U.S. patent application number 09/271226 was filed with the patent office on 2001-12-27 for multi-layer film with core layer of syndiotactic polypropylene.
Invention is credited to HEFFELFINGER, MICHAEL T., KEUNG, JAY K., PEET, ROBERT G..
Application Number | 20010055692 09/271226 |
Document ID | / |
Family ID | 23034721 |
Filed Date | 2001-12-27 |
United States Patent
Application |
20010055692 |
Kind Code |
A1 |
HEFFELFINGER, MICHAEL T. ;
et al. |
December 27, 2001 |
MULTI-LAYER FILM WITH CORE LAYER OF SYNDIOTACTIC POLYPROPYLENE
Abstract
The present invention is directed to a biaxially oriented
multi-layer film which comprises: (a) a core layer comprising a
syndiotactic propylene homopolymer; and (b) at least one additional
layer adjacent to the core layer comprising a polymer which is an
ethylene or a propylene homopolymer, ethylene copolymer or
terpolymer containing comonomers of propylene and/or butene-1.
Optionally, there can be a skin layer applied to the exposed
surface of the outer layer. The skin layer and/or the at least one
additional layer is a polyolefin selected from the group consisting
of isotactic polypropylene, polyethylene, ethylene-propylene random
copolymer, ethylene-propylene block copolymer or
ethylene-propylene-butene-1 terpolymer.
Inventors: |
HEFFELFINGER, MICHAEL T.;
(ALPHARETTA, GA) ; KEUNG, JAY K.; (VICTOR, NY)
; PEET, ROBERT G.; (PITTSFORD, NY) |
Correspondence
Address: |
EXXONMOBIL CHEMICAL COMPANY
P O BOX 2149
BAYTOWN
TX
775222149
|
Family ID: |
23034721 |
Appl. No.: |
09/271226 |
Filed: |
March 17, 1999 |
Current U.S.
Class: |
428/516 ;
264/173.12; 264/173.13; 264/211.12; 428/518 |
Current CPC
Class: |
B32B 2323/10 20130101;
Y10T 428/31743 20150401; Y10T 428/31928 20150401; B32B 27/08
20130101; B32B 27/32 20130101; Y10S 428/91 20130101; B32B 2307/518
20130101; Y10T 428/31913 20150401; Y10T 428/31757 20150401; Y10T
428/31909 20150401; Y10T 428/31797 20150401; Y10T 428/31746
20150401; B32B 37/153 20130101; Y10T 428/3175 20150401; Y10T
428/31938 20150401; Y10T 428/31935 20150401; Y10T 428/1352
20150115; Y10T 428/31739 20150401; B32B 2038/0068 20130101; Y10T
428/3192 20150401; Y10T 428/31855 20150401 |
Class at
Publication: |
428/516 ;
428/518; 264/173.12; 264/173.13; 264/211.12 |
International
Class: |
B32B 027/08; B29C
047/06; B32B 027/32; B32B 027/30 |
Claims
What is claimed is
1. A biaxially oriented multi-layer film which comprises: (a) a
core layer comprising a syndiotactic propylene polymer; and (b) at
least one additional layer adjacent to the core layer comprising an
ethylene or propylene homopolymer, an ethylene copolymer, a
terpolymer containing propylene, ethylene, and butene-1 as
comonomers, or a blend thereof.
2. The biaxially oriented multi-layer film of claim 1 which further
comprises a coating and/or a skin layer adjacent the at least one
additional layer, the skin layer comprising a polyolefin.
3. The biaxially oriented multi-layer film of claim 1 in which the
skin layer is a polyolefin selected from the group consisting of
isotactic polypropylene, ethylene-propylene random copolymer,
ethylene-propylene block copolymer or ethylene-propylene-butene-1
terpolymer.
4. The biaxially oriented multi-layer film of claim 2 in which the
coating is selected from the group consisting of a polyvinylidene
chloride coating, a polyvinyl alcohol coating and an acrylic
polymer coating.
5. The biaxially oriented multi-layer film of claim 1 in which the
at least one additional layer further comprises silica
particles.
6. The biaxially oriented multi-layer film of claim 1 further
comprising an alicyclic hydrocarbon.
7. A process for preparing an oriented multi-layer film which
comprises the steps of: (a) melt coextruding a film comprising: (i)
a core layer comprising syndiotactic polypropylene, and (ii) at
least one additional layer adjacent the core layer comprising an
ethylene or propylene homopolymer, an ethylene copolymer, a
terpolymer containing propylene, ethylene and butene-1 as
comonomers, or a blend thereof; and (b) orienting the coextruded
combination in at least one direction.
Description
FIELD OF THE INVENTION
[0001] The present invention relates to a multi-layer thermoplastic
film having a core layer of syndiotactic polypropylene.
BACKGROUND OF THE INVENTION
[0002] Oriented polypropylene films are known for use in packaging
operations. U.S. Pat. No. 4,604,324 to Nahmias, et al. discloses a
multi-layer polypropylene film structure comprising coextruded
layers of a base layer of high stereoregularity polypropylene and a
skin layer of comparatively low stereoregularity which contains
anti-stick additives. In addition, the skin layer can contain up to
10 wt. % of a wax to improve heat seal characteristics or optical
properties of the film. U.S. Pat. No. 5,254,394 to Bothe, et al.,
discloses a polyolefin film for packaging comprising isotactic
polypropylene base layer and a top layer of syndiotactic
polypropylene which has high sealed-seam strength and excellent
optical properties. The layers may contain lubricant additives such
as waxes at levels of up to 2 wt %, relative to each layer.
SUMMARY OF THE INVENTION
[0003] The present invention relates to an oriented multi-layer
film which comprises:
[0004] (a) a core layer comprising syndiotactic propylene polymer;
and
[0005] (b) at least one additional layer adjacent to the core layer
comprising an ethylene or propylene homopolymer, an ethylene
copolymer, a terpolymer containing propylene, ethylene, and
butene-1 as comonomers, or a blend thereof.
[0006] The polymer of the at least one additional layer can be made
by any conventional method such as Ziegler-Natta catalysis or
metallocene catalysis. When the at least one additional layer
comprises a blend of polymers, such blend can comprise, e.g.,
ethylene and/or propylene homopolymers and/or one or more
copolymers or terpolymers of propylene with ethylene and/or
butene-1.
[0007] The present invention is further directed to a process for
preparing an oriented multi-layer film which comprises the steps
of
[0008] (a) melt coextruding a film comprising: (i) a core layer
comprising syndiotactic polypropylene, and (ii) at least one
additional layer adjacent the core layer comprising an ethylene or
propylene homopolymer, an ethylene copolymer, a terpolymer
containing propylene, ethylene and butene-1 as comonomers, or a
blend thereof; and
[0009] (c) orienting the coextruded combination.
[0010] In several possible applications, it would be desirable to
create films that have properties of the type that would be
achieved by making those films from syndiotactic polypropylene.
Some of these characteristics, such as the very slow development of
its crystalline structure, make it impossible to make a monolayer
film of syndiotactic polypropylene, however. What we have found is
that the syndiotactic monolayer web extruded from a die onto a
casting drum sticks very tightly to the casting drum. Because the
crystalline development is very slow, the web distorts unacceptably
under the low forces that are used in the accepted methods for
pulling the web free from the drum.
[0011] We have determined that we can solve this problem and
produce a film that can have about as much of the desired
properties of a syndiotactic polypropylene film as we choose. This
is accomplished by coextruding a layer of isotactic polypropylene,
made either by the standard Ziegler-Natta catalyst system or by
metallocene catalysts, on at least the side of the cast web that
would otherwise contact the casting drum. The degree that the
resulting film approximates a monolayer syndiotactic polypropylene
film depends, to a large extent, on what fraction of the total
structure is made up of syndiotactic polypropylene and what
fraction is isotactic polypropylene, i.e., how thin or how thick a
skin layer of isotactic polypropylene one chooses to use.
[0012] We have also determined that we can extend this concept so
that a film with a core layer of syndiotactic polypropylene can be
produced along with intermediate layers of isotactic polypropylene
and outer layers of other polymeric materials providing additional
characteristics, such as sealability.
DETAILED DESCRIPTION OF THE INVENTION
[0013] The core layer is made from syndiotactic polypropylene. The
syndiotactic polypropylene generally possesses a syndiotacticity of
at least 70% based on racemic pentads, typically greater than 75%,
as measured by C.sup.13 NMR spectroscopy. The mean length of
sequence n.sub.r of the syndiotactic sequences is preferably
greater than about 20, more preferably greater than about 25.
[0014] Commercially available syndiotactic propylene polymers
suitable for use in the present invention include EOD 95-01 and
95-02, available from Fina Oil and Chemical Company. These
materials have melt flows of about 4 and 7 g/10 min, respectively,
as measured in accordance with the standard ASTM D1238 method.
[0015] The syndiotactic propylene polymer can, optionally, contain
other monomeric units as in the case of a copolymer of propylene
with ethylene or .alpha.-olefin having from 4 to 20 carbon atoms
such as butene-1, pentene-1, hexene-1, heptene-1 or
4-methylpentene-1. Typically, the amount of monomer other than
propylene is no more than 10% by weight of the entire polymer.
[0016] Propylene polymers having a syndiotactic structure are
described in U.S. Pat. Nos. 5,254,394; 5,254,384; 5,162,278;
5,155,080; 4,892,851 and European Pat. No. 0499216, all of which
are incorporated herein by reference.
[0017] The propylene polymer is usually predominantly comprised of
propylene (at least 90% by weight) and has a melting point of about
140.degree. C. or higher, more typically a melting point of
150.degree. C. or higher. The melt flow rate usually ranges from
about 0.5 g/10 min to about 15 g/10 min at 230.degree. C., more
typically about 1.5 g/10 min to about 4 g/10 min at 230.degree. C.
The melt flow rate is measured according to the standard procedure
set forth in ASTM D1238.
[0018] The at least one additional layer of the present invention
may be any one of the coextrudable, biaxially orientable
film-forming resins known in the art. Such materials include, but
are not limited to, isotactic polypropylene, other syndiotactic
polypropylenes, ethylene copolymers and terpolymers which include
other monomers such as propylene and/or butene-1. Typical
copolymers are ethylene-propylene copolymers, ethylene-butene-1
copolymers, butene-1 -propylene random copolymers, and
ethylene-propylene block copolymers. Typical terpolymers are
ethylene-propylene-butene-1 terpolymers. Alternative and useful
thermoplastic materials for the at least one additional layer
include, but are not limited to nylon, polyester, ethylene-vinyl
acetate copolymer, and ethylene-vinyl alcohol copolymer. Blends of
any of the foregoing homopolymers, copolymers and terpolymers are
contemplated.
[0019] Ethylene-propylene-butene-1 random terpolymers appropriate
for use in the at least one additional layer of the present
invention include those containing 1-5 weight percent random
ethylene and 10-25 weight percent random butene-1, with the balance
being made up of propylene. The amounts of the random ethylene and
butene-1 components in these terpolymers are typically in the range
of 10 to 25 weight percent (ethylene plus butene-1) based on the
total amount of the copolymer.
[0020] The copolymers and terpolymers typically have a melt flow
rate in the range of about 5 to 10 g/10 min, with a density of
about 0.9 and a melting point in the range of about 115 to about
130.degree. C.
[0021] The polymers of the outermost layers of the film can also be
fabricated from any polymers, copolymers or terpolymers or blends
of homopolymers and blends of copolymer(s) and homopolymer(s) which
have heat seal properties. Several of the materials identified
above are illustrative of heat sealable copolymers which can be
used in the present invention.
[0022] In one aspect of the invention the at least one additional
layer is derived from polyethylene. The polyethylene can be low
density polyethylene (LDPE), linear low density polyethylene
(LLDPE), medium density polyethylene (MDPE) or high density
polyethylene (HDPE). These ethylene polymers typically have a melt
index ranging from about 0.3 to about 15 g/10 min, as measured in
accordance with the standards of ASTM D1238. The low density
polyethylenes should have a density of about 0.88 to about 0.93
g/cm.sup.3. Linear materials may have a density as high as 0.94
g/cm.sup.3, often ranging from 0.90 to 0.94 g/cm.sup.3, with a melt
index of about 1 to about 10. The linear low density polyethylenes
may be derived from ethylene together with other higher comonomers
such as butene-1, hexene-1, or octene-1. Typically it is useful to
use HDPE as the at least one additional layer as it enhances film
toughness. HDPE has a density of greater than about 0.941
g/cm.sup.3, typically from about 0.941 to about 0.965 g/cm.sup.3.
High density polyethylene suitable for use as the at least one
additional layer is described in Bakker, Ed. "The Wiley
Encyclopedia of Packaging Technology, pp. 514 to 523 (1986).
[0023] Each of the at least one additional layer can range in
thickness from about 0.01 mil to about 0.20 mil, specifically from
about 0.02 mil to about 0.06 mil.
[0024] There can be more than one layer coextruded on each side of
the core. That is, one or more layers, selected from the materials
defined for the at least one additional layer, can be added to one
or both surfaces of the core layer. Films having such a multi-layer
structure are represented, in simplified form, as having a
structure "ABCDE" where "C" represents a core layer, "B" represents
an outer layer adjacent to the core layer and "A" represents a
further outer layer or skin layer applied to the outer surface of
outer layer "B." In such a film structure, the outer layer "B" can
be referred to as a "tie-layer" or an "intermediate layer." Layers
"A" and "B" may be the same or different. Similarly, "D" and "E"
represent additional layers on the other side of the core layer.
Layers "B" and "D" may be the same or different, and layers "D" and
"E" may be the same or different. A layer may also be absent.
Additionally, structures containing more than five layers are
contemplated, e.g., six, seven, eight, nine, and more layers are
contemplated.
[0025] In order to modify or enhance certain properties of the
multi-layer films of the invention for specific end-uses, it is
possible for one or more of the layers to contain appropriate
additives in effective amounts. Preferred additives include
antistatic agents, antiblocking agents, lubricants, stabilizers
and/or one or more of a class of hydrocarbons resins, such as
alicyclic hydrocarbon resins which are known to improve barrier
properties. Such additives are further described in U.S. Pat. No.
5,254,394, which is incorporated herein by reference. It is useful
to incorporate additives such as wax, finely divided inorganic
antiblock particles, silicone oil, and silicone spheres such as
non-migratory particulate crosslinked hydrocarbyl substituted
polysiloxane slip agent, such as TOSPEARL which is marketed
world-wide by Toshiba Silicone Co., Ltd. and in the United States
by General Electric. The alicyclic hydrocarbons include
polyterpenes, petroleum resins, and "hard" resins employed in the
films to improve barrier properties and sealability. Examples of
these materials would include PICCOLYTE and REGALREZ from Hercules,
ZONTEC from Arizona Chemical Company, ARKON from Arakawa Chemical
Co., and ESCOREZ from Exxon. Other additives that can be
incorporated into one or more layers of the film include
nucleators, such as MILLAD 3938 from Milliken for modifying the
crystalline structure, and carbon black for brightening.
[0026] Finely divided inorganic antiblock materials, comprehended
above, include, Syloid, a synthetic amorphous silica gel, having a
composition of 99.7% SiO.sub.2; diatomaceous earth having a
composition of, for example, SiO.sub.2 92%, Al.sub.2O.sub.3 3.3%,
Fe.sub.2O.sub.3 1.2%, which can be obtained in various grades with
average particle sizes ranging from about 0.5 microns to about 7-10
microns, which particles are porous and irregularly shaped;
dehydrated kaolin clays, such as Kaopolite SF which has the
composition SiO.sub.2 55%, Al.sub.2O.sub.3 44%, Fe.sub.2O.sub.3
0.4% which has an average particle size of about 0.7 microns, and
whose particles are thin flat platelets; and synthetic precipitated
silicates, Sipernat 44, for example, having a composition of
SiO.sub.2 42%, Al.sub.2O.sub.3 36%, Na.sub.2O 22%, which has an
average particle size of about 3-4 microns, which particles are
porous and irregularly shaped. The amount of antiblock typically
ranges from about 0.002 to about 0.5 weight % based upon the weight
of the polymer.
[0027] Typically, a commercially available intensive mixer, such as
those of the Boling- or Banbury-type can be employed in mixing a
concentrate of the finely divided inorganic material and the
selected polymer until there is a uniform dispersion of the
inorganic material in the polymer.
[0028] The alicyclic hydrocarbon is advantageously used to improve
the barrier properties of the film. It has also been found that the
alicyclic hydrocarbon contributes to film stiffness: the stiffness
of the film increases as the amount of alicyclic hydrocarbon
increases. The amount of alicyclic hydrocarbon employed in a layer
of the film typically ranges from about 3 to about 15 wt. % based
upon the weight of the layer.
[0029] One or more of the exposed layers of the multi-layer films
of the present invention can be surface-treated to render the films
receptive to printing inks, adhesives and/or coatings. The surface
treatment can be carried out by any method known in the art such as
corona discharge treatment or flame treatment.
[0030] Optionally a coating may be applied to one or both of the
exposed surface(s) of the outermost layer(s) of the film. Prior to
application of the coating material, the film may be surface
treated or may be primed with a primer layer. Appropriate coatings
contemplated include acrylic coatings such as those described in
U.S. Pat. Nos. 3,753,769 and 4,865,908, PVDC coatings such as those
described in U.S. Pat. No. 4,214,039; 4,447,494; 4,961,992;
5,019,447 and 5,057,177, all of which are incorporated herein by
reference. A vinyl alcohol polymer, such as VINOL 325, may also be
used as a coating composition.
[0031] Appropriate primer materials are poly(ethyleneimine), epoxy
primer, and the like.
[0032] The outer surface of the film is preferably treated to
increase its surface energy and therefor insure that the coating
layer will be strongly adherent thereto, thereby reducing the
possibility of the coating peeling or being stripped from the film.
In addition to corona discharge and flame treatment, this treatment
can be accomplished employing other known techniques, such as, for
example, film chlorination, i.e., exposure of the film surface to
aqueous chlorine, treatment with oxidizing agents such as chromic
acid, hot air, or steam treatment, and the like. Although any of
these techniques are effectively employed to pretreat the film
surface, a particularly desirable method of treatment is the
so-called electronic treatment method which comprises exposing the
film surface to a high voltage corona discharge while passing the
film between a pair of spaced electrodes. After electronic
treatment of the film surface, the coating composition is then
applied thereto.
[0033] The exposed, treated or untreated surface(s), e.g., the
surface(s) of layer(s) A and/or E, may have applied to it/them
coating compositions, as mentioned above, and/or substrates such as
another polymer film or laminate; a metal foil such as aluminum
foil; cellulosic webs, e.g. numerous varieties of paper such as
corrugated paperboard, craft paper, glassines, cartonboard;
nonwoven tissue, e.g., spunbonded polyolefin fiber, melt-blown
microfibers, etc. The application may employ a suitable adhesive,
e.g., a hot melt adhesive such as low density polyethylene,
ethylene-methacrylate copolymer, water-based adhesive such as
polyvinylidene chloride latex, and the like.
[0034] The extruded film can be stretched in the machine direction,
coated with the coating composition and then stretched
perpendicularly in the transverse direction. In yet another
embodiment, the coating can be carried out after biaxial
orientation is completed.
[0035] The coating composition should be applied in such amount
that there will be deposited upon drying a smooth, evenly
distributed layer, generally on the order of from about 0.01 to
about 0.2 mil thickness (equivalent to about 0.2 to 3.5 g per 1000
sq. in. of film). In general, the thickness of the applied coating
is such that it is sufficient to impart the desired seal
sealability and/or oxygen and/or water vapor barrier
characteristics to the resulting film. Generally, the coating
comprises 1 to 25 wt %, preferably 7 to 15 wt % of the entire
coated film composition. The coating on the film is subsequently
dried by hot air, radiant heat or by any other convenient
means.
[0036] There are many advantages to the film of the invention.
However, most notable is the advantageous barrier properties which
permit the film to be adapted to controlled atmosphere packaging.
Additionally, the film has remarkable toughness and resistance to
deformation but it also can be made with a soft, "drapy" feel which
would be useful as a protective cover for clothing such as
dry-cleaning bags.
[0037] Usually the film of the invention has a total thickness
ranging from about 0.4 mil to about 2.5 mils, specifically from
about 0.5 mil to about 2.0 mils. The thickness relationship of the
layers can be important. In particular, the core layer is a
relatively thick layer which constitutes about 40 to about 95 % of
the total film thickness, an intermediate or tie layer may be of a
thickness ranging from about 0 to about 50% of the total film
thickness, while an outer skin layer may range from about 1 to
about 15% of the total film thickness.
[0038] It is preferred that all layers of the multi-layer film
structures of the present invention be coextruded. Thereafter, the
film may be biaxially oriented.
[0039] The polymers are brought to the molten state and coextruded
from a conventional extruder through a flat sheet die, the melt
streams are combined in an adapter prior to being extruded from the
die or within the die. After leaving the die, the multi-layer film
is chilled and the quenched sheet is reheated and oriented.
[0040] The film is oriented by biaxially stretching the film. The
film can be oriented by stretching from about 3.5 to about 6.5
times in the machine direction (MD) at temperatures ranging from
about 110.degree. C. to about 150.degree. C., and from about 5 to
about 14 times in the transverse direction (TD) at temperatures
ranging from about 152.degree. C. to about 165.degree. C.
[0041] In each of the examples, the film was oriented about 4.5-6
times in the MD at a temperature of about 125-135.degree. C. and
about 8-9 times in the TD at a temperature of about 155-160.degree.
C. Multi-layer films were prepared employing commercially available
systems for coextrusion.
[0042] The properties of the films were determined according to the
following methods:
1 A. Tensile Properties: 1. Modulus (psi) ASTM D882 2. Elongation
at Break (%) ASTM D882 3. Tensile Strength (psi) ASTM D882 B.
Dimensional Stability (% change): ASTM D1204 C. Optics: 1. Haze (%
light transmitted) ASTM D1003 2. Gloss (% light reflected at ASTM
D2457 about a 45.degree. angle) D. WVTR (G/100 in.sup.2/day): ASTM
F1249 E. TO.sub.2 (g/100 in.sup.2/day): ASTM D3985 F. Tear Strength
(g/mil): ASTM D1922 G. Coefficient of Friction (COF): ASTM D1894 H.
Puncture Resistance (g/mil): Standard Mobil PR Test
EXAMPLE 1
[0043] In Example 1, a five layer film was made having a core layer
of syndiotactic polypropylene having a melt flow rate of about 7,
tie layers of conventional isotactic polypropylene (Fina 3371) and
a skin layer of ethylene-propylene-butene-1 terpolymer was applied
to each outer surface of the tie layer. The core layer was 50% of
the total film structure, the tie layers were 40% of the total film
structure and the skin layers were 10% of the total film structure.
The unoriented film measured 50-56 mils. The biaxially oriented
film, oriented by conventional sequential biaxially orienting
apparatus, measured about 1 mil in thickness.
[0044] The syndiotactic polypropylene was melted in an extruder to
provide the core layer. A second and a third extruder, in
association with the first extruder, were supplied with the
isotactic polypropylene; these extruders provided the tie-layers. A
fourth extruder, in association with the first three extruders, was
supplied with ethylene-propylene-butene-1 terpolymer. A melt
coextrusion was carried out maintaining the extruder at a
temperature sufficient to maintain all polymers in the molten state
(about 240.degree. C. to about 270.degree. C.). The polymer
extruded as the tie layers was maintained at about the same
temperature as the polymer used in making the core layer, as was
the terpolymer of the skin layers. The terpolymer of the fourth
extruder was split into two streams to enable formation of skin
layers on each surface of the tie layer.
EXAMPLE 2
[0045] In Example 2, a five layer film was made, following the
procedure of Example 1, having a core layer of syndiotactic
polypropylene, melt flow rate of about 7, tie layers of
conventional isotactic polypropylene (Fina 3371) and skin layers of
metallocene catalyzed polyethylene (Exxon product designated as
Exxon 3016) located on each exposed surface of the tie layers. The
core layer was 50% of the total film thickness, the tie layers were
40% of the total film thickness and the skin layers were 10% of the
total film thickness. The entire film was 1 mil.
[0046] The properties of the films of Examples 1 and 2 are reported
in Table 1.
2 TABLE 1 Tensile Properties Water Ultimate Dimensional Coefficient
of Vapor Tear Modulus Elongation Tensile Stability Friction Optics
Trans. Strength Puncture EX. MD TD MD TD MD TD MD TD I/I O/O I/O
Haze Gloss Rate MD TD Resistance 1 178 327 147 49 8.9 18.9 -6.9
-7.7 0.81 0.83 0.85 2.3 86.7 0.52 14.4 1.9 1531 2 150 283 172 47
9.2 16.7 -7.4 -7.9 0.37 0.58 0.45 3.1 90.7 0.52 12.8 4.2 1301 Note:
"I/I," "O/O," and "I/O" designate "inside to inside," "outside to
outside," and "inside to outside" of the films, respectively.
EXAMPLE 3
[0047] In Example 3, five layer films were made by the process
described in Example 1 having a core layer of syndiotactic
polypropylene, melt flow rate of about 3. To the core layer was
added 0, 3, 9, and 15 wt. %, based upon the weight of the core
layer, of an alicyclic hydrocarbon, ARKON P115 from Arakawa
Chemical Co. Tie layers of conventional isotactic polypropylene
(Fina 3371) were coextruded on each side of the core layer and a
skin layer of ethylene-propylene-butene-1 terpolymer was applied to
each exposed surface of the tie layers. The core layer was 38% of
the total film thickness, the tie layers were 52% of the total film
thickness and the skin layers were 10% of the total film thickness.
The entire film was about 1 mil in thickness. The properties of the
films of this example are reported in Table 2.
3 TABLE 2 Tensile Properties Ultimate Dimensional Coefficient Tear
% Modulus Elongation Tensile Stability of Friction Optics Barrier
Strength Puncture P115 MD TD MD TD MD TD MD TD I/I I/O Haze Gloss
WVTR TO.sub.2 MD TD Resistance 0 170 331 159 39 9.0 19.8 -5.0 -6.5
0.79 0.82 2.3 85.6 0.56 135.8 14.5 2.8 1550 3 186 356 152 46 9.3
20.9 -3.5 -6.4 0.76 0.85 2.7 85.3 0.52 132.9 14.2 2.4 1694 9 222
405 182 50 12.2 22.1 -5.0 -6.0 0.72 0.79 2.8 84.7 0.45 113.8 6.7
1.2 1920 15 244 441 172 43 12.3 22.4 -5.7 -8.4 0.80 0.90 2.9 86.5
0.40 105.7 5.6 1.9 2053
EXAMPLE 4
[0048] In Example 4, a five layer film was made following the
procedure of Example 1 having a core layer of syndiotactic
polypropylene, melt flow rate of about 3, tie layers of
conventional isotactic polypropylene (Fina 3371) and a skin layer
on each side of the tie layer, which skin layers were metallocene
catalyzed polyethylene commercially available from Exxon under the
product designation 3016. This metallocene catalyzed polyethylene
had a density of 0.910 and a melt index of 4.5. The skin layers
each contained 2300 ppm silica antiblock (0.23 wt. % based on the
weight the skin layer). The silica antiblock additive was a
commercial material sold under the product designation SYLOBLOC 42
by W. R. Grace & Co. The core layer was 50% of the total film
structure and the tie layers were 40% of the total film structure
while the skin layers were 10% of the total film structure. The
entire film was 1 mil thick.
EXAMPLE 5
[0049] Example 5 is substantially the same as Example 4, except
that the skin layers were metallocene catalyzed polyethylene
commercially available from Exxon under the product designation
Exxon 3027. This metallocene catalyzed polyethylene had a density
of 0.908 and a melt index of 3.5.
EXAMPLE 6
[0050] Example 6 is substantially the same as Example 4, except
that the core layer propylene polymer had a melt flow of 7, and the
skin layers were metallocene catalyzed polyethylene commercially
available from Exxon under the product designation Exxon 3034. This
metallocene catalyzed polyethylene had a density of 0.902 and a
melt index of 3.5.
[0051] The properties of each film of Examples 4, 5 and 6 are
reported in Table 3.
4 TABLE 3 Tensile Properties Water Ultimate Dimensional Coefficient
of Vapor Tear Modulus Elongation Tensile Stability Friction Optics
Trans. Strength Puncture EX. MD TD MD TD MD TD MD TD I/I O/O I/O
Haze Gloss Rate MD TD Resistance TO.sub.2 4 143 227 146 42 8.9 11.6
-5.0 -13.9 0.49 0.47 0.47 2.5 85.8 0.59 13.5 5.6 1191 155 5 148 227
140 59 9.2 12.1 -4.7 -14.2 0.55 0.54 0.57 1.7 90.8 0.6 12.3 4.9
1314 145 6 167 273 131 39 9.5 13.6 -4.7 -13.2 0.55 0.55 0.55 1.5
92.2 0.58 11.3 4.2 1100 173
EXAMPLE 7
[0052] In Example 7, a three layer film was made having a core
layer of syndiotactic polypropylene, melt flow rate of about 3, and
outer layers made from conventional isotactic polypropylene (Fina
3371). The core layer was 50% of the total film structure while the
skin layers were 50% of the total film structure. The film of this
example was made by the process described in Example 1, except the
fourth extruder was omitted. The entire film was about 1 mil
thick.
[0053] The properties of this film are reported in Table 4.
5 TABLE 4 Tensile Properties Ultimate Dimensional Modulus
Elongation Tensile Stability Optics Puncture Ex. MD TD MD TD MD TD
MD TD Haze Gloss WVTR Resistance 7 187 321 139 48 10.8 16.9 -5.9
-15.9 0.9 91.5 0.53 1948
* * * * *