CA2262081C - Opaque films comprising isotactic polypropylene - Google Patents
Opaque films comprising isotactic polypropylene Download PDFInfo
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- CA2262081C CA2262081C CA002262081A CA2262081A CA2262081C CA 2262081 C CA2262081 C CA 2262081C CA 002262081 A CA002262081 A CA 002262081A CA 2262081 A CA2262081 A CA 2262081A CA 2262081 C CA2262081 C CA 2262081C
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/06—Layered 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
- B32B27/08—Layered 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
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B5/00—Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts
- B32B5/18—Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts characterised by features of a layer of foamed material
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/18—Layered products comprising a layer of synthetic resin characterised by the use of special additives
- B32B27/20—Layered products comprising a layer of synthetic resin characterised by the use of special additives using fillers, pigments, thixotroping agents
- B32B27/205—Layered products comprising a layer of synthetic resin characterised by the use of special additives using fillers, pigments, thixotroping agents the fillers creating voids or cavities, e.g. by stretching
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/32—Layered products comprising a layer of synthetic resin comprising polyolefins
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B7/00—Layered products characterised by the relation between layers; Layered products characterised by the relative orientation of features between layers, or by the relative values of a measurable parameter between layers, i.e. products comprising layers having different physical, chemical or physicochemical properties; Layered products characterised by the interconnection of layers
- B32B7/04—Interconnection of layers
- B32B7/12—Interconnection of layers using interposed adhesives or interposed materials with bonding properties
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/10—Homopolymers or copolymers of propene
- C08L23/12—Polypropene
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2270/00—Resin or rubber layer containing a blend of at least two different polymers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/40—Properties of the layers or laminate having particular optical properties
- B32B2307/41—Opaque
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/70—Other properties
- B32B2307/726—Permeability to liquids, absorption
- B32B2307/7265—Non-permeable
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2323/00—Polyalkenes
- B32B2323/10—Polypropylene
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2439/00—Containers; Receptacles
- B32B2439/70—Food packaging
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
- C08J2323/10—Homopolymers or copolymers of propene
- C08J2323/12—Polypropene
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L77/00—Compositions of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Compositions of derivatives of such polymers
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- Polymers & Plastics (AREA)
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Abstract
An opaque polymeric film having enhanced moisture barrier and mechanical properties. The film has a base layer which includes a blend of a high crystallinity polypropylene having an isotactic stereoregularity greater than 93 % and a cavitating agent in an amount effective to cavitate the base layer.
Description
BACKGROUND OF THE INVENTION
The present invention relates to an opaque polypropylene-based multilayer film structure which exhibits enhanced moisture barrier and mechanical properties.
Opaque polymeric films are used in many commercial applications. One particularly important application is the packaging of products such as snack foods and candy bars. Films employed in the food packaging industry are chosen and/or designed to provide characteristics necessary for proper food containment. Such characteristics include water vapor barrier properties, oxygen and gas barrier properties and flavor and aroma barrier properties.
Polypropylene is a polymer commonly employed in the manufacture of opaque films used in the food packaging industry. In the case of multilayer films, polypropylene is typically used in the base or core layer and is cavitated with a cavitating agent such as polybutylene terephthalate (PBT). Typically, it has been necessary to use from 6% to 12% by weight of the cavitating agent in the prior art films to achieve the desired degree of cavitation.
However, the use of the PBT cavitating agent within the aforementioned ranges is not' without its drawbacks. Particularly, the loading ranges typically employed in the art may negatively impact production uptime. Moreover, the PBT itself, at the loading ranges typically employed in the art, represents a significant percentage of the raw material costs.
The mechanical properties of a polymeric film structure are another important 2 o characteristic, particularly with respect to such applications as food and candy wrappings.
Films having enhanced mechanical properties facilitate handling and packaging because such films are more readily accommodated by typical industrial machinery. Attempts have been made to enhance the mechanical properties of polypropylene-based films (as measured by the stiffness and moduli of the film) through increased orientation and/or by the addition of additives. However, increased orientation often increases the likelihood offilm splitting during manufacturing, while the addition of additives typically provides limited enhancement of mechanical properties but can negatively impact other film characteristics such as dimensional stability.
The present invention relates to an opaque polypropylene-based multilayer film structure which exhibits enhanced moisture barrier and mechanical properties.
Opaque polymeric films are used in many commercial applications. One particularly important application is the packaging of products such as snack foods and candy bars. Films employed in the food packaging industry are chosen and/or designed to provide characteristics necessary for proper food containment. Such characteristics include water vapor barrier properties, oxygen and gas barrier properties and flavor and aroma barrier properties.
Polypropylene is a polymer commonly employed in the manufacture of opaque films used in the food packaging industry. In the case of multilayer films, polypropylene is typically used in the base or core layer and is cavitated with a cavitating agent such as polybutylene terephthalate (PBT). Typically, it has been necessary to use from 6% to 12% by weight of the cavitating agent in the prior art films to achieve the desired degree of cavitation.
However, the use of the PBT cavitating agent within the aforementioned ranges is not' without its drawbacks. Particularly, the loading ranges typically employed in the art may negatively impact production uptime. Moreover, the PBT itself, at the loading ranges typically employed in the art, represents a significant percentage of the raw material costs.
The mechanical properties of a polymeric film structure are another important 2 o characteristic, particularly with respect to such applications as food and candy wrappings.
Films having enhanced mechanical properties facilitate handling and packaging because such films are more readily accommodated by typical industrial machinery. Attempts have been made to enhance the mechanical properties of polypropylene-based films (as measured by the stiffness and moduli of the film) through increased orientation and/or by the addition of additives. However, increased orientation often increases the likelihood offilm splitting during manufacturing, while the addition of additives typically provides limited enhancement of mechanical properties but can negatively impact other film characteristics such as dimensional stability.
Thus, there is a need in the art for an opaque polypropylene-based film which may be readily manufactured (i.e., improved production uptime and reduced raw material costs), and which exhibits enhanced moisture barrier and mechanical properties.
The present invention, which addresses the needs of the prior art, relates to an opaque polymeric film having enhanced moisture barrier and mechanical properties. The film has a base layer which includes a blend of a first polypropylene polymer having an isotactic stereoregularity greater than 93% and a cavitating agent in an amount effective to cavitate the base layer.
In one preferred embodiment, the base layer includes less than 6% by weight of 1 o cavitating agent, and preferably from 2% to S% of cavitating agent. In another preferred embodiment, the base layer further includes a resin modifier in an amount up to 9% by weight of said base layer. The resin modifier is preferably a hydrogenated hydrocarbon.
In still another preferred embodiment, at least one tie layer is adhered to the cavitated base layer. A skin is preferably adhered to the other side of the tie layer.
The tie layer, which facilitates adherence of the skin layer to the cavitated base layer, is preferably formed from polypropylene. The skin layer is preferably formed from an ethylene-propylene random copolymer or an ethylene-propylene-butene-1 terpolymer.
As a result, the present invention provides an opaque polypropylene-based film structure exhibiting enhanced moisture barrier and mechanical properties.
These improved 2 o properties are obtained without a negative impact on such film characteristics as dimensional stability. More to the point, these improved properties are obtained while using a significantly lower level of cavitating agent, thus providing improved production uptime and reduced raw material costs. The film structure further exhibits a high degree of machinability and processability.
2 5 The present invention is prepared by blending high crystallinity polypropylene (HCPP) with a cavitating agent in an amount effective to cavitate the HCPP. The HCPP
has an isotactic stereoregularity of greater than 93%, preferably from 94% to 98%.
The base layer preferably includes less than 6% by weight of the cavitating agent.
T _ ~_._.___ Commercially suitable PPs include Fina 3371 (available from Fina Oil and Chemical Co., Dallas, Texas), Exxon 4612 and Exxon X052 (available from Exxon Chemical Co., Houston, Texas) and Amoco*6361 (available from Amoco Chemical Co., Chicago, Illinois).
Commercially suitable HCPPs include Amoco 9117, Amoco 9119 and Amoco''~218(available from Amoco Chemical Co., Chicago, Illinois), and Chisso"i~5010 and Chisso~2805 (available from Chisso Chemical Co., Ltd., Tokyo, Japan). Suitable HCPPs are also available from Solvay in Europe.
The HCPP has a high isotactic stereoregularity, resulting in higher crystallinity than conventional isotactic polypropylene, i.e, greater than 93%. (Conventional isotactic polypropylene is defined herein as having an isotactic stereoregularity of from 90% to 93%.) The HCPP thus exhibits higher stiffness, surface hardness, lower deflection at higher temperatures and better creep properties than conventional isotactic polypropylene. Further information relating to HCFP, including methods for preparation thereof, is disclosed in U.S.
Patent No. 5,063,264.
For purposes of the present invention, stereoregularity can be determined by IR
spectroscopy according to the procedure set out in "Integrated Infrared Band Intensity Measurement of Stereoregularity in Polypropylene," L L. Koenig and A.VanRoggen, Journal of Applied Polymer Science, Vol. 9, pp. 359-367 (1965) and in "Chemical Microstructure of Polymer Chains," J. L. Koenig, Wiley-Inerscience Publication, John Wiley and Sons, New 2 o York, Chichester, Brisbane, Toronto. Stereoregularity can also be determined by decahydronaphthalene (decalin) solubility and nuclear magnetic resonance spectroscopy The use of HCPP in the base layer unexpectedly lowers the amount of cavitating agent required to cavitate the film and produce the desired opacity. More particularly, the use of 2 5 HCPP in the base layer lowers the amount of cavitating agent necessary to cavitate the film from the prior art levels of approximately 6% to 12% by weight, or greater, to a level in the present invention of less than 6% by weight, and preferably from 2% to 5% by weight. This reduction in loading level of the cavitating agent is significant in that it results in greater production uptime. In addition, the reduction in the amount of cavitating agent necessary to 3 o cavitate the base layer translates into a significant cost savings in raw materials.
* Trade-mark More to the point, the blend of HCPP and cavitating agent in the base layer provides a significant improvement in the moisture barrier of the resultant film. As demonstrated in the example set forth hereinbelow, improvements in moisture barrier of up to 20%
to 30% may be achieved with the film structures of the present invention. It will be recognized by those skilled in the art that this 20% to 30% improvement in moisture barrier is significant in the food packaging industry.
Preferred cavitating agents include polybutylene terephthalate (PBT), calcium carbonate (CaCO,),.polyester (FET), polyamides including nylon and other polymers and/or inorganic materials which are incompatible.with HCPP.
In one preferred embodiment, the HCPP in the base layer is blended with a conventional isotactic polypropylene (PP). The base layer preferably includes an amount of PP effective to plasticize the base layer and thus increase the processability of the resultant extruded film structure. The blended base layer increases manufacturing efFrciency by increasing line operability and line percentage uptime. For example, the blended base layer reduces the force necessary to stretch the film and in addition facilitates edge trimming of the extruded film. Thus, the blended base layer results in a reduction in cost associated with manufacture of the film structure.
In another preferred embodiment, a resin modifier is blended with the base layer precursor. The resin modifier is present in an amount of up to 9% by weight, and preferably 2 o from 3% to 6% by weight. The blending may be accomplished by the direct feeding of HCPP
and resin modifier into the film extruder or by use of a masterbatch. One preferred method of blending the components utilizes a masierbatch formed of HCPP and resin modifier, e.g., 80'%
HCPP and 20% resin modifier. The masterbatch is then blended with additional HCPP, which reduces the concentration of the resin modifier to the final desired level.
Applicant has discovered that polymeric film structures formed from HCPP exhibit unexpectedly large decreases in water vapor transntission with small additions of resin modifier. The moisture barrier increases as the loading level of resin modifier is increased until a point is reached (less than 10% resin 3 o modifier) at which further increases in the loading level of the resin modifier do not provide further substantial increases in moisture barrier. Moreover, the HCPP-based film structures also provide enhanced mechanical properties without suffering from losses in dimensional stability, as is common in prior art film structures which may require upwards of 20% resin modifier to achieve maximum moisture barrier.
The resin modifier is preferably a low molecular weight hydrogenated hydrocarbon which is compatible with the HCPP polymer and which provides the desired enhancement of film properties. The preferred resin modifier has a number average molecular weight less than 5000, preferably less than 2000, and more preferably from 500 to 1000. The resin modifier can be natural or synthetic and preferably has a softening point of from 60° to 180°C.
1o Particularly suitable hydrocarbons which can be subsequently hydrogenated are the hydrocarbon resins. Preferred hydrocarbon resins include among others petroleum resins, terpene resins, styrene resins and cyclopentadiene resins.
Examples of commercially available hydrogenated hydrocarbon resins suitable for use in the present invention are those sold under the trademarks PICCOLYTE, REGALREZ and REGALITE by Hercules Corporation of Delaware and under the trademark ESCOREZ
by Exxon Chemical Company of Houston, Texas. The ESCOREZ resins are particularly preferred hydrogenated hydrocarbon resins.
One particularly preferred resin modifier is referred to herein as a saturated alicyclic resin. The saturated alicyclic resins are obtained by the hydrogenation of aromatic 2 o hydrocarbon resins. The aromatic resins are themselves obtained by polymerizing reactive unsaturated hydrocarbons containing, as the principal component, aromatic hydrocarbons in which the reactive double bonds are generally in side-chains. More particularly, the alicyclic resins are obtained from the aromatic resins by hydrogenating the latter until all, or almost all, of the unsaturation has disappeared, including the double bonds in the aromatic rings.
The saturated alicyclic resins used in the present invention have a softening point from 85 ° to 140 ° C, and preferably from 100 ° to 140 ° C, as measured by the ball and ring method.
Examples of commercially available saturated alicyclic resins suitable for use in the present invention are those sold under the trademark ARKON-P by Arakawa Forest Chemical Industries, Ltd. of Japan.
In one preferred embodiment, a tie layer of an olefinic polymer is adhered to the base layer. Inasmuch as the skin layers discussed below may not adequately adhere to the cavitated base layer, a tie layer compatible with the cavitated base layer is first adhered to the base layer.
A skin layer of an olefinic polymer is, in turn, adhered to the tie layer.
Both the tie and skin layers are preferably coextruded with the base layer. The tie layers may include a whitening agent such as Ti02.
Suitable olefinic polymers utilized for the skin layers) include i) ethylene homopolymers, ii) copolymers of ethylene and propylene, iii) copolymers of ethylene or propylene and butylene or another alpha olefin having 5 to 10 carbon atoms, iv) terpolymers of ethylene, propylene and butylene or another alpha-olefin having 5 to 10 carbon atoms, and v) mixtures thereof.
Olefinic polymers which are particularly preferred for the skin layers) include ethylene-propylene copolymers with propylene as the main constituent and an ethylene content of 2% to I 0% by weight (relative to the weight of the copolymer), propylene-butylene copolymers with propylene as the main constituent and a butylene content of 0.5% to 25% by weight (relative to the weight of the copolymer), and ethylene-propylene-butene-1 terpolymers with propylene as the main constituent, 0.5% to 7% by weight of ethylene and 5% to 30% by weight of butene-1 (each time relative to the weight of the terpolymer), and mixtures of these polymers. The co- and terpolymers are preferably random polymers.
2 0 In a still further preferred embodiment, a coating is applied to the outer surface of the skin layer(s). An acrylic coating, which provides improved printability, machinability and aroma barrier characteristics, may be applied to one of the skin layers. A
heat seal coating such as ethylene methyl acrylate (EMA) or ethylene acrylic acid (EAA) may be applied to the other skin layer. Other suitable coatings include polyvinylidene chloride (PVDC), polyvinyl alcohol (PVOH) and low temperature heat seal coatings, as disclosed in commonly-owned U. S. Patent No. 5,419,960.
In order to further improve certain properties of the resultant film, effective amounts of additives such as antiblocking agents, antistatic agents and/or slip agents may be contained in the base layer, tie layers) and/or skin layer(s).
_ ___ ._ __. .____~____~_ ._._..._.___ _._____._. __.._~_. _._ _.___.__ _.
Preferred antiblocking agents include silica, talc, clay, sodium aluminum silicate, and conventional inorganic anti-blocks. Other suitable antiblocking agents include inorganic additives, such as silicon dioxide, calcium carbonate, magnesium silicate, aluminum silicate, calcium phosphate, and the like, and/or incompatible organic polymers, such as polyamides, polyesters, polycarbonates and the like.
Preferred antistatic agents include alkali alkane sulfonates and essentially straight-chain, saturated aliphatic tertiary amines possessing aliphatic radicals with 10 to 20 carbon atoms and being substituted by 2-hydroxyalkyl-(C, to C4) groups. Preferred amines are N,N-bis-(2-hydroxyethyl)-alkylamines having 10 to 20, preferably 12 to 18, carbon atoms in their 1o alkyl groups. The effective amount of antistatic agent varies in the range from 0.05% to 3%
by weight, relative to the weight of the layer.
Preferred slip agents include higher aliphatic acid amides, higher aliphatic acid esters, waxes, metallic soaps and silicone oils such as polydimethylsiloxane. The effective added amount of lubricant varies from 0.1% to 2% by weight.
The multilayer films of the present invention may be prepared employing commercially available systems for coextruding resins. As mentioned, the blended HCPP and cavitating agent precursor is preferably coextruded with at least one second and at least one third polymeric material, which form the tie and skin layers, respectively. The polymers can be brought to the molten state and coextruded from a conventional extruder through a flat sheet 2 o die, the melt streams being combined in an adapter prior to being extruded from the die. After leaving the die orifice, the multilayer film structure is quenched.
The film structure of the present invention is preferably biaxially oriented.
In orie preferred embodiment, the film structure is stretched from 4.5 to 6 times in the machine direction (MD) and from 6 to 13 times in the transverse direction (TD). The overall 2 5 orientation (MD x TD) preferably ranges from 25 to 80. After orientation, the edges of the film can be trimmed and the film wound onto a core.
The film structures of the present invention also exhibit unexpectedly increased stiffness and moduli (MD and TD) over film structures having conventional isotactic polypropylene-based core layers. The increased stiffness and moduli provide the film structure 3 0 with enhanced mechanical properties which, in turn, facilitate subsequent handling and . . ~ i , i ,. , g packaging. Moreover, the increases in MD and TD moduli are accomplished at relatively low orientation, thus reducing manufacturing costs and the associated likelihood of splitting.
The film structures of the present invention are formed having a thickness ranging from microns to 60 microns, preferably from 15 microns to 50 microns. Each tie layer 5 represents from 5% to 15% of the structure, while each skin layer represents from 2% to 6%
of the structure.
EXAMPLES
Water Vapor Transmission Rate (WVTR) in each of the following examples was measured at 37.8°C (100°F) and 90% Relative Humidity (ASTM F
3?2) and is expressed in 10 g/100 in2/day/mil.
Samples 1 a to 1 c were produced to compare the moisture barrier of an opaque PP-based film structure with an opaque HCPP-based film structure and an opaque HCPP-based film structure modified with a hydrogenated hydrocarbon.
Sample 1 a was produced with a core layer of 94% standard PP (Exxon*4252) and 6%
cavitating agent (Ceianese*1300a) having a thickness of 28.25 microns, and was coextruded with skin.layers of standard PP (Exxon*4252) each having a thickness of 6.0 microns to produce an ABA extrudate. The ABA extrudate was stretched 5.3 times in the machine direction and 9.0 times in the transverse direction.
Sample lb was produced with a core layer of 96% HCPP (Amoco~911?) and 4%
cavitating agent (Celanese*1300a) having a thickness of 26.75 microns, and was coextruded with skin layers of HCPP (Amocd'9117) each having a thickness of 5.75 microns to produce an ABA extrudate. The ABA extrudate was stretched 5.3 times in the machine direction and 9.0 times in the transverse direction.
2 5 Sample 1 c was produced with a core layer of 93% HCPP (Amoco*9117) and 4%
cavitating agent (Celanese*1300a) and 3% hydrogenated hydrocarbon (Arkon*P-115) having a thickness of 24.5 microns, and was coextruded with skin layers of HCPP (Amoco 9117) each having a thickness of 5.25 microns to produce an ABA extrudate. The ABA
extrudate was stretched 5.3 times in the machine direction and 9.0 times in the transverse direction.
* Trade-mark i n Sample Core % Cav. % Resin WVTR
Layer Agent Modifier (Aged) 1 a PP 6.0 0.0 .301 1 b HCPP 4.0 0.0 .242 1 c HCPP 4.0 3 .0 .216 Samples 2a to 2d were produced by samples 2a to 2d were produced to compare the moisture barrier of an opaque PP-based film structure with opaque HCPP-based film structures.
Sample 2a was produced with a core layer of 92% standard PP (Amoco*6317) and 8%
cavitating agent (Celanese 1300x) having a thickness of 25.0 microns, and was coextruded with skin layers of 94% standard PP (Amoco*6317), 4% Ti02 (Titanium Oxide), and 2% Talc each having a thickness of 5.35 microns to produce a ABA extrudate. The ABA
extmdate was stretched 5.5 times in the machine direction and 8.5 times in the transverse direction.
Sample 2b was produced with a core layer of 30% standard PP (Amoco'1i317), 66.8%
HCPP (Chisso''~A4141) and 3.2% cavitating agent (Celanese*1300a) having a thickness of 22.75 microns, and was coextruded with skin layers of 94% standard PP (Amoco 6317), 4%
Ti02 (Titanium Oxide), and 2% Talc each having a thickness of 4.85 microns to produce a ABA extrudate. The ABA extrudate was stretched 5.5 times in the machine direction and 8.5_ time in the transverse direction.
Sample Zc was produced with a core layer of 45% standard PP (Amoco*6317), S
1.8%
HCPP (Chisso XA4141) and 3.2% cavitating agent (Celanese*1300a) having a thickness of 22.75 microns, and was coextruded with skin layers of 94% standard PP
(Amoco*6317), 4%
Ti02 (Titanium Oxide), and 2% Talc each having a thickness of 4.85 microns to produce a ABA extrudate. The ABA extrudate was stretched 5.5 times in the machine direction and 8.5 times in the transverse direction.
Sample 2d was produced with a core layer of 30% standard PP (Amoco*6317), 66.8%
HCPP (Amoco*4141X) and 3.2% cavitating agent (Celanese*1300a) having a thickness of 22.75 microns, and was coextruded with skin layers of 94% standard PP
(Amoco'6317), 4%
Ti02 (Titanium Oxide), and 2% Talc each having a thickness of 4.85 microns to produce a * Trademark ABA extrudate. The ABA extrudate was stretched S.5 times in the machine direction and 8.5 times in the transverse direction.
Sample Core % Cav. % PP' % HCPP WVTR
5 Layer Agent in Core in Core (Unaged) 2a PP 8.0 92.0 0.0 0.47 2b HCPP 3.2 30.0 66.8 0.39 2c HCPP 3.2 45.0 51.8 0.39 10 2d HCPP ~ 3.2 30.0 ~ 66.8 0.40 ' Total % PP includes 30.0% of reprocessed polypropylene Sample 3a was produced to demonstrate the moisture barrier of an opaque HCPP-based film structure containing a low level of cavitating agent.
Sample 3a was produced with a core layer of 97% HCPP (Amoco 9218) and 3%
cavitating agent (Celenese*1300a) having a optical thickness of 28 microns.
This core was coextruded with skin layers of 92% HCPP (Amoco''~218) and 8% whitening agent (Schulman*
CTW5050) each having a thickness of 3.5 microns to produce an ABA extrudate.
The ABA
extrudate was stretched 5.3 times in the machine direction and 8.5 times in the transverse direction.
Sample Core % Cav. % Resin WVTR
Layer Agent Modifier (Aged) 3 a HCPP 3.0 0.0 0.24 It is thus readily apparent from the data set forth above that the present invention provides an opaque film structure exhibiting significantly improved moisture barrier properties, as compared to the prior art control samples (samples la and 2a). The films of the present invention exhibited substantially the same degree ofopacity as the prior art control samples (la and 2a), while utilizing significantly lower levels of cavitating agent.
Moreover, these film structures exhibit enhanced mechanical properties, e.g., improved stiffness and moduli and provide ease of manufacturing, e.g., increased line operability and line percentage uptime (as observed during manufacture of the present film structures).
* Trade-mark
The present invention, which addresses the needs of the prior art, relates to an opaque polymeric film having enhanced moisture barrier and mechanical properties. The film has a base layer which includes a blend of a first polypropylene polymer having an isotactic stereoregularity greater than 93% and a cavitating agent in an amount effective to cavitate the base layer.
In one preferred embodiment, the base layer includes less than 6% by weight of 1 o cavitating agent, and preferably from 2% to S% of cavitating agent. In another preferred embodiment, the base layer further includes a resin modifier in an amount up to 9% by weight of said base layer. The resin modifier is preferably a hydrogenated hydrocarbon.
In still another preferred embodiment, at least one tie layer is adhered to the cavitated base layer. A skin is preferably adhered to the other side of the tie layer.
The tie layer, which facilitates adherence of the skin layer to the cavitated base layer, is preferably formed from polypropylene. The skin layer is preferably formed from an ethylene-propylene random copolymer or an ethylene-propylene-butene-1 terpolymer.
As a result, the present invention provides an opaque polypropylene-based film structure exhibiting enhanced moisture barrier and mechanical properties.
These improved 2 o properties are obtained without a negative impact on such film characteristics as dimensional stability. More to the point, these improved properties are obtained while using a significantly lower level of cavitating agent, thus providing improved production uptime and reduced raw material costs. The film structure further exhibits a high degree of machinability and processability.
2 5 The present invention is prepared by blending high crystallinity polypropylene (HCPP) with a cavitating agent in an amount effective to cavitate the HCPP. The HCPP
has an isotactic stereoregularity of greater than 93%, preferably from 94% to 98%.
The base layer preferably includes less than 6% by weight of the cavitating agent.
T _ ~_._.___ Commercially suitable PPs include Fina 3371 (available from Fina Oil and Chemical Co., Dallas, Texas), Exxon 4612 and Exxon X052 (available from Exxon Chemical Co., Houston, Texas) and Amoco*6361 (available from Amoco Chemical Co., Chicago, Illinois).
Commercially suitable HCPPs include Amoco 9117, Amoco 9119 and Amoco''~218(available from Amoco Chemical Co., Chicago, Illinois), and Chisso"i~5010 and Chisso~2805 (available from Chisso Chemical Co., Ltd., Tokyo, Japan). Suitable HCPPs are also available from Solvay in Europe.
The HCPP has a high isotactic stereoregularity, resulting in higher crystallinity than conventional isotactic polypropylene, i.e, greater than 93%. (Conventional isotactic polypropylene is defined herein as having an isotactic stereoregularity of from 90% to 93%.) The HCPP thus exhibits higher stiffness, surface hardness, lower deflection at higher temperatures and better creep properties than conventional isotactic polypropylene. Further information relating to HCFP, including methods for preparation thereof, is disclosed in U.S.
Patent No. 5,063,264.
For purposes of the present invention, stereoregularity can be determined by IR
spectroscopy according to the procedure set out in "Integrated Infrared Band Intensity Measurement of Stereoregularity in Polypropylene," L L. Koenig and A.VanRoggen, Journal of Applied Polymer Science, Vol. 9, pp. 359-367 (1965) and in "Chemical Microstructure of Polymer Chains," J. L. Koenig, Wiley-Inerscience Publication, John Wiley and Sons, New 2 o York, Chichester, Brisbane, Toronto. Stereoregularity can also be determined by decahydronaphthalene (decalin) solubility and nuclear magnetic resonance spectroscopy The use of HCPP in the base layer unexpectedly lowers the amount of cavitating agent required to cavitate the film and produce the desired opacity. More particularly, the use of 2 5 HCPP in the base layer lowers the amount of cavitating agent necessary to cavitate the film from the prior art levels of approximately 6% to 12% by weight, or greater, to a level in the present invention of less than 6% by weight, and preferably from 2% to 5% by weight. This reduction in loading level of the cavitating agent is significant in that it results in greater production uptime. In addition, the reduction in the amount of cavitating agent necessary to 3 o cavitate the base layer translates into a significant cost savings in raw materials.
* Trade-mark More to the point, the blend of HCPP and cavitating agent in the base layer provides a significant improvement in the moisture barrier of the resultant film. As demonstrated in the example set forth hereinbelow, improvements in moisture barrier of up to 20%
to 30% may be achieved with the film structures of the present invention. It will be recognized by those skilled in the art that this 20% to 30% improvement in moisture barrier is significant in the food packaging industry.
Preferred cavitating agents include polybutylene terephthalate (PBT), calcium carbonate (CaCO,),.polyester (FET), polyamides including nylon and other polymers and/or inorganic materials which are incompatible.with HCPP.
In one preferred embodiment, the HCPP in the base layer is blended with a conventional isotactic polypropylene (PP). The base layer preferably includes an amount of PP effective to plasticize the base layer and thus increase the processability of the resultant extruded film structure. The blended base layer increases manufacturing efFrciency by increasing line operability and line percentage uptime. For example, the blended base layer reduces the force necessary to stretch the film and in addition facilitates edge trimming of the extruded film. Thus, the blended base layer results in a reduction in cost associated with manufacture of the film structure.
In another preferred embodiment, a resin modifier is blended with the base layer precursor. The resin modifier is present in an amount of up to 9% by weight, and preferably 2 o from 3% to 6% by weight. The blending may be accomplished by the direct feeding of HCPP
and resin modifier into the film extruder or by use of a masterbatch. One preferred method of blending the components utilizes a masierbatch formed of HCPP and resin modifier, e.g., 80'%
HCPP and 20% resin modifier. The masterbatch is then blended with additional HCPP, which reduces the concentration of the resin modifier to the final desired level.
Applicant has discovered that polymeric film structures formed from HCPP exhibit unexpectedly large decreases in water vapor transntission with small additions of resin modifier. The moisture barrier increases as the loading level of resin modifier is increased until a point is reached (less than 10% resin 3 o modifier) at which further increases in the loading level of the resin modifier do not provide further substantial increases in moisture barrier. Moreover, the HCPP-based film structures also provide enhanced mechanical properties without suffering from losses in dimensional stability, as is common in prior art film structures which may require upwards of 20% resin modifier to achieve maximum moisture barrier.
The resin modifier is preferably a low molecular weight hydrogenated hydrocarbon which is compatible with the HCPP polymer and which provides the desired enhancement of film properties. The preferred resin modifier has a number average molecular weight less than 5000, preferably less than 2000, and more preferably from 500 to 1000. The resin modifier can be natural or synthetic and preferably has a softening point of from 60° to 180°C.
1o Particularly suitable hydrocarbons which can be subsequently hydrogenated are the hydrocarbon resins. Preferred hydrocarbon resins include among others petroleum resins, terpene resins, styrene resins and cyclopentadiene resins.
Examples of commercially available hydrogenated hydrocarbon resins suitable for use in the present invention are those sold under the trademarks PICCOLYTE, REGALREZ and REGALITE by Hercules Corporation of Delaware and under the trademark ESCOREZ
by Exxon Chemical Company of Houston, Texas. The ESCOREZ resins are particularly preferred hydrogenated hydrocarbon resins.
One particularly preferred resin modifier is referred to herein as a saturated alicyclic resin. The saturated alicyclic resins are obtained by the hydrogenation of aromatic 2 o hydrocarbon resins. The aromatic resins are themselves obtained by polymerizing reactive unsaturated hydrocarbons containing, as the principal component, aromatic hydrocarbons in which the reactive double bonds are generally in side-chains. More particularly, the alicyclic resins are obtained from the aromatic resins by hydrogenating the latter until all, or almost all, of the unsaturation has disappeared, including the double bonds in the aromatic rings.
The saturated alicyclic resins used in the present invention have a softening point from 85 ° to 140 ° C, and preferably from 100 ° to 140 ° C, as measured by the ball and ring method.
Examples of commercially available saturated alicyclic resins suitable for use in the present invention are those sold under the trademark ARKON-P by Arakawa Forest Chemical Industries, Ltd. of Japan.
In one preferred embodiment, a tie layer of an olefinic polymer is adhered to the base layer. Inasmuch as the skin layers discussed below may not adequately adhere to the cavitated base layer, a tie layer compatible with the cavitated base layer is first adhered to the base layer.
A skin layer of an olefinic polymer is, in turn, adhered to the tie layer.
Both the tie and skin layers are preferably coextruded with the base layer. The tie layers may include a whitening agent such as Ti02.
Suitable olefinic polymers utilized for the skin layers) include i) ethylene homopolymers, ii) copolymers of ethylene and propylene, iii) copolymers of ethylene or propylene and butylene or another alpha olefin having 5 to 10 carbon atoms, iv) terpolymers of ethylene, propylene and butylene or another alpha-olefin having 5 to 10 carbon atoms, and v) mixtures thereof.
Olefinic polymers which are particularly preferred for the skin layers) include ethylene-propylene copolymers with propylene as the main constituent and an ethylene content of 2% to I 0% by weight (relative to the weight of the copolymer), propylene-butylene copolymers with propylene as the main constituent and a butylene content of 0.5% to 25% by weight (relative to the weight of the copolymer), and ethylene-propylene-butene-1 terpolymers with propylene as the main constituent, 0.5% to 7% by weight of ethylene and 5% to 30% by weight of butene-1 (each time relative to the weight of the terpolymer), and mixtures of these polymers. The co- and terpolymers are preferably random polymers.
2 0 In a still further preferred embodiment, a coating is applied to the outer surface of the skin layer(s). An acrylic coating, which provides improved printability, machinability and aroma barrier characteristics, may be applied to one of the skin layers. A
heat seal coating such as ethylene methyl acrylate (EMA) or ethylene acrylic acid (EAA) may be applied to the other skin layer. Other suitable coatings include polyvinylidene chloride (PVDC), polyvinyl alcohol (PVOH) and low temperature heat seal coatings, as disclosed in commonly-owned U. S. Patent No. 5,419,960.
In order to further improve certain properties of the resultant film, effective amounts of additives such as antiblocking agents, antistatic agents and/or slip agents may be contained in the base layer, tie layers) and/or skin layer(s).
_ ___ ._ __. .____~____~_ ._._..._.___ _._____._. __.._~_. _._ _.___.__ _.
Preferred antiblocking agents include silica, talc, clay, sodium aluminum silicate, and conventional inorganic anti-blocks. Other suitable antiblocking agents include inorganic additives, such as silicon dioxide, calcium carbonate, magnesium silicate, aluminum silicate, calcium phosphate, and the like, and/or incompatible organic polymers, such as polyamides, polyesters, polycarbonates and the like.
Preferred antistatic agents include alkali alkane sulfonates and essentially straight-chain, saturated aliphatic tertiary amines possessing aliphatic radicals with 10 to 20 carbon atoms and being substituted by 2-hydroxyalkyl-(C, to C4) groups. Preferred amines are N,N-bis-(2-hydroxyethyl)-alkylamines having 10 to 20, preferably 12 to 18, carbon atoms in their 1o alkyl groups. The effective amount of antistatic agent varies in the range from 0.05% to 3%
by weight, relative to the weight of the layer.
Preferred slip agents include higher aliphatic acid amides, higher aliphatic acid esters, waxes, metallic soaps and silicone oils such as polydimethylsiloxane. The effective added amount of lubricant varies from 0.1% to 2% by weight.
The multilayer films of the present invention may be prepared employing commercially available systems for coextruding resins. As mentioned, the blended HCPP and cavitating agent precursor is preferably coextruded with at least one second and at least one third polymeric material, which form the tie and skin layers, respectively. The polymers can be brought to the molten state and coextruded from a conventional extruder through a flat sheet 2 o die, the melt streams being combined in an adapter prior to being extruded from the die. After leaving the die orifice, the multilayer film structure is quenched.
The film structure of the present invention is preferably biaxially oriented.
In orie preferred embodiment, the film structure is stretched from 4.5 to 6 times in the machine direction (MD) and from 6 to 13 times in the transverse direction (TD). The overall 2 5 orientation (MD x TD) preferably ranges from 25 to 80. After orientation, the edges of the film can be trimmed and the film wound onto a core.
The film structures of the present invention also exhibit unexpectedly increased stiffness and moduli (MD and TD) over film structures having conventional isotactic polypropylene-based core layers. The increased stiffness and moduli provide the film structure 3 0 with enhanced mechanical properties which, in turn, facilitate subsequent handling and . . ~ i , i ,. , g packaging. Moreover, the increases in MD and TD moduli are accomplished at relatively low orientation, thus reducing manufacturing costs and the associated likelihood of splitting.
The film structures of the present invention are formed having a thickness ranging from microns to 60 microns, preferably from 15 microns to 50 microns. Each tie layer 5 represents from 5% to 15% of the structure, while each skin layer represents from 2% to 6%
of the structure.
EXAMPLES
Water Vapor Transmission Rate (WVTR) in each of the following examples was measured at 37.8°C (100°F) and 90% Relative Humidity (ASTM F
3?2) and is expressed in 10 g/100 in2/day/mil.
Samples 1 a to 1 c were produced to compare the moisture barrier of an opaque PP-based film structure with an opaque HCPP-based film structure and an opaque HCPP-based film structure modified with a hydrogenated hydrocarbon.
Sample 1 a was produced with a core layer of 94% standard PP (Exxon*4252) and 6%
cavitating agent (Ceianese*1300a) having a thickness of 28.25 microns, and was coextruded with skin.layers of standard PP (Exxon*4252) each having a thickness of 6.0 microns to produce an ABA extrudate. The ABA extrudate was stretched 5.3 times in the machine direction and 9.0 times in the transverse direction.
Sample lb was produced with a core layer of 96% HCPP (Amoco~911?) and 4%
cavitating agent (Celanese*1300a) having a thickness of 26.75 microns, and was coextruded with skin layers of HCPP (Amocd'9117) each having a thickness of 5.75 microns to produce an ABA extrudate. The ABA extrudate was stretched 5.3 times in the machine direction and 9.0 times in the transverse direction.
2 5 Sample 1 c was produced with a core layer of 93% HCPP (Amoco*9117) and 4%
cavitating agent (Celanese*1300a) and 3% hydrogenated hydrocarbon (Arkon*P-115) having a thickness of 24.5 microns, and was coextruded with skin layers of HCPP (Amoco 9117) each having a thickness of 5.25 microns to produce an ABA extrudate. The ABA
extrudate was stretched 5.3 times in the machine direction and 9.0 times in the transverse direction.
* Trade-mark i n Sample Core % Cav. % Resin WVTR
Layer Agent Modifier (Aged) 1 a PP 6.0 0.0 .301 1 b HCPP 4.0 0.0 .242 1 c HCPP 4.0 3 .0 .216 Samples 2a to 2d were produced by samples 2a to 2d were produced to compare the moisture barrier of an opaque PP-based film structure with opaque HCPP-based film structures.
Sample 2a was produced with a core layer of 92% standard PP (Amoco*6317) and 8%
cavitating agent (Celanese 1300x) having a thickness of 25.0 microns, and was coextruded with skin layers of 94% standard PP (Amoco*6317), 4% Ti02 (Titanium Oxide), and 2% Talc each having a thickness of 5.35 microns to produce a ABA extrudate. The ABA
extmdate was stretched 5.5 times in the machine direction and 8.5 times in the transverse direction.
Sample 2b was produced with a core layer of 30% standard PP (Amoco'1i317), 66.8%
HCPP (Chisso''~A4141) and 3.2% cavitating agent (Celanese*1300a) having a thickness of 22.75 microns, and was coextruded with skin layers of 94% standard PP (Amoco 6317), 4%
Ti02 (Titanium Oxide), and 2% Talc each having a thickness of 4.85 microns to produce a ABA extrudate. The ABA extrudate was stretched 5.5 times in the machine direction and 8.5_ time in the transverse direction.
Sample Zc was produced with a core layer of 45% standard PP (Amoco*6317), S
1.8%
HCPP (Chisso XA4141) and 3.2% cavitating agent (Celanese*1300a) having a thickness of 22.75 microns, and was coextruded with skin layers of 94% standard PP
(Amoco*6317), 4%
Ti02 (Titanium Oxide), and 2% Talc each having a thickness of 4.85 microns to produce a ABA extrudate. The ABA extrudate was stretched 5.5 times in the machine direction and 8.5 times in the transverse direction.
Sample 2d was produced with a core layer of 30% standard PP (Amoco*6317), 66.8%
HCPP (Amoco*4141X) and 3.2% cavitating agent (Celanese*1300a) having a thickness of 22.75 microns, and was coextruded with skin layers of 94% standard PP
(Amoco'6317), 4%
Ti02 (Titanium Oxide), and 2% Talc each having a thickness of 4.85 microns to produce a * Trademark ABA extrudate. The ABA extrudate was stretched S.5 times in the machine direction and 8.5 times in the transverse direction.
Sample Core % Cav. % PP' % HCPP WVTR
5 Layer Agent in Core in Core (Unaged) 2a PP 8.0 92.0 0.0 0.47 2b HCPP 3.2 30.0 66.8 0.39 2c HCPP 3.2 45.0 51.8 0.39 10 2d HCPP ~ 3.2 30.0 ~ 66.8 0.40 ' Total % PP includes 30.0% of reprocessed polypropylene Sample 3a was produced to demonstrate the moisture barrier of an opaque HCPP-based film structure containing a low level of cavitating agent.
Sample 3a was produced with a core layer of 97% HCPP (Amoco 9218) and 3%
cavitating agent (Celenese*1300a) having a optical thickness of 28 microns.
This core was coextruded with skin layers of 92% HCPP (Amoco''~218) and 8% whitening agent (Schulman*
CTW5050) each having a thickness of 3.5 microns to produce an ABA extrudate.
The ABA
extrudate was stretched 5.3 times in the machine direction and 8.5 times in the transverse direction.
Sample Core % Cav. % Resin WVTR
Layer Agent Modifier (Aged) 3 a HCPP 3.0 0.0 0.24 It is thus readily apparent from the data set forth above that the present invention provides an opaque film structure exhibiting significantly improved moisture barrier properties, as compared to the prior art control samples (samples la and 2a). The films of the present invention exhibited substantially the same degree ofopacity as the prior art control samples (la and 2a), while utilizing significantly lower levels of cavitating agent.
Moreover, these film structures exhibit enhanced mechanical properties, e.g., improved stiffness and moduli and provide ease of manufacturing, e.g., increased line operability and line percentage uptime (as observed during manufacture of the present film structures).
* Trade-mark
Claims (14)
1. An opaque polymeric film having enhanced moisture barrier and mechanical properties, comprising:
a base layer including a blend of a first polypropylene polymer having an isotactic stereoregularity of from about 94% to about 98% and from about 2% to about 5% by weight of said base layer of a cavitating agent to cavitate said base layer.
a base layer including a blend of a first polypropylene polymer having an isotactic stereoregularity of from about 94% to about 98% and from about 2% to about 5% by weight of said base layer of a cavitating agent to cavitate said base layer.
2. The film according to Claim 1, wherein said cavitating agent is selected from the group consisting of polybutylene terephthalate, calcium carbonate, polyester and polyamide.
3. The film according to Claim 1, wherein said base layer further includes a synthetic resin modifier in and amount up to 9% by weight of said base layer.
4. The film according to Claim 3, wherein said base layer includes from about 3% to about 6% of said resin modifier.
5. The film according to Claim 4, wherein said resin modifier is a hydrogenated hydrocarbon.
6. The film according to Claim 5, wherein said hydrogenated hydrocarbon is a hydrogenated hydrocarbon resin.
7. The film according to any one of Claims 1 to 6, wherein said base layer further comprises an additive selected from the group consisting of antiblocking agents, antistatic agents and slip agents.
8. The film according to any one of Claims 1 to 7, further comprising at least one tie and at least one skin layer, and wherein said tie layer is interposed between said cavitated base layer and said skin layer and is formed form a polymeric material compatible with both said cavitated base layer and said skin layer whereby said layers are adhered together due to interaction of said polymeric materials.
9. The film according to Claim 8, wherein said tie layer is polypropylene.
10. The film according to Claims 8 or 9, wherein said skin layer is formed from a polymer selected from the group consisting of ethylene-propylene random copolymers and ethylene-propylene-butene-I terpolymers.
11. The film according to any one of Claims 8 to 10, wherein said skin layer further comprises an additive selected from the group consisting of antiblocking agents, antistatic agents and slip agents.
12. The film according to any one of Claims 8 to 11, wherein said skin layer includes an outer surface and further comprising a coating layer on the outer surface of said skin layer.
13. The film according to Claim 12, wherein said coating layer is selected from the group consisting of ethylene methyl acrylate, ethylene acrylic acid, polyvinylidene chloride and polyvinyl alcohol.
14. The film according to any one of Claims 1 to 13, wherein said blend further comprises a second polypropylene polymer having an isotactic stereoregularity of from about 90% to about 93%.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US69062096A | 1996-07-31 | 1996-07-31 | |
| US08/690,620 | 1996-07-31 | ||
| PCT/US1997/012995 WO1998004403A1 (en) | 1996-07-31 | 1997-07-23 | Opaque films comprising isotactic polypropylene |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2262081A1 CA2262081A1 (en) | 1998-02-05 |
| CA2262081C true CA2262081C (en) | 2006-01-03 |
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ID=24773215
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|---|---|---|---|
| CA002262081A Expired - Fee Related CA2262081C (en) | 1996-07-31 | 1997-07-23 | Opaque films comprising isotactic polypropylene |
Country Status (11)
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|---|---|
| EP (1) | EP0914245A4 (en) |
| JP (1) | JP2001525737A (en) |
| KR (1) | KR20000029693A (en) |
| CN (1) | CN1226854A (en) |
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| AU (1) | AU712306B2 (en) |
| BR (1) | BR9710775A (en) |
| CA (1) | CA2262081C (en) |
| ID (1) | ID17972A (en) |
| TW (1) | TW339312B (en) |
| WO (1) | WO1998004403A1 (en) |
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| US6312825B1 (en) * | 1998-09-21 | 2001-11-06 | Exxonmobil Oil Corporation | High barrier multi-layer film |
| WO2000069962A1 (en) * | 1999-05-12 | 2000-11-23 | Mobil Oil Corporation | Method for producing improved opaque polymeric films |
| JP2003511275A (en) * | 1999-10-13 | 2003-03-25 | モービル・オイル・コーポレイション | Heat sealable multi-layer white opaque film |
| WO2002040270A1 (en) * | 2000-11-14 | 2002-05-23 | Exxonmobil Oil Corporation | Plastic film having improved imaging properties |
| US6946203B1 (en) * | 2002-12-31 | 2005-09-20 | Exxon Mobil Oil Corporation | Multilayer polyolefin substrate with low density core and stiff outer layers |
| US7314901B2 (en) | 2003-01-30 | 2008-01-01 | Exxonmobil Chemical Patents Inc. | Polypropylene films |
| KR101041924B1 (en) * | 2009-08-26 | 2011-06-16 | (주)상아프론테크 | Entry Sheet for Drilling hole in Printed Circuit Boards, Lubricant Resin Composition and Method for Preparing the Same |
| EP4196521A4 (en) * | 2021-06-07 | 2024-10-23 | Jindal Films Americas Llc | Maintaining suitable sealability and hot tack strengths of acrylic- and acetate-based coatings when using base films containing hcr to improve their water-vapor barriers |
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|---|---|---|---|---|
| JPS5129191B2 (en) * | 1972-01-24 | 1976-08-24 | ||
| US4377616A (en) * | 1981-12-30 | 1983-03-22 | Mobil Oil Corporation | Lustrous satin appearing, opaque film compositions and method of preparing same |
| US5231126A (en) * | 1985-04-01 | 1993-07-27 | Shi Guan Yi | Beta-crystalline form of isotactic polypropylene and method for forming the same |
| US4632869A (en) * | 1985-09-03 | 1986-12-30 | Mobil Oil Corporation | Resin composition, opaque film and method of preparing same |
| US4681803A (en) * | 1985-10-18 | 1987-07-21 | Mobil Oil Corporation | Pigmented, heat-sealable coating composition for application to oriented polyolefin films |
| US4944990A (en) * | 1988-06-16 | 1990-07-31 | Mobil Oil Corporation | Oriented white opaque multilayer heat sealable film and method of forming same |
| US5147936A (en) * | 1991-04-08 | 1992-09-15 | Mobil Oil Corporation | LLDPE films by blending with specific polypropylenes |
| WO1994014606A1 (en) * | 1992-12-21 | 1994-07-07 | Mobil Oil Corporation | Multi-layer high opacity film structures |
| DE4307440A1 (en) * | 1993-03-10 | 1994-09-15 | Wolff Walsrode Ag | Multilayer, stretched, heat-sealable polypropylene film |
| US6322883B1 (en) * | 1994-07-15 | 2001-11-27 | Exxonmobil Oil Corporation | Uniaxially shrinkable biaxially oriented polypropylene film with HDPE skin |
| US5500282A (en) * | 1994-07-15 | 1996-03-19 | Mobil Oil Corporation | High moisture barrier OPP film containing high crystallinity polypropylene and terpene polymer |
| EP0831994B2 (en) * | 1995-04-25 | 2012-02-15 | ExxonMobil Oil Corporation | Production of uniaxially shrinkable biaxially oriented polypropylene films |
| US5827615A (en) * | 1996-07-15 | 1998-10-27 | Mobil Oil Corporation | Metallized multilayer packaging film |
| DE19635503A1 (en) * | 1996-09-02 | 1998-03-05 | Basf Ag | Low-whitening, tough modified propylene polymers |
-
1997
- 1997-07-23 BR BR9710775-1A patent/BR9710775A/en not_active Application Discontinuation
- 1997-07-23 JP JP50897898A patent/JP2001525737A/en active Pending
- 1997-07-23 AU AU38929/97A patent/AU712306B2/en not_active Ceased
- 1997-07-23 EP EP97936197A patent/EP0914245A4/en not_active Withdrawn
- 1997-07-23 KR KR1019997000772A patent/KR20000029693A/en not_active Application Discontinuation
- 1997-07-23 CA CA002262081A patent/CA2262081C/en not_active Expired - Fee Related
- 1997-07-23 CN CN97196866A patent/CN1226854A/en active Pending
- 1997-07-23 WO PCT/US1997/012995 patent/WO1998004403A1/en not_active Application Discontinuation
- 1997-07-31 ID IDP972676A patent/ID17972A/en unknown
- 1997-07-31 AR ARP970103485A patent/AR008138A1/en unknown
- 1997-08-21 TW TW086110950A patent/TW339312B/en active
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| AU3892997A (en) | 1998-02-20 |
| TW339312B (en) | 1998-09-01 |
| AU712306B2 (en) | 1999-11-04 |
| WO1998004403A1 (en) | 1998-02-05 |
| KR20000029693A (en) | 2000-05-25 |
| BR9710775A (en) | 2002-03-05 |
| ID17972A (en) | 1998-02-12 |
| EP0914245A4 (en) | 2001-09-12 |
| JP2001525737A (en) | 2001-12-11 |
| CA2262081A1 (en) | 1998-02-05 |
| EP0914245A1 (en) | 1999-05-12 |
| AR008138A1 (en) | 1999-12-09 |
| CN1226854A (en) | 1999-08-25 |
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