Background of the Invention Polyethylene has traditionally been used as a layer in polyolefin films and packaging because of its desirable properties such as moisture impermeability good sealing behavior, good optical properties and good organoleptics. Typically polyethylene has been coextruded, laminated or otherwise bonded to other polyolefins which have better strength than polyethylene, yet do not seal as well as polyethylene. For example, in a typical multilayer film, a polypropylene layer, especially a mono or biaxially oriented polypropylene (OPP) layer, provides a high clarity, high melting, high barrier properties, combined with high stiffness, while a polyethylene layer will provide extra body to the film and will allow a low sealing temperature, meaning higher packaging speeds. However, polypropylene (PP) and polyethylene (PE) have very limited compatibility and direct sealing of polyethylene onto polypropylene film is not commonly done. When a layer of PE is combined with a layer of PP, extra primer may be needed. For example, extra primer is used when polyethylene, such as low density polyethylene, is coated onto polypropylene films. In addition tie layers may also be necessary.

Coextrudable tie layers such as ethylene vinyl acetate copolymers, typically having more that 8 weight % vinyl acetate, have been extruded between PP and PE to enhance adhesion between the PE and the PP. Another solution to the compatibility problem has been to blend polypropylene into the polyethylene.

This however has the disadvantage or creating layers that have greater haze and are thus undesirable in the industry.

Therefore there is a need in the art to provide a means to provide a polyethylene polypropylene blend for film layers that does not have haze, yet retains good mechanical properties such impact strength.

WO 94/26816 discloses blends of metallocene polyethylene and high molecular weight high density polyethylene for use in films.

Summary of the Invention This invention relates to a film comprising a blend of: (i) a homopolymer of ethylene having an Mw/Mn of 3 or less or a copolymer of ethylene and up to 50 weight % of a C3 to C20 olefin, wherein the copolymer has a CDBI of 50 % or more, preferably 60% or more; (ii) a homopolymer of propylene or a copolymer of propylene and up to 50 weight% of a comonomer, preferably copolymerized with ethylene and/or a C4 to C20 olefin; and (iii) a polymer produced in a high pressure process using a free radical initiator (High Pressure Polymer).

This invention also relates to films as described above where one or more layers are oriented in one or more directions to the same or different extents.

Detailed Description of the Invention.

In a preferred embodiment, this invention relates to a film comprising a blend of: (i) a homopolymer of ethylene having an Mw/Mn of 3 or less, preferably between 1 and 2.5 or a copolymer of ethylene and up to 50 weight %, preferably 1 to 35 weight %, preferably 1-20 weight % of one or more C3 to C20 olefins, (based upon the weight of the copolymer) having an Mw/Mn of 6 or less, preferably 3 or less, even more preferably between 1 and 2.5, wherein the polymer or copolymer preferably has: a) a density of 0.86 g/cm3 to 0.96 g/cm3, preferably 0.88 to 0.94 g/cm3, more preferably between 0.88 g/cm3 and 0.935 g/ cm3, more preferably between 0.88 g/cm3 and 0.95 g/ cm3 more preferably between 0.915 g/cm3 and 0.935 g/ cm3; and b) a CDBI of 50 % or more, preferably above 60%; (ii) a homopolymer of propylene or a copolymer of propylene and up to 50 weight %, preferably 1 to 35 weight %, even more preferably 1 to 6 weight % of ethylene and/or a C4 to C20 olefin; and (iii) polymer produced in a high pressure process using a free radical initiator (High Pressure Polymer).

Composition Distribution Breadth Index (CDBI) is a measure of the composition distribution of monomer within the polymer chains and is measured by the procedure described in PCT publication WO 93/03093, published February 18, 1993 including that fractions having a weight average molecular weight (Mw) below 15,000 are

ignored when determining CDBI. For purposes of this invention a homopolymer is defined to have a CDBI of 100%.

The C3 to C20 and C4 to C20 olefin comonomers for the polyethylene or polypropylene copolymers described above may be any polymerizable olefin monomer and are preferably a linear, branched or cyclic olefin, even more preferably an a-olefin.

Examples of suitable olefins include propylene, butene, isobutylene, pentene, isopentene, cyclopentene, hexene, isohexene, cyclohexene, heptene, isoheptene, cycloheptene, octene, isooctene, cyclooctene, nonene, cyclononene, decene, isodecene, dodecene, isodecene, 4-methyl-pentene- 1, 3 -methyl-pentene- 1, 3,5,5-trimethyl hexene- 1. Suitable comonomers also include dienes, trienes, and styrenic monomers.

Preferred examples include styrene, a-methyl styrene, para-alkyl styrene (such as para- methyl styrene), hexadiene, norbornene, vinyl norbornene, ethylidene norbornene, butadiene, isoprene, heptadiene, octadiene, and cyclopentadiene.

Preferred comonomers for the copolymer of ethylene are propylene, butene, hexene and/or octene.

The polyethylene or polypropylene copolymers described above may also contain termonomers and tetramonomers which may be one or more of the C3 to C20 olefins described above, any C4 to C30 linear, cyclic or branched dienes or trienes and any styrenic monomers such as styrene, a-methyl styrene, or para-methyl styrene.

Preferred examples include butadiene, pentadiene, cyclopentadiene, hexadiene, cyclohexadiene, heptadiene, octadiene, nonadiene, norbornene, vinyl norbornene, ethylidene norbornene, isoprene and heptadiene.

The polyethylene copolymers described above preferably have a composition distribution breadth index (CDBI) of 50 % or more, preferably above 60%, even more preferably above 70%. In one embodiment the CDBI is above 80%, even more preferably above 90%, even more preferably above 95%. In another particularly preferred embodiment, the polyethylene copolymer has a CDBI between 60 and 85 %, even more preferably between 65 and 85 %.

In a particularly preferred embodiment the ethylene homopolymer or copolymer has a CDBI of 65 to 85 %, a density of 0.915 to 0.96 g/cm3 and a Mw/Mn between 1 and 2.5.

In another preferred embodiment the ethylene homopolymer or copolymer has a density of 0.86 to 0.925 g/cm3 and a CDBI of over 80%, preferably between 80 and 99%.

In another preferred embodiment the blend comprises a homopolymer of ethylene having an Mw/Mn of 3 or less, preferably between 2.5 and 1.

In general, the polyethylene homopolymers and copolymers described above are metallocene polyethylenes (mPE's). The mPE homopolymers or copolymers are typically produced using mono- or bis-cyclopentadienyl transition metal catalysts in combination with an activator such as alumoxane and/or a non-coordinating anion in solution, slurry, high pressure or gas phase. The catalyst and activator may be supported or unsupported and the cyclopentadienyl rings by may substituted or unsubstituted. Several commercial products produced with such catalyst/activator combinations are commercially available from Exxon Chemical Company in Baytown Texas under the tradenames EXCEEDTM and EXACTTM.

For more information on the methods and catalysts/activators to produce such mPE homopolymers and copolymers see WO 94/26816; WO 94/03506; EPA 277,003; EPA 277,004; US 5,153,157; US 5,198,401; US 5,240,894; US 5,017,714; CA 1,268,753; US 5,324,800; EPA 129,368; US 5,264,405; EPA 520,732; WO 92 00333; US 5,096,867; US 5,507,475; EPA 426 637; EPA 573 403; EPA 520 732; EPA 495 375; EPA 500 944; EPA 570 982; W091/09882; W094/03506 and US 5,055,438.

The polypropylene homopolymer or copolymer preferably has an MFR (melt flow rate) of 1 to 20 as measured according to ASTM D 1238 (230 "C, 2.16 kg). In another embodiment the polypropylene homopolymer or copolymer preferably has a CDBI of 50 % or more, preferably above 60%, even more preferably above 70 %. Polypropylenes having a CDBI above 60% are available from Exxon Chemical Company in Baytown, Texas under the tradename ACHIEVETM.

In another embodiment the polypropylene homopolymer or copolymer can be blended with any of the other propylene homopolymers or copolmyers described above. Likewise, The polyethylene homopolymers or copolymers described above for use in the blend may be used alone, may be blended with any of the other polyethylene homopolymers or copolymers described above.

In a preferred embodiment the polymer produced in a high pressure process using a free radical initiator (High Pressure Polymer) is a polymer comprising one or more of C2 to C20 olefins and polar monomers. Preferred C2 to C20 olefins include, but are not limited to, ethylene, propylene, butene, pentene, hexene, octene, 3 -methyl-pentene- 1, 4-methyl-pentene- 1, cyclopentene, cyclohexene, hexadiene, norbornene, isobutene, norbornadiene, pentadiene and 3,5,5-trimethyl hexene - 1. Preferred polar monomers include, but are not limited to, acetates (such as vinyl acetate), acrylics (such as acrylic acid, methacrylic acid), acrylates (such as methacrylate, butylacrylate, methylmethacrylate, hydroxyethylmethylacrylate). Polar modifiers can also be used in high pressure free radical process such as alcohols (such as isopropanol ) or aldehydes (such as acetaldehyde). Other modifiers known in the art can also be used.

In a preferred embodiment the High Pressure Polymer is low density polyethylene (density 0.910 to less than 0.940 g/cm3 , preferably 0.915 to less than 0.935 g/cm3 Even more preferably 0.920 to less than 0.935 g/cm3), a copolymer of ethylene and vinyl acetate, a copolymer of ethylene and methyl acrylate, a copolymer of acrylic acid, a copolymer of methylmethacrylate or any other polymers polymerizable by a high- pressure free radical process. The LDPE preferably has up to 20 weight % of comonomer. The EVA and acrylate copolymers preferably has 20 weight % of the polar monomer or less, preferably less than 10 weight %, even more preferably less than 6 weight %. In a preferred embodiment the Melt Index of the LDPE is between 0.2 and 50 g/10 min, preferably between 0.5 and 10 g/10 min, even more preferably between 0.6 and 5 g/10 min, even more preferably between 0.6 and 2.5 g/10 min.

Many such High Pressure Polymers are commercially available. For example, LDPE made in a high pressure process is available from Exxon Chemical Company under the trade name ESCORENE TM EVA made in a high pressure process is available from Exxon Chemical Company under the trade name ESCORENETM.

Polymethylmethacrylate made in a high pressure process is available from Exxon Chemical Company under the trade name ESCORENETM.

In a preferred embodiment the polyethylene (component (i)) is present in the blend at from 1 to 99 weight %, based upon the weight of the polymers in the blend, preferably the polyethylene is present at 10 to 90 weight %, even more

preferably at least 20 to 80 weight %, even more preferably at least 30 to 70 weight %, even more preferably at least 40 to 70 weight %.

In a preferred embodiment the polypropylene (component (ii)) is present in the blend at from 1 to 99 weight %, based upon the weight of the polymers in the blend, preferably the polypropylene is present at 10 to 90 weight %, even more preferably at least 20 to 80 weight %, even more preferably at least 30 to 70 weight %, even more preferably at least 40 to 70 weight %.

In a preferred embodiment the High Pressure Polymer (component (iii)) is present in the blend at from 1 to 50 weight %, based upon the weight of the polymers in the blend, preferably at 2 to 30 weight %, even more preferably at least 5 to 20 weight %.

The blends described above can also further include other polymers such as polybutene, high density polyethylene (density 0.945 to less than 0.98 g/cm3) linear low density polyethylene, medium density polyethylene (density 0.935 to less than 0.945 g/cm3), polyvinylchloride, isotactic polybutene, ABS resins, elastomers such as ethylene-propylene rubber (EPR), vulcanized EPR, EPDM, block copolymer elastomers such as SBS, nylons, polycarbonates, PET resins, crosslinked polyethylene, copolymers of ethylene and vinyl alcohol (EVOH), polymers of aromatic monomers such as polystyrene, poly-l esters, graft copolymers generally, polyacrylonitrile homopolymer or copolymers, thermoplastic polyamides, polyacetal, polyvinylidine fluoride and other fluorinated elastomers, polyethylene glycols and polyisobutylene.

The blends described above may be produced by mixing the three (or more) polymers together, by connecting reactors together in series to make reactor blends or by using more than one catalyst in the same reactor to produce multiple species of polymer. The polymers can be mixed together prior to being put into an extruder or may be mixed or compounded in an extruder.

The blends described above are typically formed into monolayer or multilayer films. These films may be formed by any of the conventional techniques known in the art including extrusion, co-extrusion, extrusion coating, lamination, blowing and casting. The film may be obtained by the flat film or tubular process which

may be followed by orientation in an uniaxial direction or in two mutually perpendicular directions in the plane of the film.

In a preferred embodiment a film of the blend is used as a sealing layer. In another preferred embodiment a film of the blend is used as that functional layer, that is to say it is used to provide mechanical strength and/or stiffness. Films of the blends described herein have excellent stiffness and mechanical strength as compared to films of the individual components.

This invention also relates to films as described above where one or more of the layers are oriented in the transverse and/or longitudinal directions to the same or different extents. This orientation may occur before or after the individual layers are brought together. For example the blend layer can be extrusion coated or laminated onto another layer or the layers can be coextruded together into a film then oriented.

Typically the films are oriented in the Machine Direction (MD) at a ratio of up to 15, preferably between 5 and 7, and in the Transverse Direction (TD) at a ratio of up to 15 preferably 7 to 9. However in another embodiment the film is oriented to the same extent in both the MD and TD directions. Orientation to the same extent in both directions will generally produce roughly equal mechanical properties.

In another embodiment the blend layer is combined with one or more other layers. The other layer(s) may be any layer typically included in multilayer film structures. For example the other layer or layers may be: 1. Polyolefins Preferred polyolefins include homopolymers or copolymers of C2 to C40 olefins, preferably C2 to C20 olefins, preferably a copolymer of an a-olefin and another olefin or a-olefin (ethylene is defined to be an a-olefin for purposes of this invention).

Preferably homopolyethylene, homopolypropylene, propylene copolymerized with ethylene and or butene, ethylene copolymerized with one or more of propylene, butene or hexene, and optional dienes. Preferred examples include thermoplastic polymers such as ultra low density polyethylene, very low density polyethylene, linear low density polyethylene, low density polyethylene, medium density polyethylene, high density polyethylene, polypropylene, isotactic polypropylene, highly isotactic polypropylene, syndiotactic polypropylene, random copolymer of propylene and ethylene and/or butene and/or hexene, elastomers such as ethylene propylene rubber, ethylene propylene diene monomer rubber, neoprene, and blends of thermoplastic

polymers and elastomers, such as for example, thermoplastic elastomers and rubber toughened plastics.

2. Polar polymers Preferred polar polymers include homopolymers and copolymers of esters, amides, actates, anhydrides, copolymers of a C2 to C20 olefin, such as ethylene and/or propylene and/or butene with one or more polar monomers such as acetates, anhydrides, esters, alcohol, and or acrylics. Preferred examples include polyesters, polyamides, ethylene vinyl acetate copolymers, and polyvinyl chloride.

3. Cationic polymers Preferred cationic polymers include polymers or copolymers of geminally disubstituted olefins, alpha-heteroatom olefins and/or styrenic monomers. Preferred geminally di sub stituted olefins include isobutylene, isopentene, isoheptene, isohexane, isooctene, isodecene, and isododecene. Preferred alpha-heteroatom olefins include vinyl ether and vinyl carbazole, preferred styrenic monomers include styrene, alkyl styrene, para-alkyl styrene, alpha-methyl styrene, chloro-styrene, and bromo-para-methyl styrene.

Preferred examples of cationic polymers include butyl rubber, isobutylene copolymerized with para methyl styrene, polystyrene, and poly-a-methyl styrene.

4. Miscellaneous Other preferred layers can be paper, wood, cardboard, metal, metal foils (such as aluminum foil and tin foil), metallized surfaces, glass (including silicon oxide (SiOx)coatings applied by evaporating silicon oxide onto a film surface), fabric, spunbonded fibers, and non-wovens (particularly polypropylene spun bonded fibers or non-wovens), and substrates coated with inks, dyes, pigments, PVDC and the like.

Further any of the above layers may be oriented before or after being combined with the blend layers.

A particularly preferred embodiment includes an ABC structure film where the A layer comprises mPE or a blend comprising mPE and the B layer is a blend according to this invention and the C layer is a sealing layer for example a random copolymer of propylene and up to 20 weight % of ethylene, preferably 3 to 6 weight % ethylene, even more preferably 3.5 to 5.5 weight % ethylene, or a terpolymer of propylene, ethylene and butene.

In a preferred embodiment up to 100 pm thick monolayer films of the blend described above are characterized by a haze, as measured by ASTM 1003 condition A of 16% or less, more preferably 14% or less, more preferably 12 % or less, more preferably 10% or less, even more preferably 5% or less.

The films described herein may vary in thickness depending on the intended application, however films of a thickness from 1 to 350 ,um are usually suitable. Films intended for packaging are usually from 10 to 120 ,um thick. The thickness of the sealing layer is typically 0.2 to 50 llm. There may be a sealing layer on both the inner and outer surfaces of the film or the sealing layer may be present on only the inner or the outer surface.

Additives such as antiblock, antioxidants, pigments, fillers, processing aids, UV stabilizers, neutralizers, lubricants, surfactants and/or nucleating agents may also be present in one or more than one layer in the films. Preferred additives include silicon dioxide, titanium dioxide, polydimethylsiloxane, talc, dyes, wax, calcium stearate, carbon black, low molecular weight resins, tackifiers, and glass beads.

In another embodiment the layers may be modified by corona treatment, electron beam irradiation, gamma irradiation, or microwave. In particular the corona treatment will produce a significant difference in the coefficient of friction of the two surface layers as described in US Patent Application Number USSN 08/905,211, which is incorporated by reference herein.

In a particularly preferred embodiment film of the blends described herein are cast, blown or co-extruded and the polyethylene is present at 50 to 80 weight %, the polypropylene is present at 10 to 45 weight% and polymer produced in high pressure process using a free radical initiator is LDPE and is present at 2 to 10 weight%, based upon the weight of the blend.

In another embodiment films of the blends described herein are laminated to a substrate. Preferred substrates include polypropylene, polyamide, polyester, polyethylene, or metallized substrates.

The films described herein may also comprise from 5 to 60 weight %, based upon the weight of the polymer and the resin, of a hydrocarbon resin. The resin preferably has a softening point above 100 "C, even more preferably from 130 to 180 OC, even more

preferably between 140 and 180 "C.. Preferred hydrocarbon resins include those described in EPA 288 227 and EPA 247 898. These films comprising a hydrocarbon resin may be oriented in uniaxial or biaxial directions to the same or different degrees.

In a preferred embodiment this invention also relates to a method to produce a film characterized by good haze values comprising: i) selecting a first polymer having a CDBI of 50 % or more comprising homopolyethylene or a copolymer of ethylene and up to 50 weight % of a C3 to C20 olefin, ii) selecting a second polymer comprising homopolypropylene or a copolymer of propylene and up to 50 weight % of ethylene or a C4 to C20 olefin, iii) selecting a third polymer comprising one or more polymers produced in a high pressure process using a free radical initiator, and iv) combing the first, second and third polymers and forming them into a film.

In a preferred embodiment this invention also relates to a method of packaging an article comprising: i) selecting a first polymer having a CDBI of 50 % or more comprising homopolyethylene or a copolymer of ethylene and up to 50 weight % of a C3 to C20 olefin, ii) selecting a second polymer comprising homopolypropylene or a copolymer of propylene and up to 50 weight % of ethylene or a C4 to C20 olefin, iii) selecting optional polymers for core layers, iv) combing the first polymer and second polymer so that the first polymer forms all or part of a film surface layer and the second polymer forms all or part of a film surface layer and, if present, the optional polymers for core layers are formed into film layers in between the first surface layer and the second surface layer, v) enclosing an article in the film, and vi) heat sealing the enclosed article such that at least one seal is formed by heat sealing the first surface layer to the second surface layer.

In a preferred embodiment the films formed from the blends described herein when formed into a film 50 ,um thick film have an average secant modulus greater than 350 MPa and a dart drop impact strength greater than 5 g/micron.

Additionally the film produced herein can be laminated with another film such as polyethylene, polypropylene, polyester, polyamides and the like which may or may not be oriented. These combinations are particularly suitable for high quality packaging performance such as modified atmosphere packaging or controlled atmosphere packaging.

The films produced herein may be used for typical packaging applications, form fill and seal applications, cling films, stretch films, frozen film, heavy duty packaging film, can liners and other similar applications.

Examples MATERIALS: ECD 109 is an ethylene hexene copolymer produced in the gas phase having about 4.1 weight % hexene, a melt index of about 0.8 g/l Omin, a CDBI of about 59, an Mw/Mn of about 2.3 and a density of about 0.928 g/cm3, sold under the tradename EXCEEDTM by Exxon Chemical Company in Baytown, Texas.

ECD 103 is an ethylene hexene copolymer produced in the gas phase having approximately 7.6 weight % hexene, a melt index of about 1 g/lOmin, a Mw/Mn of about 2.3, a CDBI of about 67% and a density of about 0.917 g/cm3, sold under the tradename EXCEEDTM by Exxon Chemical Company in Baytown, Texas.

ECD 202 is an ethylene hexene copolymer produced in the gas phase having approximately 7.6 weight % hexene, a melt index of about 2.4 g/lOmin, a Mw/Mn of about 2.3, a CDBI of about 67% and a density of about 0.917 g/cm3, sold under the tradename EXCEEDTM by Exxon Chemical Company in Baytown, Texas.

PP-1 is a homopolymer of propylene having a Melt Index of about 2.9 g/10 min and a broad molecular weight distribution (Mw/Mn) sold under the trade name of ESCORENE PP 4352F1 by Exxon Chemical Company.

LD-2 is a low density polyethylene having a density of about 0.922 g/cm3 and a melt index of about 0.75 g/ 10 min commercially available under the trade name ESCORENE LD 150 BW from Exxon Chemical Belgium.

LL-3 is ESCORENE LLN 1201 XV a ethylene butene copolymer having a Melt Index of about 0.7 g/10 min, a density of 0.925 g/cm3 and produced in a gas phase

using a Ziegler Natta catalyst and is commercially available from Exxon Chemical Belgium.

TESTING METHODS: Composition Distribution Breadth Index (CDBI) is measured by the procedure described in PCT publication WO 93/03093, published February 18, 1993.

Fractions having a molecular weight (Mw) less than 15,000 were ignored.

Melt Index (MI) was measured according to ASTM D 1238. (190 "C, 2.16 kg) Density was measured according to ASTM D1505, where the sample was prepared according to ASTM D 1928/.

Mw and Mn were measured by GPC (Gel Permeation Chromatography) on a Waters 150 gel permeation chromatograph equipped with a differential refractive index (DRI) detector and a Chromatix KMX-6 on line light scattering photometer. The system was used at 135 "C with 1,2,4-trichlorobenzene as the mobile phase. Shodex (Showa Denko America, Inc) polystyrene gel columns 802, 803, 804 and 805 were used. This technique is discussed in "Liquid Chromatography of Polymers and Related Materials III", J. Cazes editor, Marcel Dekker. 1981, p. 207, which is incorporated herein by reference. No corrections for column spreading were employed; however, data on generally accepted standards, e.g. National Bureau of Standards Polyethylene 1484 and anionically produced hydrogenated polyisoprenes (an alternating ethylene-propylene copolymer) demonstrated that such corrections on Mw/Mn (= MWD) were less than 0.05 units. Mw/Mn was calculated from elution times. The numerical analyses were performed using the commercially available Beckman/CIS customized LALLS software in conjunction with the standard Gel Permeation package. Calculations involved in the characterization of polymers by 13CNMR follow the work of F. A.

Bovey in "Polymer Conformation and Configuration" Academic Press, New York, 1969.

Dyna Impact Strength properties (Max Force, Damaging Energy, Total Energy, Damaging Travel, Total Travel) were measured according to DIN 53373.

Tensile properties (Tensile at yield, elongation at yield, tensile at break, elongation at break, and Secant Modulus) were measured according to ASTM D 882. Average secant modulus is the mathematical average of the MD Secant Modulus and the TD Secant Modulus.

Elmendorf Tear Strength (N/llm) was measured according to ASTM 1922.

Gloss was measured according to ASTM D2457/60".

Dart Drop was measured acording to ASTM D 1709.

Heat seal testing procedure: Seal were made on a Topwave sealing machine. The film was folded between TEFLONTM film and inserted between the sealing bars. At various the sealing bars were closed with a pressure of 0.5 MPa for 0.5 seconds. The film was removed from the Top wave machine and conditioned for a minimum of 12 hours at 23 "C 13 3 "C and 50% humidity 15% humidity.

Seal Strength was tested according to the following procedure. After conditioning for a minimum of 12 hours at 23 "C + 3 °C and 50% humidity 15% humidity, the seal strength of 15mm wide sample was measured in a Zwick tensile instrument under the following conditions: speed-100 mm/min, load cell-200N, and clamp distance-50 mm.

The film was placed between the clamps and the clamps were moved apart at a speed of 100mm/min. During the rest the force (N) was recorded as a function of elongation (%). Four test specimens were measured and the average seal strength curve was recorded. The seal strength was the force at which the test specimen failed.

Example 1 Eleven monolayer films 50 p thick of various blends were blown on an Alpine extruder under the conditions in Table 1, Table 3 and Table 6. The individual polymers were fed into the same extruder hopper at the same time. The blend components and test data on the resulting films are reported in Tables 2, 4, 5 and 7.

Table 1 ECD109 95w% ECD109 90w% ECD109 80w% ECD109 80w% ECD109 75w% PP-I 5w% PP-1 10w% CP-I 20w% P-i 15w% PP-I 20w% LD-2 5w% LD-2 5w% Barrell temp settings (°C) zone 1 190 190 190 190 190 zone 2 200 200 200 199 200 zone 3 220 220 220 220 220 zone 4 220 220 220 220 220 zone 6 230 230 225 235 230 one 7 230 230 230 224 230 zone 8 230 230 222 235 230 zone 9 240 240 239 241 240 zone 10 240 240 240 240 240 one 11 240 240 240 240 240 one 12 240 240 240 240 240 diegap (mm) 1.5 1.5 1.5 1.5 1.5 cooling air temp 16 17 16 16 (°C) Die Diam (mm) 200 200 200 200 200 Melt temp. (°C) T1 243 240 233 233 T2 242 237 234 232 T3 245 239 237 235 T4 242 237 234 232 T5 245 242 232 233 Tmelt 237 243 235 237 Melt pressure (bar) P1 545 526 464 P2 518 491 444 P3 501 473 432 P4 516 500 480 P5 562 545 524 P6 388 365 339 screw speed 59 rpm 60 rpm 62 rpm 62 rpm Output (kg/hr) 140 140 140 140 Lay-flat (mm) 900 900 900 900 Frost line (mm) 700 700 700 700 keoff(m/min) 28 28 28 28 Blow up ratio 2.9 2.9 2.9 2.9 w% = weight percent based upon the weight of the polymers. Table 2 ECD109 ECD109 ECD109 ECD109 ECD109 95w% 90w% 80w% 80w% 75w% PP-1 PP-1 PP-1 PP-1 PP-1 5w% 10w% 20w% 15w% 20w% LD- LD- 2 5w% 2 5w% Haze (%) 19 18 22 9.5 9.7 Gloss (%) 7.8 7.1 5.4 10.7 9.9 Max Force N/µ 1.3 1.3 1.3 1.2 1.2 Damaging Energy mJ/µ 20 17 12 13 11 Total Energy mJ/µ 22 20 14 16 12 Damaging Travel (mm) 24 20 16 18 15 Total Travel (mm) 25 28 18 23 17 Tensile @ Yield (Mpa) MD 14.1 16.2 18.7 16.1 18.5 Elong @ Yield (%) MD 16.1 13.1 12 16.8 14.1 Tensile @ Break (MPa) MD 61 64 62 61 60 long @ Break (%) MD 682 670 649 678 674 Energy MD (mJ/mm3) 168 177 176 180 190 Tensile @ Yield (Mpa) TD 14.6 15.7 17.8 16.4 18.1 Elong @ Yield (%) TD 12.5 11.2 10.0 10.0 9.9 Tensile @ Break (MPa) TD 56 57 50 54 51 Elong @ Break (%) TD 724 735 698 719 706 Energy TD (mJ/mm3) 169 177 160 167 164 Secant Modulus (MPa) MD 335 444 548 442 539 Secant Modulus (MPa) TD 369 440 540 478 557 Average Secant Modulus (MPa) 352 442 544 460 548 Elmendorf tear (g/µ) MD 8.9 7.8 5.6 7.1 4.3 Elmendorf Tear (g/li) TD 15 13 10 16 15 TD = transverse direction.

MD= machine direction.

Table 3 ECD103 ECD103 95w% ECD103 80w% ECD103 75w% 100 w% LD-150 5w% PP-1 15w% PP-1 20w% LD-2 5w% LD-2 5w% Barrell temp settings (°C) zone 1 170 190 190 191 zone 2 175 200 200 201 zone 3 175 220 220 219 zone 4 175 220 220 219 zone 6 185 230 225 224 one7 185 230 230 230 zone 8 185 230 222 228 zone 9 190 240 239 240 zone 10 190 240 240 240 one 11 200 240 240 240 one 12 200 240 240 240 diegap (mm) 1.5 1.5 1.5 1.5 cooling air temp (°C) 17 16 16 17 Die Diam (mm) 200 200 200 200 Melt temp. (°C) 1 214 243 231 230 T2 227 248 235 234 3 233 252 238 236 T4 226 248 234 233 5 211 242 231 230 melt 206 243 230 231 Melt pressure (bar) P1 440 234 276 245 P2 437 278 301 275 P3 456 316 370 305 P4 517 400 397 378 P5 600 465 446 425 P6 414 326 304 288 screw speed 52 rpm 68 rpm 67 rpm 68 rpm Output (kg/hr) 133 138 139 141 Lay-flat (mm) 930 900 900 900 Frost line (mm) 600 700 700 700 take off(m/min) 26 28 28 28 blow up ratio 3.0 - 2.9 2.9 2.9 weight percent based upon the weight of the polymers. Table 4 ECD103 ECD103 ECD103 ECD103 100% 95w% 80w% 75wO/o LD 150 PP-1 PP-1 5 woo 15w% 20w% LD-2 LD-2 5WO/o 5w% Haze (%) 25 5.4 3.7 4.7 Gloss (%) 5.8 12.9 13.0 12.0 Max Force N/µ >1.7 >1.7 1.4 1.4 Damaging Energy mJ/y >47 >47 24 22 Total Energy mJ/µ >47 >47 26 25 Damaging Travel (mm) >44 >44 26 24 Total Travel (mm) >44 >44 28 27 Tensile @ Yield (Mpa) MD 10.0 10.2 15.2 15.9 Elong @ Yield (%) MD 13.9 13.6 16 15.4 Tensile @ Break (MPa) MD 69 62 65 64 Elong @ Break (%) MD 613 642 637 653 Energy MD (MJ/mm3) 143 148 173 178 Tensile @ Yield (Mpa) TD 9.7 10.5 13.6 14.3 Elong @ Yield (%) TD 20.0 16.6 12.0 12.0 Tensile @ Break (MPa) TD 60 59 56 56 Elong @ Break (%) TD 661 671 692 688 Energy TD (mJ/mm3) 140 144 157 158 Secant Modulus (MPa) MD 183 202 395 443 Secant Modulus (MPa) TD 189 | 221 361 394 Average Secant Modulus (MPa) 186 212 378 419 Elmendorf tear (g/µ) MD 12 12 13 12 Elmendorf Tear (g/µ) TD 14 17 16 16 Table 5 Heat Seal Strength (N/15mm) of 50 micron films Heat Seal Temp ECD 103 95 w% ECD 103 75 w% ECD 109 75 w% LD-2 5 w% PP-1 20 w% PP-1 20 w% LD-2 5w% LD-2 5w% 110 0C 6.0 0.7 1200C 9.5 11.5 1.2 1300C 10.0 12.3 13.1 140°C 9.2 11.3 13.4 1500C 11.1 11.0 13.1 160°C 12.0 10.7 12.5 180°C 11.7 11.0 12.6 Table 6 LL-3 80w% ECD202 80w% LD-15020w% PP-1 15w% LD-2 5w% Barrell temp settings (°C) zone 1 170 170 zone 2 175 175 zone 3 175 180 zone 4 175 190 zone 6 185 190 zone 7 185 190 zone 8 190 195 zone 9 190 215 zone 10 190 215 zone 11 200 225 zone 12 200 225 diegap (mm) 1.5 1.5 cooling air temp (°C) 15 15 Die Diam (mm) 200 200 Melt temp. (°C) T1 197 197 T2 205 205 3 209 219 T4 204 204 T5 196 196 Tmelt 196 196 Melt pressure (bar) P1 563 201 P2 620 207 P3 595 210 P4 556 207 P5 552 200 P6 412 200 screw speed 41 rpm 44 rpm Output (kg/hr) 100 95 Lay-flat (mm) 785 785 Frost line (mm) 500 500 take off(m/min) 50 62 blow up ratio 2.5 2.5 w% = weight percent based upon the weight of the polymers. Table 7 LL-3 80A ECD202 80w% LD-150 20w% PP-1 15w% LD-2 5w% Haze (%) 2.7 3.8 Gloss (%) 13.6 12.2 Tensile @ Break (MPa) MD 68.1 98.1 Elong @ Break (%) MD 474 552 Tensile @ Break (MPa) TD 35.4 49.4 Elong @ Break (%) TD 815 695 Secant Modulus (MPa) MD 407 337 Secant Modulus (MPa) TD 502 316 Dart Drop (g/pm) 3.1 8.1 Elmendorf tear (g/µ) MD 0.3 4.0 Elmendorf Tear (g/µ) TD 13.7 15.7 All documents described herein are incorporated by reference herein, including any priority documents and/or testing procedures. As is apparent from the foregoing general description and the specific embodiments, while forms of the invention have been illustrated and described, various modifications can be made without departing from the spirit and scope of the invention. Accordingly, it is not intended that the invention be limited thereby.