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.