylene




LLDPE=linear low density polyethylene




HDPE=high density polyethylene




mPE=metallocene catalyzed polyethylene




PET=polyethylene terephthalate




PETP=polyethylene terphthalate polymer




PP=polypropylene




OPP=oriented polypropylene




PS=polystyrene




SIS=styrene isoprene styrene




SBS=styrene butadiene styrene




SEBS=styrene ethylene butadiene styrene




PSA=pressure sensitive adhesive




SEP=styrene ethylene propylene




UV=ultra violet




UVC=ultra violet curing



Claims
  • 1. Process for the production of a multilayer coextrudate with a plastic layer that has release properties with respect to adhesives, comprisinglocating materials producing the release properties within the plastic layer, wherein a first plastic web film (2, 22) is provided in production of the coextrudate on one side of which a layer of adhesive (3, 23) is located, after which the plastic layer (4, 24) with the release properties follows, which is in turn bonded to a second plastic web film (5, 25); and wherein the layers of the coextrudate are coextruded simultaneously; and wherein further layers (26) are provided that are located on and bonded to both sides of the plastic web films (2, 5 or 22, 25), such that both plastic web films are each provided with a further layer (26) bonded to the plastic films.
  • 2. Process according to claim 1, wherein the layers are extruded simultaneously by the blown film process.
  • 3. Process according to claim 1, wherein the layers are produced by the cast film process.
  • 4. Process according to claim wherein a substrate web (2,5; 22,25), to which the other layers are extruded in a single process operation, is provided as the first or second web.
  • 5. Process according to claim 1, wherein a plastic film, to which the other layers are extruded in a single process operation, is provided as the substrate web (2, 5; 22, 25).
  • 6. Process according to claim 1, wherein at least the substrate web is oriented.
  • 7. Process according to claim 6, wherein the entire coextrudate is oriented.
  • 8. Multilayer coextrudate produced in accordance with the process as described in claim 1, wherein at least two plastic web films (2, 5; 22, 25) are provided, between which a layer of adhesive (3, 23) and a further layer (4, 24) that has release properties with respect to the adhesive are located.
  • 9. Multilayer coextrudate according to claim 8, wherein at least part of the coextrudate structure is oriented.
Priority Claims (1)
Number Date Country Kind
198 51 105 Nov 1998 DE
CROSS REFERENCE TO RELATED APPLICATIONS

Applicant claims priority under 35 U.S.C. §119 of German Application No. 198 51 105.1 filed Nov. 6, 1998. Applicant also claims priority under 35 U.S.C. §365 of PCT/EP99/08405 filed Nov. 3, 1999. The international application under PCT article 21 (2) was not published in English.

PCT Information
Filing Document Filing Date Country Kind
PCT/EP99/08405 WO 00
Publishing Document Publishing Date Country Kind
WO00/27940 5/18/2000 WO A
US Referenced Citations (5)
Number Name Date Kind
4339485 Shibano et al. Jul 1982 A
4626460 Duncan Dec 1986 A
4867818 Morgan Sep 1989 A
5605717 Simmons et al. Feb 1997 A
5807632 Pedginski Sep 1998 A
Foreign Referenced Citations (3)
Number Date Country
195 48 265 Jun 1997 DE
55 080479 Jun 1980 JP
59 122570 Jul 1984 JP