WO2002051630A2 - Multilayer barrier shrink films and process for their manufacture - Google Patents

Multilayer barrier shrink films and process for their manufacture Download PDF

Info

Publication number
WO2002051630A2
WO2002051630A2 PCT/IL2001/000856 IL0100856W WO02051630A2 WO 2002051630 A2 WO2002051630 A2 WO 2002051630A2 IL 0100856 W IL0100856 W IL 0100856W WO 02051630 A2 WO02051630 A2 WO 02051630A2
Authority
WO
WIPO (PCT)
Prior art keywords
class
layers
layer
polymers
multilayer
Prior art date
Application number
PCT/IL2001/000856
Other languages
French (fr)
Other versions
WO2002051630A3 (en
Inventor
Israel Sarid
Arthur Bobovitch
Yiftach Nir
Original Assignee
Syfan Saad (99) Ltd.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Syfan Saad (99) Ltd. filed Critical Syfan Saad (99) Ltd.
Priority to AU2001288035A priority Critical patent/AU2001288035A1/en
Publication of WO2002051630A2 publication Critical patent/WO2002051630A2/en
Publication of WO2002051630A3 publication Critical patent/WO2002051630A3/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/06Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B27/08Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/09Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
    • B29C48/10Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels flexible, e.g. blown foils
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/16Articles comprising two or more components, e.g. co-extruded layers
    • B29C48/18Articles comprising two or more components, e.g. co-extruded layers the components being layers
    • B29C48/185Articles comprising two or more components, e.g. co-extruded layers the components being layers comprising six or more components, i.e. each component being counted once for each time it is present, e.g. in a layer
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C55/00Shaping by stretching, e.g. drawing through a die; Apparatus therefor
    • B29C55/28Shaping by stretching, e.g. drawing through a die; Apparatus therefor of blown tubular films, e.g. by inflation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/30Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers
    • B32B27/306Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers comprising vinyl acetate or vinyl alcohol (co)polymers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/32Layered products comprising a layer of synthetic resin comprising polyolefins
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/34Layered products comprising a layer of synthetic resin comprising polyamides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B38/00Ancillary operations in connection with laminating processes
    • B32B38/0012Mechanical treatment, e.g. roughening, deforming, stretching
    • B32B2038/0028Stretching, elongating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2250/00Layers arrangement
    • B32B2250/022 layers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2250/00Layers arrangement
    • B32B2250/24All layers being polymeric
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2307/00Properties of the layers or laminate
    • B32B2307/70Other properties
    • B32B2307/724Permeability to gases, adsorption
    • B32B2307/7242Non-permeable
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2307/00Properties of the layers or laminate
    • B32B2307/70Other properties
    • B32B2307/732Dimensional properties
    • B32B2307/734Dimensional stability
    • B32B2307/736Shrinkable
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2323/00Polyalkenes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2329/00Polyvinylalcohols, polyvinylethers, polyvinylaldehydes, polyvinylketones or polyvinylketals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2377/00Polyamides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2439/00Containers; Receptacles
    • B32B2439/70Food packaging
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2553/00Packaging equipment or accessories not otherwise provided for
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B37/00Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding
    • B32B37/14Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the properties of the layers
    • B32B37/15Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the properties of the layers with at least one layer being manufactured and immediately laminated before reaching its stable state, e.g. in which a layer is extruded and laminated while in semi-molten state
    • B32B37/153Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the properties of the layers with at least one layer being manufactured and immediately laminated before reaching its stable state, e.g. in which a layer is extruded and laminated while in semi-molten state at least one layer is extruded and immediately laminated while in semi-molten state

Definitions

  • This invention relates to novel shrinkable, multilayer film structures
  • Heat-shrinkable multilayer film structures useful particularly for
  • films having a layer of a hydrolyzed ethylene-vinyl acetate copolymer having a layer of a hydrolyzed ethylene-vinyl acetate copolymer
  • US 5,114,795 discloses a multilayered gas barrier film which comprises at
  • polymer is functionalized for compatibility with the gas barrier polymer so
  • the gas barrier properties is modified so as to provide good adhesion to a
  • a gas barrier layer comprising a non-chlorine-containing
  • composition contained within at least one layer of said film.
  • the multilayer film described in this reference has at least one
  • PCE polymer cross-linking enhancer
  • polyene monomer at least one C2-C20 olefinic monomer, and further
  • polymeric units derived from said polyene monomer and at least one
  • polymer having polymeric units derived from at least one C2-C20 olefinic
  • At least one layer forming a major surface of the film is sealable.
  • the outer layer has a high degree of cross-linking
  • the inner layer has a low degree of cross-linking.
  • an internal EVOH has to be
  • EVOH provides high oxygen barrier properties
  • the barrier properties are inferior to pure EVOH, or to cross-link the primary extruded tube by electron-beam irradiation.
  • heat-shrinkable polymeric structure which can be easily oriented for
  • the present invention provides a multilayer polymeric film, particularly a
  • the invention further provides a process for producing the aforesaid
  • multilayer structures which comprises co-extruding a plurality of the
  • Class A Class A
  • B Class A
  • C Class A
  • D Class A
  • Class A a layer comprising polyethylene polymers and copolymers of
  • ethylene copolymers such as EVA, EBA, EAA
  • Class B a tie layer comprises of maleic anhydride grafted polyolefins, such
  • ADMERTM NF 478 or NF578 Ex Mitsui Chemicals
  • BYNEL BYNEL
  • Class C barrier layers essentially consisting of ethylene vinyl alcohol
  • Class D polyamides, such as N-MXD6 (a unique aliphatic polyamide resin
  • the invention in particular preferred embodiments, may provide a three
  • - Fig. 1 is a schematic illustration of the double-bubble process
  • FIG. 2 is a schematic illustration of a five-layer film
  • FIG. 3 is a schematic illustration of a seven-layer film.
  • the production of a polymer film begins with the melting of a polymer
  • Fig. 1 the double-bubble technique for making the film is schematically
  • Air pressure separates the inner surfaces of
  • MD orientation is produced by stretching the tube
  • the second bubble is axially cut and rolled
  • ultraviolet oven (11) may be added at any location between the tape
  • cross-linking agent if required.
  • film may be processed after extrusion in the same way as a single-layer
  • Fig. schematically illustrates a five-layer structure (A B/C/B/A), in which
  • the outer layers (A) are PE, adjacent to a tie layer (B) and the central
  • Nylon N-MXD6 (C).
  • polymeric structures are formed, preferably forming a heat shrinkable
  • layers are selected from the group consisting of ethylene copolymers, a tie layer comprising maleic anhydride grafted polyolefins, ethylene vinyl
  • external layers comprise polyethylene copolymers.
  • process comprises coextruding several layers of the selected from the
  • a five-layer structure A/B/C/B/A- was produced as follows:
  • the external "skin" layers A comprised 97% LLDPE, Dowlex 5056 ex
  • Layer B was a tie layer, comprised of 100% NF578 ex, Mitsui chemicals.
  • Layer C the central layer, was Nylon N-MXD6 6007.
  • the primary tube thickness was 230 microns.
  • a five-layer extrusion line manufactured by Kuhne was used. The
  • extrusion temperature was that known for N-MXD6 extrusion, i.e., 250-
  • the barrel temperature was: PE and tie 220°C, MXD-6 250°C.
  • the die Temp was : 250°C.
  • a film of 25 microns thickness was obtained by orientation of the tube:
  • Relative thickness PE-5.5, Tie-2, N- MXD6 - 10.
  • a seven-layer structure was produced forming the following structure:
  • A/B/C/D/C/B/A having relative layer thicknesses of 26/4/12/16/12/4/26 %
  • the polymers used were:
  • a 250 micron primary tube was oriented to produce a 25 micron thick film.
  • the relative thickness of each layer was :
  • EVOH layer was E-105B ex By EVAL Europe (density: 1.14 gr/cc). The
  • the thickness of the layers was: PE-5.5, Tie-2, MXD-6- 4,
  • EVOH-2 Total thickness 25 microns.
  • Example 3 The same conditions as described for Example 3 were:
  • a seven-layer structure (A/B/C/D/C/B/A), was produced in the same
  • a five-layer structure (A/B/C/B/A), was produced in the same conditions as
  • Example 3 The relative thicknesses were 37/5/16/5/37%, respectively.
  • the total film thickness was 25 microns.

Abstract

Multilayer polymeric structures, particularly heat-shrinkable structures, wherein the polymers of which the layers tat are formed are chosen from the following calsses: Class A: a sealing and humidity-protection layer essentially consisting of ethylene copolymers and ethylene/alpha-olefin copolymers and blends thereof; Class B: a tie layer essentially consisting of maleic anhydride grafted polyethylenes; and, in any order; Class C: barrier layers essentially consisting of ethylene vinyl alcohol copolymers (EVOH), or EVOH containing up to 30% of a polyamide; or Class D: polyamides, such that when Class C and Class D polymers are found on adjacent layers, they cannot be the same.

Description

MULTILAYER BARRIER SHRINK FILMS AND PROCESS FOR
THEIR MANUFACTURE
Field of the Invention
This invention relates to novel shrinkable, multilayer film structures,
comprising specific compatible contiguous layers, particularly useful for
flexible packaging, e.g. of food, and to a method for their manufacture.
Background of the Invention
Heat-shrinkable multilayer film structures, useful particularly for
packaging purposes, are known in the art, and various structures of such
fils and methods for their manufacture have been described.
US Patent No. 4,064,296 describes heat-shrinkable multilayer packaging
films having a layer of a hydrolyzed ethylene-vinyl acetate copolymer,
preferably formed by coextruding a layer of such copolymer between two
other polymeric layers, at least one of which is cross-linkable, and
thereafter orienting the multilayer structure.
US 4,643,943 describes an oriented multilayer film comprising five layers,
a cross-linked core layer, two cross-linked interior layers and two
cross-linked surface layers. US 5,114,795 discloses a multilayered gas barrier film which comprises at
least one layer of polymer having low permeability to moisture and a
polymer blend layer containing a gas barrier polymer, wherein the second
polymer is functionalized for compatibility with the gas barrier polymer so
as to allow the polymer blend layer to adhere to the first polymer layer. A
unique feature of these structures is said to be that the layer, providing
the gas barrier properties, is modified so as to provide good adhesion to a
polyolefin or other moisture barrier layer bonded thereto, without the
necessity of a separate, adhesive tie layer.
US 5,895,694 describes a chlorine-free multilayer film material which
comprises a gas barrier layer comprising a non-chlorine-containing
organic polymer, two tie layers, each contacting one side of said barrier
layer, an inner surface layer, and an outer surface layer.
US 5,993,922 relates to polymeric compositions capable of providing
enhanced cross-linking efficiency, to single and multilayer films having
the said composition contained within at least one layer of said film. It
further relates to a method of treating said film to provide enhanced
cross-linking within selected layers of the film, and to the resulting
cross-linked film product and articles made from said cross-linked film product. The multilayer film described in this reference has at least one
layer containing a polymer cross-linking enhancer (PCE) composition
comprising a copolymer having polymeric units derived from at least one
polyene monomer, at least one C2-C20 olefinic monomer, and further
comprising a polymeric mixture comprising at least one polymer having
polymeric units derived from said polyene monomer, and at least one
polymer having polymeric units derived from at least one C2-C20 olefinic
monomer, each of at least one layer formed with PCE composition being
cross-linked to a greater degree than at least one layer of said film and at
least one layer forming a major surface of the film is sealable.
US 6,051,292 discloses a multilayer packaging film comprising layers
having various degrees of cross-linking when subjected to electron beam
radiation, wherein the outer layer has a high degree of cross-linking and
the inner layer has a low degree of cross-linking.
The prior art has dealt with two difficulties. First of all, in order to
achieve satisfactory barrier properties, an internal EVOH has to be
introduced into the film. EVOH provides high oxygen barrier properties,
however, it is very cumbersome to stretch it in the double-bubble process
and to achieve high shrinkage. The solution is to either blend it with
Nylon, but then the barrier properties are inferior to pure EVOH, or to cross-link the primary extruded tube by electron-beam irradiation. The
later process requires expensive equipment. In addition the barrier
properties of film with EVOH is diminished by humidity.
It is therefore a purpose of this invention to provide a multilayer
structure, particularly a heat-shrinkable film, with high oxygen and
moisture barrier, polymeric structure in which the various layers are
chemically strongly bonded.
It is another purpose of this invention to provide a multilayer barrier
heat-shrinkable polymeric structure, which can be easily oriented for
example in a double-bubble process, without the need for irradiation and
while achieving satisfactory shrinkage properties.
It is still a further purpose of this invention to provide such a structure,
which allows to manufacture film with high barrier properties, equal to
those achieved in a five-layer structure containing pure EVOH as a
barrier layer.
It is yet another purpose of the invention to provide a film structure, in
which the barrier properties are not affected by the film exposure to high
humidity. It is still a further purpose of the present invention to provide a process for
the manufacture of such multilayer polymer films.
Other purposes and advantages of the invention will appear as the
description proceeds.
Summary of the Invention
The present invention provides a multilayer polymeric film, particularly a
heat-shrinkable and gas barrier film, which is made of specific compatible
layers provided between the contiguous layers thereof.
The invention further provides a process for producing the aforesaid
multilayer structures, which comprises co-extruding a plurality of the
several specific film layers. The different layers must be bonded to each
other to form a multilayer structure. The various layers have preferred
chemical natures, which can be classified in four different classes. Said
classes will be designated as Class A, B, C and D, for the sake of brevity.
Class A: a layer comprising polyethylene polymers and copolymers of
higher α-olefines or blend of different such copolymers, preferably — but
not limitatively - with densities from 0.87gr/cm3 to 0.95 gr/cm3, and melting temperatures preferably - but not limitatively - from 70°C to
135°C; or, alternatively, ethylene copolymers, such as EVA, EBA, EAA
and EMA, alternatively, ionomers, copolymers of ethylene and methacrylic
acid, thermally linked to metal ions (e.g., Surlyn Ex. DuPont).
Class B: a tie layer comprises of maleic anhydride grafted polyolefins, such
as ADMER™ NF 478 or NF578 (Ex Mitsui Chemicals), or BYNEL
( Ex Du Pont).
Class C: barrier layers essentially consisting of ethylene vinyl alcohol
copolymers (EVOH), or EVOH containing up to 30% of a polyamide, and
Class D: polyamides, such as N-MXD6 (a unique aliphatic polyamide resin
containing meta-xylene groups, and copolyamides, such as Nylon 6/12
(nylon 6 to nylon 12 ratio 1:1).
When C and D are adjacent, the two layers should be chemically different,
but should be compatible to adhere one to the other.
The invention, in particular preferred embodiments, may provide a three
or more layer structure. Indicating by A, B, C and D respectively any
polymers of the above classes A, B , C and D respectively, a five-layer structure may be symbolized by A/B/C/B/A and a seven-layer structure
may be symbolized as A/B/C/D/C/B/A.
Brief Description of the Drawings
In the drawings:
- Fig. 1 is a schematic illustration of the double-bubble process;
- Fig. 2 is a schematic illustration of a five-layer film; and
- Fig. 3 is a schematic illustration of a seven-layer film.
Detailed Description of Preferred Embodiments
The production of a polymer film begins with the melting of a polymer
composition, followed by its extrusion through a die. This extrudate is
further processed, e.g. by tenter drawing or double-bubble orientation, to
give the polymer film with its desired thickness and properties.
In Fig. 1 the double-bubble technique for making the film is schematically
illustrated. Polymer granules from a feeder (1) are melted in an extruder
(2). The melted polymer is continuously pushed through an annular die (6)
to produce a tubular tape that is inflated by air flowing around a mandrel
to form a first bubble (3) which is externally cooled by a quenching water
flow (4). After passing through a quench bath (5), the first bubble has
already solidified, and the tape is collapsed and transported by the use of nip rollers (9) to an oven or to hot water bath (7), which brings the tape to
its orientation temperature. Air pressure separates the inner surfaces of
the tube and produces the second bubble (8). The circumference of the
bubble is several-fold larger than that of the tube, and the tube is
oriented in the transverse direction (TD) by this stretching. In the
machine direction (MD) orientation is produced by stretching the tube
longitudinally, the rollers at the entrance to the stretching zone, before
the bubble, rotating at a peripheral speed which is several-fold lower than
the exit speed. After cooling, the second bubble is axially cut and rolled
onto spindles (10) for packaging and further processing (racking). An
ultraviolet oven (11) may be added at any location between the tape
solidification point and the second bubble. In this case, the formulation
includes a suitable concentration of an appropriate photo-initiator, and a
cross-linking agent if required.
By using a coextrusion die, more than one layer can be simultaneously
extruded, each layer with the same or different polymer composition to
form a multilayer film. In the case of the double-bubble technique, the die
will be coaxial annular die where the number of passageways is
determined by the number of layers desired in the produced film. When two contiguous layers are compatible, that it to say when they bind
sufficiently well to each other when coextruded in their molten states, the
film may be processed after extrusion in the same way as a single-layer
film.
However, incompatible layers must be bound together using an
intermediate adhesive (or tie) layer.
Fig 2. schematically illustrates a five-layer structure (A B/C/B/A), in which
the outer layers (A) are PE, adjacent to a tie layer (B) and the central
layer is Nylon, N-MXD6 (C).
The formation of a seven-layer structure (A B/C/D/C/B/A), is schematically
shown in Fig. 3, in which the outer layer is PE (A), adjacent to a tie layer
(B) and the three central layers are Nylon, N-MXD6 (C) and EVOH (D).
According to a preferred embodiment of the invention multilayer
polymeric structures are formed, preferably forming a heat shrinkable
film.
According to another preferred embodiment of the invention the film
layers are selected from the group consisting of ethylene copolymers, a tie layer comprising maleic anhydride grafted polyolefins, ethylene vinyl
alcohol copolymers and polyamides.
According to yet another preferred embodiment of the invention the film is
produced using the double-bubble technique.
According to a further preferred embodiment of the invention, the two
external layers comprise polyethylene copolymers.
According to a preferred embodiment of the invention the film production
process comprises coextruding several layers of the selected from the
above polymer groups.
All the above and other characteristics and advantages of the invention
will be further explained through the following illustrative and
non-limitative examples.
Example 1
A five-layer structure, A/B/C/B/A- was produced as follows:
The external "skin" layers A comprised 97% LLDPE, Dowlex 5056 ex
DOW and 3% antiblock masterbatch ( synthetic silica). When not otherwise indicated percentages given in respect of material contents are
by weight.
Layer B was a tie layer, comprised of 100% NF578 ex, Mitsui chemicals.
Layer C, the central layer, was Nylon N-MXD6 6007.
The above structure was formed by extrusion of the different polymers,
which lead to an A/B/C/B/A structure having relative thicknesses of
34/8/16/8/34 %, respectively. The primary tube thickness was 230 microns.
A five-layer extrusion line manufactured by Kuhne was used. The
extrusion temperature was that known for N-MXD6 extrusion, i.e., 250-
270°C. The barrel temperature was: PE and tie 220°C, MXD-6 250°C.
The die Temp was : 250°C.
A film of 25 microns thickness was obtained by orientation of the tube:
Relative thickness ( microns): PE-5.5, Tie-2, N- MXD6 - 10.
Stretching ratio (MDxTD): 3.3x2.7
OTR ( Oxygen Transmission Rate)- 12 cc/m2/day/atm/ @ 23°C,
90% RH( Relative Humidity)
Shrink % @ 95°C ( MD/TD) - 29/27 Example 2
A seven-layer structure was produced forming the following structure:
A/B/C/D/C/B/A, having relative layer thicknesses of 26/4/12/16/12/4/26 %,
respectively. The above structure was obtained by extrusion, using the
same conditions as described in Example 1.
The polymers used were:
Layer A- LLDPE 5056E ( DOW), density 0.92 g/cm3, Layer B- Tie, NF578
(Mitsui), density 0.91 g/cm3, Layer C- N-MXD6 (MGC) , density 1.22g/cm3,
Layer D- EVOH G156B (Kuraray), density 1.12 g/cm3-.
A 250 micron primary tube was oriented to produce a 25 micron thick film.
The relative thickness of each layer was :
6.5, B- 1, C- 3, D- 4 microns.
OTR- 17 cc/m2/day/atm/ @ 25°C and RH 0 and 90%
Shrink % - 90°C MD/TD - 28/30 Example 3
The production of other seven-layer structures is exemplified as follows:
The following structure was extruded A/B/C/D/C/B/A having relative %
thicknesses of 26/4/12/16/12/4/26, respectively.
The same procedure as described in Example 2 was employed, but the
EVOH layer was E-105B ex By EVAL Europe (density: 1.14 gr/cc). The
conditions were:
Barrel Temp. : PE and Tie: 220°C, N-MXD6 250°C, EVOH 230° C
The die Temp: 250°C
The thickness of the layers (microns) was: PE-5.5, Tie-2, MXD-6- 4,
EVOH-2. Total thickness 25 microns.
Stretching ratio (MDxTD) 3x3
OTR- 7.7 cc/m2/day/atm/ @ 23°C, 0 % RH.
Shrink % @ 95°C ( MD/TD) - 35/31
Example 4
A seven-layer film structure. The relative layer thickness % ratio was as
in Example 3. The same conditions as described for Example 3 were
employed, but a different Nylon was used, i.e., F28 Ex EMS. The same results for the film thickness and stretching ratio were obtained
as in Example 3.
OTR- 17.6 cc/m2/day/atm/ @ 23°C, 0% RH
Shrink % @ 95°C (MD/TD) - 31/29
Example 5
The same conditions as in Example 4 were used, except for the tie layer
which was NF498 Ex Mitsui Chemicals, and the Nylon layer which was
N-MXD6 6007.
OTR- 9.7 cc/m2/day/atm/ @ 23°C, 90% RH
Shrink % @ 95°C (MD/TD) - 31/34
Example 6
A seven-layer structure (A/B/C/D/C/B/A), was produced in the same
conditions as in Example 2. The relative layer thicknesses were
21/5/18/12/18/5/21%, respectively. Total thickness 25 microns.
Layer A - LLDPE ( 5056E Ex. DOW)
Layer B - Tie (NF 578 Ex. Mitsui Chemicals)
Layer C - Copolyamide Nylon 6/12, (CF6 Ex. EMS)
Layer D- EVOH (G156B Ex. Kuraray) OTR- 29 cc/m2/day/atm/ @ 25°C, 0% RH
65 cc/m2/day/atm/ @ 25°C, 90% RH
Shrink % @ 90°C (MD/TD)- 20/24
Example 7
A five-layer structure (A/B/C/B/A), was produced in the same conditions as
in Example 3. The relative thicknesses were 37/5/16/5/37%, respectively.
The total film thickness was 25 microns.
Layer A - LLDPE (5056E Ex. DOW)
Layer B - Tie ( NF 578 Ex. Mitsui Chemicals)
Layer C - EVOH and Copolyamide Nylon (E105B Ex. Kuraray +
10% CF6 Ex. EMS)
OTR - 32 cc/m2/day/atm/ @ 25°C, 0% RH
78 cc/m2/day/atm/ @ 25°C, 90% RH
Shrink % 90°C (MD/TD) - 20/24
While embodiments of the invention have been described by way of
illustration, it will be understood that the invention can be carried out by
persons skilled in the art with many modifications, variations and adaptations, without departing from its spirit or exceeding the scope of the
claims.

Claims

1. Multilayer polymeric structures, particularly heat-shrinkable
structures, wherein the polymers of which the layers are formed are
chosen from the group consisting of:
Class A: a sealing and humidity-protection layer essentially
consisting of ethylene copolymers and ethylene/alpha-olefin copolymers
and blends thereof;
Class B: a tie layer essentially consisting of maleic anhydride
grafted polyethylenes; and, in any order:
Class C: barrier layers essentially consisting of ethylene vinyl
alcohol copolymers (EVOH), or EVOH containing up to 30% of a
polyamide, and
Class D: polyamides;
wherein, when Class C and Class D polymers are found on adjacent layers
they cannot be the same.
2. Multilayer structures according to claim 1, comprising five or more
layer structures.
3. A structure according to claim 1, wherein the Class C and/or Class D
polymers comprise Nylon or MXD6.
4. Multilayer structure according to claim 2, comprising two outer
layers of class A polymer and an inner layer of class B polymer.
5. Multilayer structure according to claims 2 or 3, comprising two outer
layers of class A polymers, a central layer of class C polymers, and two
intermediate layers of class B polymers.
6. Multilayer structure according to claims 2 or 3, comprising two outer
layers of polymers of class A, two central layers of polymers of class C, and
one central layer of polymers of class D, and two intermediate layers of
polymers of class B.
7. Process for the manufacture of multilayer polymeric structure,
particularly shrinkable structure for packaging purposes, which comprises
co-extruding a plurality of layers of different polymer compounds selected
from class A, class B, class C and class D compounds.
8. Multilayer structure according to claim 1, wherein one, several or all
layers, excluding Nylon layers, are cross-linked.
9. Multilayer film wherein Nylon or N-MXD6, or their blend are used as
separate layer in contact with the EVOH layer.
10. Multilayer polymeric structure, substantially as described and
illustrated.
11. Process for making a polymeric structure substantially as described
and illustrated.
PCT/IL2001/000856 2000-12-25 2001-09-10 Multilayer barrier shrink films and process for their manufacture WO2002051630A2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU2001288035A AU2001288035A1 (en) 2000-12-25 2001-09-10 Multilayer barrier shrink films and process for their manufacture

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IL140543 2000-12-25
IL14054300A IL140543A0 (en) 2000-12-25 2000-12-25 Multilayer barrier shrink films and process for their manufacture

Publications (2)

Publication Number Publication Date
WO2002051630A2 true WO2002051630A2 (en) 2002-07-04
WO2002051630A3 WO2002051630A3 (en) 2002-10-10

Family

ID=11074966

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/IL2001/000856 WO2002051630A2 (en) 2000-12-25 2001-09-10 Multilayer barrier shrink films and process for their manufacture

Country Status (3)

Country Link
AU (1) AU2001288035A1 (en)
IL (1) IL140543A0 (en)
WO (1) WO2002051630A2 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004080804A2 (en) 2003-03-07 2004-09-23 Pechiney Emballage Flexible Europe Multilayer barrier structures, methods of making the same and packages made therefrom
EP1603800A2 (en) * 2003-03-07 2005-12-14 Pechiney Emballage Flexible Europe Multilayer structures, packages, and methods of making multilayer structures
WO2007092265A1 (en) * 2006-02-07 2007-08-16 Evergreen Packaging International B.V. Barrier laminate containing partially aromatic nylon materials, blank constructed from the barrier laminate, and container constructed from the barrier laminate
EP2248666A1 (en) * 2008-02-27 2010-11-10 Ishida Co., Ltd. Display strip and merchandise display
US8741433B2 (en) 2004-12-10 2014-06-03 Curwood, Inc. Packaging films comprising nylon blend compositions
EP3083426A4 (en) * 2013-12-20 2017-08-16 Bemis Company, Inc Liners for bulk containers
WO2018022607A1 (en) * 2016-07-26 2018-02-01 Sealed Air Corporation (Us) Flexible packaging composite for thermally processed, shelf stable, high acid foods
WO2018172510A1 (en) * 2017-03-24 2018-09-27 Borealis Ag Oriented multilayer barrier film

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0561428A1 (en) * 1986-02-28 1993-09-22 W.R. Grace & Co.-Conn. Oxygen barrier packaging film
US5491009A (en) * 1990-08-03 1996-02-13 W. R. Grace & Co.-Conn. Amorphous nylon composition and films
WO1997012758A1 (en) * 1995-10-06 1997-04-10 W.R. Grace & Co.-Conn. Backseamed casing and packaged product incorporating same
EP0801096A1 (en) * 1996-04-12 1997-10-15 W.R. Grace & Co.-Conn. Heat sealable film
DE19830977A1 (en) * 1998-07-10 2000-01-13 Wolff Walsrode Ag Multi-layer, symmetrical, non-curling, coextruded thermoforming film
EP0987103A1 (en) * 1998-09-14 2000-03-22 Cryovac, Inc. Heat-shrinkable multilayer thermoplastic film

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0561428A1 (en) * 1986-02-28 1993-09-22 W.R. Grace & Co.-Conn. Oxygen barrier packaging film
US5491009A (en) * 1990-08-03 1996-02-13 W. R. Grace & Co.-Conn. Amorphous nylon composition and films
WO1997012758A1 (en) * 1995-10-06 1997-04-10 W.R. Grace & Co.-Conn. Backseamed casing and packaged product incorporating same
EP0801096A1 (en) * 1996-04-12 1997-10-15 W.R. Grace & Co.-Conn. Heat sealable film
DE19830977A1 (en) * 1998-07-10 2000-01-13 Wolff Walsrode Ag Multi-layer, symmetrical, non-curling, coextruded thermoforming film
EP0987103A1 (en) * 1998-09-14 2000-03-22 Cryovac, Inc. Heat-shrinkable multilayer thermoplastic film

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2679517A1 (en) * 2003-03-07 2014-01-01 Bemis Company, Inc Multilayer barrier structures, methods of making the same and packages made therefrom
US9498937B2 (en) 2003-03-07 2016-11-22 Coveris Flexibles Us Llc Multilayer structures, packages, and methods of making multilayer structures
EP1603800A2 (en) * 2003-03-07 2005-12-14 Pechiney Emballage Flexible Europe Multilayer structures, packages, and methods of making multilayer structures
EP2679518A1 (en) * 2003-03-07 2014-01-01 Bemis Company, Inc. Multilayer structures, packages, and methods of making multilayer structures
EP1603800A4 (en) * 2003-03-07 2008-03-26 Pechiney Emballage Flexible Eu Multilayer structures, packages, and methods of making multilayer structures
EP1603812A4 (en) * 2003-03-07 2008-03-26 Pechiney Emballage Flexible Eu Multilayer barrier structures, methods of making the same and packages made therefrom
EP2679518B1 (en) 2003-03-07 2017-07-19 Bemis Company, Inc. Multilayer structures, packages, and methods of making multilayer structures
WO2004080804A2 (en) 2003-03-07 2004-09-23 Pechiney Emballage Flexible Europe Multilayer barrier structures, methods of making the same and packages made therefrom
EP1603812A2 (en) * 2003-03-07 2005-12-14 Pechiney Emballage Flexible Europe Multilayer barrier structures, methods of making the same and packages made therefrom
US9498936B2 (en) 2003-03-07 2016-11-22 Coveris Flexibles Us Llc Multilayer barrier structures, methods of making the same and packages made therefrom
US8741433B2 (en) 2004-12-10 2014-06-03 Curwood, Inc. Packaging films comprising nylon blend compositions
WO2007092265A1 (en) * 2006-02-07 2007-08-16 Evergreen Packaging International B.V. Barrier laminate containing partially aromatic nylon materials, blank constructed from the barrier laminate, and container constructed from the barrier laminate
EP2248666A4 (en) * 2008-02-27 2012-04-18 Ishida Seisakusho Display strip and merchandise display
EP2248666A1 (en) * 2008-02-27 2010-11-10 Ishida Co., Ltd. Display strip and merchandise display
US8545955B2 (en) 2008-02-27 2013-10-01 Ishida Co., Ltd. Display strip and product assembly
EP3083426A4 (en) * 2013-12-20 2017-08-16 Bemis Company, Inc Liners for bulk containers
WO2018022607A1 (en) * 2016-07-26 2018-02-01 Sealed Air Corporation (Us) Flexible packaging composite for thermally processed, shelf stable, high acid foods
CN109952195A (en) * 2016-07-26 2019-06-28 克里奥瓦克公司 Flexible packaging composites for thermally processed shelf-stable high acid foods
WO2018172510A1 (en) * 2017-03-24 2018-09-27 Borealis Ag Oriented multilayer barrier film
CN110636938A (en) * 2017-03-24 2019-12-31 博里利斯股份公司 Oriented multilayer barrier film

Also Published As

Publication number Publication date
IL140543A0 (en) 2002-02-10
WO2002051630A3 (en) 2002-10-10
AU2001288035A1 (en) 2002-07-08

Similar Documents

Publication Publication Date Title
CA1309821C (en) Multilayer film containing amorphous nylon
FI100511B (en) Multilayered packaging film
EP1651438B1 (en) Multilayer oriented high-modulus film
JP5685553B2 (en) Multi-layered, heat-shrinkable film comprising a number of microlayers and method for making the same
US6218024B1 (en) Multilayer plastic film
CA1077667A (en) Heat shrinkable multi-layer film and method of producing same
EP0457598B1 (en) Use of a breathable abuse resistant film for packaging cheese
US6565985B2 (en) Heat-shrinkable multilayer film
US7744806B2 (en) Process for making shrink film comprising rapidly-quenched semi-crystalline polyamide
JP2654054B2 (en) Thermoplastic multilayer barrier packaging film and bags made therefrom
US5077109A (en) Oriented multilayer film and process for making same
WO2016053956A1 (en) Multilayer food casing or food film
PL207071B1 (en) Multilayer packaging structures
NZ203319A (en) Multi-layer polyolefine films
JPH0834100A (en) Oriented multilayer film
US20080182052A1 (en) Multilayer heat-shrinkable film of high transparency, low haze, and high semi-crystalline polyamide content
WO2017063087A1 (en) Multilayer plastic film with heat resistant outer layers and slow and normal crystallizing polyamides
US20080182051A1 (en) Heat shrinkable retortable packaging article and process for preparing retorted packaged product
WO2002051630A2 (en) Multilayer barrier shrink films and process for their manufacture
WO2002051632A1 (en) Multilayer barrier polymeric films
GB2135239A (en) Improved linear laminated polyethylene shrink films
JPH04232048A (en) Ethylene propyrene terpolymer film
JPH071680A (en) Plasticization of ethylene-vinyl alcohol copolymer by acrylic ester ternary copolymer, and plasticized product obtained by said plasticization
AU1983899A (en) Heat-shrinkable multilayered film
GB2135240A (en) Linear polyethylene shrink films

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A2

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ PH PL PT RO RU SD SE SG SI SK SL TJ TM TR TT TZ UA UG US UZ VN YU ZA ZW

AL Designated countries for regional patents

Kind code of ref document: A2

Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG

AK Designated states

Kind code of ref document: A3

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ PH PL PT RO RU SD SE SG SI SK SL TJ TM TR TT TZ UA UG US UZ VN YU ZA ZW

AL Designated countries for regional patents

Kind code of ref document: A3

Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG

121 Ep: the epo has been informed by wipo that ep was designated in this application
REG Reference to national code

Ref country code: DE

Ref legal event code: 8642

122 Ep: pct application non-entry in european phase
NENP Non-entry into the national phase

Ref country code: JP