Description of the Prior Art Oriented, multilayered films are an important class of industrial products useful principally in the wrapping or packaging of various products in commerce.

In particular, oriented isotactic polypropylene film is known to be useful for its high barrier properties, clarity and stiffness. Polypropylene for oriented films is typically isotactic homopolymer, or are modified polypropylene blends of isotactic polypropylene with differing isotactic polypropylene, e.g., differing melt flow rates (MFR) or tacticity, atactic polypropylene, syndiotactic polypropylene, random polypropylene copolymers having minor amounts of ethylene or higher a- olefins, and ethylene copolymers, see for example, U.S. patent 4,950,720 and WO 96/02386. As indicated in U.S. patent 4,921,749 and related art, other components such as petroleum resins may be added as well to modify properties such as heat sealing performance, gas permeability and stiffness. Such oriented polypropylene, particularly biaxially oriented polypropylene (BOPP), has many desirable properties. However, excellent hot tack and heat seal are not among these since such films lack significant heat sealing and hot tack performance at operating temperatures suited to efficient industrial practice.

Accordingly, various polymeric layers have been used or proposed as heat sealing layers for biaxially oriented polypropylene film. Among those used industrially and taught in the patent literature are polyolefins, ethylene-based and propylene-based. Preferred heat sealing layers for BOPP have in the past typically

been high propylene-content polyolefins, e.g., propylene-ethylene copolymers with 1-20 wt% ethylene, and propylene-ethylene-butene terpolymers with up to about 10 wt% each of ethylene and butene and blends of those with other olefin polymers. See for example, U.S. patents 4,643,945 (LLDPE with propylene terpolymer) and 4,921,749 (propylene-ethylene copolymers) and the others listed above. These polymer selections do reduce the chemical dissimilarity of the sealing layer and core layers so as to allow good adhesion between them, but result in the requirement that subsequent heat sealing be conducted at temperatures at or above about 120 "C, requiring long contact time with heating elements or high heat input to achieve the necessary temperature ranges.

Summary of the Invention The invention is an oriented multilayer film comprising at least one outer layer comprising from 50 to 100 wt.% of said outer layer an ethylene copolymer having a density of 0.900-0.935 g/cm3 and a CDBI of 50-95% said outer layer being in contact with a polypropylene core layer, and said film having been made by coextrusion of said ethylene copolymer and said polypropylene layer and subsequent orientation.Preferably the ethylene copolymer outer or skin layer, or layers, will have a MWD (MW/M,,) of 1.8-3.5 and a MI of 0.5-10 (ASTM D 1238, 190 "C, 2.16 kg). The coextruded layers can be biaxially oriented on tenter frame equipment without difficulties caused by the presence of low molecular weight amorphous polymer fractions inherently present in traditional Ziegler-Natta linear low density polyethylene. Problems of undesirable adherence to drums and jaws in processing and the presence of extractables in the films made hereby are essentially eliminated. Optical properties of biaxially oriented polypropylene films (BOPP) are retained while the sealing temperature is lowered and the heat seal strength and the hot tack properties are improved. The ethylene copolymer heat seal layer thus offers a practical, economical solution for preparing improved heat seal BOPP for all of stiff, flexible and heat shrinkable packaging.

Brief Description of the Figures Figure 1 is a graph of the heat seal and hot tack performance of the film of the examples.

Detailed Description of the Invention Ethylene copolymers suitable in accordance with the invention are commercially available and can be made by essentially single-sited catalysts such as metallocene catalysts. The use of the term "essentially single-sited catalyst" refers here to any olefin polymerization catalyst that provides narrow molecular weight distribution (MWD) (MW/Mn) and narrow composition distribution, as measured by the composition distribution breadth index (CDBI). Commercially available products specifically include the metallocene LLDPE resins (m-LLDPE) marketed by Exxon Chemical Co., Houston, Texas, as EXCEEDS 350D60 (ethylene-hexene copolymer, MI = 1.0, density 0.917 g/cm3) and 377L60 (ethylene-hexene copolymer, MI = 1.0, density 0.922), and the metallocene plastomer ethylene copolymers marketed under the tradenames EXACTS, available from Exxon Chemical Co. and AFFINITY , available from Dow Chemical Company, Midland, Michigan, where such plastomers have densities at or above about 0.900. Typically the ethylene copolymers will comprise as comonomers any C3-C12 oc-olefin, preferably one or more C4-Cs a-olefin. The comonomer content is established by the measured density, the density preferably being in the range from 0.910 to 0.925 g/cm3, most preferably from 0.915 to 0.925 g/cm3. Preferably the molecular weight of the invention ethylene copolymers as measured in MI (polyethylene melt index, ASTM D 1238) will be in the range from about 0.7 - 8.0, and most preferably 0.7 - 5.0 . The MWD is typically about 2.0 - 3.5, preferably 2.0 - 2.7 . The CDBI will preferably be above about 55 %, most preferably above 65 %. The melt index ratios (MIR, 121/12) of the suitable ethylene copolymers will typically range from about 16 to about 50. Additional description of film suitable ethylene copolymers can be found in copending U.S. application Ser. No. 08/755,105, filed 22 November, 1996, the description of which is incorporated by reference for U.S. patent practice.

Additional ethylene copolymer compositions suitable as sealing layers in accordance with the invention include polyethylene blend compositions wherein the ethylene copolymer defined above comprises at least 50 wt% and the complement is minor amounts of essentially compatible ethylene-based homopolymers or copolymers comprising ethylene and one or more of C3-C12 a- olefins, cyclic olefins, vinyl aromatic and polar vinyl monomers, such as norbornene, alkyl-substituted norbornenes, styrene, alkyl-substituted styrenes, vinyl acetate, acrylic acid, methyl acrylate, butylacrylate, etc. The blend compositions comprising ethylene-a-olefin copolymers are preferably those having an overall density of from about 0.910 to about 0.925 and MI of about from 0.7 to 5.0. For blends comprising the other ethylene copolymers, the copolymers are preferably those having 2-5 mol% comonomer and equivalent MI.

Specific blend polyethylenes include any of LDPE, plastomers, LLDPE, MLDPE or HDPE, as those terms are used in the art, prepared by Ziegler-Natta polymerization, essentially single-sited coordination polymerization, and high pressure-free radical polymerization. Polymers comprising vinyl monomers include ethylene-vinyl (EVA), ethylene-vinyl alcohol (EVOH), ethylene acrylic acid (EAA), ethylene-methylacrylate (EMA), and the like. Blend suitable ethylene copolymers are those that have ethylene content sufficient to provide ethylene crystallinity so as to assure that the blend compositions will not be subject to gross phase separation within the blend compositions upon cooling.

Copolymers of lower crystallinity, and thus density at or below about 0.915 ("VLDPE"), including certain plastomer ethylene copolymers with C4-C8 a- olefins having densities from about 0.870 to about 0.915 g/cm3 are particularly suitable as blend components when present in sufficient amounts to allow increased line speeds due to the presence of the lower melting point, low density copolymers. The VLDPE copolymers will preferably be present in an amount up to about 30 wt.%, preferably from about 15-20 wt.%. Further description of the VLDPE and its uses in film applications appears in U.S. patents 5,206,075 and

5,358,792, both of which are incorporated by reference for purposes of U.S. patent practice.

Suitable polypropylene core or outer layer or layers will comprise any of the isotactic polypropylene compositions or blends known to be suitable for use as uniaxially or biaxially oriented films. The background art is instructive and is incorporated by reference for purposes of U.S. patent practice. Both of traditional Ziegler-Natta polypropylene resins and those of the newer essentially single-sited catalysts are suitable where having molecular weights sufficient to assure a match in melt viscosity suitable for coextrusion. Thus propylene polymers having melt flow rate "MFR" (ASTM D 1238, 230 "C, 2.16 kg) of from about 1.0 to about 40, preferably to 10, most preferably to 6.0 are suitable. The film grade polypropylene products ESCORENEB PP4592 E7, PP4372, and PP 4252 El of Exxon Chemical Co. are particularly suitable. Additionally, polypropylene random copolymers containing up to about 15 mol. % of at least one C2 - C8 a- olefin other than propylene will be suitable as a coextrudable polypropylene layer, as core, outer or intermediary layer.

Methods of preparing coextruded films are well known in the art. For this invention the ethylene copolymer compositions suitable as sealing layers and the polypropylene compositions are separately but concurrently extruded and joined for coextrusion prior to orientation. Because the melt viscosity of the preferred ethylene copolymers, or blends comprising them, is high enough to maintain sufficient dimensional stability at processing temperatures necessary to extrude the polypropylene film, both of thick and thin films of uniform thickness across the film surface can be maintained. The lack of low molecular weight amorphous fractions and the sufficiently high melting points of the ethylene copolymer compositions allow excellent processing without sticking to processing equipment yet while retaining the particularly suitable dimensional stability.

A preferred method of preparing the films according to the invention comprises a coextrusion process with subsequent orientation of the coextrudate.

Though previously known in the industry that lower-melting point polymers can

be applied by the coating method, where the polymer is extruded in a molten or softened state onto the preformed higher softening point polymer film, it is also known that the use of chemically dissimilar polymers can result in insufficient adhesion. between the layers. Thus the use of additional tie layers (or adhesive layers) capable of adhering to both layers is often recommended when two different polymers are to be combined. See, e.g., J. Stepek, et al, Polymers As Materials For Packaging , Ch. 5, p. 346-349 (Ellis Horwood Ltd., 1987, English language edition).

The discovery of this invention however resulted from the observation that the use of coextrusion multiple extruders in two or more streams at least one of which provides the ethylene copolymer compositions and another of which provides the polypropylene compositions, and concurrent feeding into a multi- channel die such that the two layers are in contact with each other for slit-die extrusion and subsequent orientation, can be used to prepare films that retain excellent adhesion between the layers and excellent composite film properties without the need of additional tie or adhesive layers . The excellent clarity of BOPP is retained while the seal initiation temperature is decreased and the sealing properties of the film are increased both in total strength and without having to apply sufficient heating to soften the polypropylene layer. Since the sealing layer polymers of the invention have softening points from about 80 to 100 OC, and melting points between about 100 and 120 "C, the effective heat sealing temperature is lower than that of typical propylene copolymer sealing layers, can be achieved more quickly in processing and results in increased line speeds in manufacturing use.

Films according to the invention particularly include oriented two-layer A/B films having the A sealing layer and a B outer layer of polypropylene or three-layer A/B/A films having two sealing layers A on either side of the core B polypropylene layer. Additional layers or treatments of the films in the B layer are also suitable, such known treatments as metallation or corona discharge treatment with the addition of other barrier layers or tie layers are also well known

in the art to be applicable in any combination for specific articles of commerce.

The A heat sealing layer can be on one side of a multilayered film, and can be used as another core layer, or on both sides to form an additional heat sealing layer. Such composite films will all benefit from the improved adherence of the A and B layers and the compatibility of the combined layered film for orientation, particularly uniaxial orientation and biannual orientation, such as by use of the tenter frame methods of orientation. Additionally, the broad plateau sealing temperatures, i.e., about 110 "C - 140 "C provide a significant advantage for industrial processes where accurate temperature controls are uneconomical are otherwise not available. The heat seals formed by pressing and heating together two such layers can fail largely by peeling within the noted plateau area when subjected to a breaking force of about 0.6-3.0 Ibs. This failure mechanism provides excellent characteristics for peelable seals useful the packaging industry, particularly for flexible packaging. Higher peel strengths (>3.0 lb., e.g., 3.0-6.0 lb.) can be achieved by increasing the thickness of the heat sealing layer exemplified herein, and/or by introducing one or more additional coextruded tie or adhesive layer such as those comprising ethylene or propylene copolymers.

The polymer characterizations presented in this application were conducted under the following conditions and procedures. MI was determined as described in ASTM D 1238. All of Mw, M", and MW/Mn (MWD) were determined by gel permeation chromatography (GPC) using a DRI differential refraction index detector, i.e., a Waters 150C GPC instrument with DRI detectors. CDBI was determined in accordance with the method described in columns 7 and 8 of WO 93/03093. Density was measured in accordance with ASTM D792 for both the polyethylene and polypropylene.

Examples I. TM Long Experiments: Coextruded structures were cast on a laboratory Killion line and then biaxially oriented (6x6) on a TM Long line to prepare a 2-layer A/B film, and a 3-layer ABA film respectively comprising one and two heat sealing layers of 0.2 mil final thickness each and a polypropylene core layer of 0.4 thickness. The ethylene copolymer heat sealing layers were extruded from EXCEEDS 350D60 or 377L60 resins and the polypropylene layer was extruded from PD4252E1, all available from Exxon Chemical Co.

II. Pilot Line Experiments: The films of Tables 1-4 below were prepared on a Black Clawson line and biaxially oriented on a tenter frame as described in the Tables 1-3 below. The film. properties are presented in Table 4.

Table 1 Processing Information for Films made using Black Clawson Line* A/B 10/90 (wt. ratio) A/B/A 10/80/10 (wt. ratio) 350D60 377L60 A 377L60 B PD4252E1 PD4252E1 PD4252E1 Film Gauge 10 | 20 10 | 20 10 (mils) A-Layer: Barrier Screw: B Extruder Screw Speed # 8 8 15 (RPM) Output (lb./hr) 47 47 92 Melt Temp. 550/ 559/ 560/ (°F/°C) Load (Amps) 67 56 107 Volts 25 22 41 Head Press. 1847 1715 2950 (psi/kPa) B-Layer: Metering Screw: A @ Extruder Screw Speed | 151 141 131 (RPM) Output 423 423 368 (Pounds/hr) Melt Temp. (°F/ 586 585 °C) Load (Amps) 128 128 123 Volts 469 431 406 Head Pressure 4100 4266 4186 (PSI) Out ut Pounds/lir Total 470 470 460 Line Speed (FPM? 50 27 43 *Screw speed and Specific output were the same for all films. 3.5 inch 30:1 L/D, 42 inch Wide Die. Air Knife Pinning. Primary Chill Roll was 87 °F ( °C) and Secondary Chill Roll was 75 °F ( °C ) Line speed was adjusted to achieve the desired gauge. All other processing conditions were constant.

Table 2 MD Conditions used for Cast Films* Coextruded A/B A/B/A Fims 10/90 10/80/10 350D60/ 377L60/ A 377L60/ PD4252E1 | PD4252E1 B PD4252E1 Roll Temperature (°F Preheat 270 Slow Draw 265 Fast Draw 265 Annealing 250 Cooling 68 MD Draw 4/5 5 5

* Stretch Gap of 0.032 Inch. Draw Speed was Adjusted to Achieve desired MD Draw Ratio.

Table 3 TD Orienting Conditions used for Cast Films Coextruded A/B A/B/A Films 10/90 | 10/80/10 350D60 PD4252E1 377L60 A 377L60 PD4252E1 l B PD4252E1 Initial Gauge 10 20 10 20 (mils) Oven Temperatures by Oven Section Preheat 315° Stretch 3150 Anneal 300° Line Speed (ft/min.) 60 20 60 50 TD Draw 6 8 6 6 Table 4 Film Properties of Biaxially Oriented Coextruded Film Film Structure A/B A/B/A 10/80/10 10/90 Type Material 350D60/ 377L60/ A 377L60/B PD PD 4252E1 PD 4252E1 4252E1 Initial Gauge (mils) 10 | 20 10 | 10 | 20 10 MD/TD Draw Ratio* Engineering 4:6 5:9 3:8 4:8 5:8 5:6 Gauge Mic (mils) Testing Area 0.28 0.33 0.29 0.25 0.43 0.32 Average Measuretech Profiler Gauge Average mils 0.27 0.33 0.35 0.22 0.39 0.31 Low 0.20 0.20 0.29 0.18 0.34 0.24 High 0.39 0.54 0.52 0.28 0.58 0.43 Dart Drop Method A (g) 228 168 168 181 263 275 (g/mil) 814 509 579 724 612 859 Puncture (Inside)*** Peak Force (Ib.) 15.09 17.13 14.87 12.57 22.83 14.85 Peak Force 53.90 51.90 51.28 50.26 53.09 46.41 (Ib./mil) Break Energy 7.60 5.17 7.07 4.72 7.43 8.54 (in-lb.) Break Energy 27.13 15.67 24.37 18.86 17.28 26.70 (in-lb./mil) Puncture (Outside) *** Peak Force (lb.) 11.34 14.62 9.75 10.04 18.05 15.02 Peak Force 40.51 44.31 33.62 40.15 41.97 46.94 (lb./mil) Break Energy 4.89 4.09 3.67 3.38 5.73 8.88 (in-Ib.) Break Energy 17.48 12.40 12.64 13.50 13.33 27.75 (in- lb./mil) Table 4 Continued Film Structure A/B 10/90 A/B/A 10/80/10 Type Material 350D60/ 377L60/ A 377L60 PD 4252E1 PD 4252E1 B PD 4252E1 Initial Gauge 10 20 10 10 20 10 (mils) Tensile @ Yield (psi) MD 6,882 6,985 6,673 7,233 7,560 5,430 TD 15,111 42,866 24,924 27,599 38,341 11,954 At 200% MD 0 0 11,461 0 0 0 Ultimate Tensile (psi) MD 19,029 19,231 12,937 18,846 23,621 16,046 TD 34,750 65,936 45,231 47,845 66,173 25,988 Elongation (0 Yield (%) MD 4.1 4.3 4.2 4.2 4.5 4.2 TD 5.9 5.6 5.3 5.6 5.9 5.8 Break Elongation (%) MD 133 140 239 155 142 145 TD 26 15 17 19 21 31 Initial Gauge 10 20 10 10 20 10 (mils) 1% Secant (psi) MD 304,830 337,830 318,670 303,170 349,000 278,170 TD 461,330 1,153,670 748,670 788,170 975,330 383,330 Elmendorf Tear * * MD (g) 1 2 2 1 2 2 MD (g/mil) 4 6 6 5 5 6 TD (g) 0 1 0 0 1 1 TD (g/mil) 0 3 0 0 2 3 Shrink (%) MD 57 58 58 64 72 42 TD 79 82 88 86 86 71

Table 4 Continued Film Structure A/B 10/90 A/B/A 10/80/10 Type Material 350D60/ 377L60/ A 377L60/ PD 4252El PD 4252E1 B PD 4252E1 Initial Gauge 10 20 10 10 20 10 (mils) Haze (°/O) 0.63 0.77 1.07 0.97 0.97 1.20 * Gloss (45 ) 93 90 88 87 88 92 * COF (kf) (I/I) No Sample .49 .46 .43 .39 > 1.0 (I/O) .51 .43 .40 .40 (O/O) .52 .53 .49 .44 WVTR(gm x 0.34 0.35 mil/100" sq/day) * Engineering draw ratios were determined during the trial. The Actual draw ratios were determined from the films produced.

** Tear values were based on using a 200 gram pendulum. ASTM states that tear values are to be obtained from readings between 20 - 60% of pendulum weight. The tear values were so low, this was impossible.

***Used 2 slip sheets of HDPE.

III. The films of the following examples 1 - 4 were prepared by coextruding and casting a 2-layer tape, and then biaxially orienting. The casting was done on a Black- Clawson line and the orientation on a pilot tenter line. The resulting films are described in Table 5 and the conditions used to orient the films on the pilot tenter line are summarized in Table 6.

The properties of the coextruded film were similar to those of biaxially oriented polypropylene film without the heat seal layer. For example, the products retained excellent optics (haze and gloss), Elmendorf tear was essentially equivalent (.10 g/mil.). The ethylene copolymer heat seal layer was just 0.03 to 0.12 mil (0.7-3.0 ,u), but microscopic examination showed that the heat seal layer drew uniformly with the polypropylene. Hot tack and sealing performance were measured along both machine direction (MD) and transverse direction (TD), see Figure 1. Though highly oriented, the seals introduced exhibited excellent appearance without observable shrinkage. For these examples the seal failure occurred at moderate force levels fully acceptable in industry, and the failure mechanism was largely by peeling rather than by tearing or breaking. The mode of failure at the exemplified moderate force levels illustrate utility for peelable seals desired for many packaging applications. The hot tack measurement, also in Figure 1, illustrate suitable values for the heat sealing at between 110 - 120 °C, a significant advantage over those temperatures required for heat sealing layers comprising polypropylene copolymers.

Table 5 Examples of A/B Coextruded Structures Biaxially Oriented on Pilot Tenter Line Coextruded m-LLDPE Polypropylene Orientation, Final Film Sample # TDxMD Thickness, mil 1 10% 350D60 90% PD4252E1 5x9 0.33 2 10% 377L60 90% PD4252E1 5x8 0.39 3 10% 350D60 90% PD4252E1 4x6 0.27 4 10% 377L60 90% PD4252E1 3x8 0.35 Table 6 b. MD Orientation Coextruded Eng'g. Input Film Pre-heat Draw Anneal Chill Sample # Orienta-tion Speed, Rolls, Rolls, Rolls, Rolls, ft/s (m/s) CC OC OC °C 1 5 10( ) 132 126 120 21 2 5 10( ) 132 126 120 21 3 4 10() 132 126 120 21 4 3 10( ) 132 126 120 21 b. TD Orientation Co extruded Eng g. Pre-heat, Stretch, Anneal, Sample # Orientation °C °C °C 1 9x 132 160 149 2 8x 132 160 149 3 6x 132 157 149 4 8x 132 157 | 149