Polyolefin stretch film

Abstract: A polyolefin blown or slot cast multilayer stretch film useful as a trayed overwrap e.g. for fresh red meat includes at least three layers in the multilayer embodiment each of which contains an ethylene alpha-olefin copolymer having a density below 0.915 g/cm 3 and having a melting point of at least 90°C with at least one outer layer and preferably also the first outer layer or the core layer having a second ethylene alpha olefin copolymer having a melting point less than 80°C blended therein.

Description: Background of the Invention The present invention relates to polyolefin stretch films. In particular, the present invention relates to flexible films which may be used as a substitute for poly(vinyl chloride) (PVC) flexible films. Poly(vinyl chloride) is a thermoplastic polymer which has been used extensively for many years to form articles, containers and films for industrial, commercial and consumer applications. Plasticized poly(vinyl chloride) has been used to make flexible films (hereinafter "PVC film") which have enjoyed great commercial success in both nonfood and food contact applications. In particular, PVC film is in widespread use as a food overwrap, e.g. for fresh fruits and vegetables, cheese, sandwiches, food trays and especially for fresh red meats, processed meats and poultry. PVC film is also used to package frozen foods, baked goods, fresh fish, as institutional packaging for overwrapping both food and such nonfood items as glassware and eating utensils, and as pharmaceutical packaging, pallet wrapping, and even as a laminate film for book covers. PVC film is well known for its stretchability, cling, clarity, transparency, gloss, toughness, machinability, heat sealability, resiliency and low cost. PVC film is used for packaging foods on trays in which the film overwraps the food and is generally tacked or sealed to itself at the bottom of the tray by heat. PVC film used to package items such as fresh red meat also has the high oxygen permeability needed to develop the bright red color that fresh red meat forms when contacted with oxygen. In addition, these overwrapped trays use PVC film having excellent elastic recovery from deformations such as those caused by depressing a thumb or finger against an overwrapped cut of red meat, poultry or ground meat. The properties of PVC film are typically easily modified for particular applications by adjusting the film thickness, or the type or amount of plasticizers and additives such as antifog, antiblock or slip agents. With all of the above advantages, the search for a polyolefin based, thermoplastic, flexible film which may act as a substitute or replacement for PVC film has been difficult. No monolayer film having an equivalent or superior combination of properties has been found. Several different polyolefin stretch films have been commercialized to varying degrees of success. Multilayer polyolefin films have come the closest to achieving a combination of physical properties which approximate those of PVC films. Such polyolefin multilayer films generally sell at a premium above the price of PVC film used for similar applications. A market has developed for chlorine-free films having a combination of properties similar to PVC film and which may act as a substitute for PVC films in various applications. There have been prior efforts to identify a polyolefin thermoplastic film having an improved combination of elongation, elastic memory, heat sealability and puncture resistance. However, most thermoplastic polyolefin film packaging materials suitable for food contact have relatively poor combinations of properties particularly with respect to elasticity or elastic memory. Another important film property for food tray overwrap applications is low permanent deformation, which is a measure of the film's increase in length after stretching and relaxation. More particularly, the permanent deformation test used herein is derived from ASTM D-621 and measures the percent increase in length of a film sample stretched 50% and then allowed to recover for 30 seconds. Lower percentage values reflect the greater ability of a film to recover after being stretched. In tray overwrap applications, good film recovery preserves package appearance and integrity following handling abuse. Perfect elastomers would have 0% permanent deformation. Plasticized PVC has 3-5% deformation, while polyolefins such as linear low density polyethylene (LLDPE) generally have significantly higher permanent deformation, on the order of 6-15%. Thus, when a food wrapped in a poor deformation recovering material is poked by a consumer to test for freshness, the film does not immediately return to its former state and a deformed package having a depression caused by the finger poke results, which is aesthetically unpleasing. Commercialized multilayer polyolefin stretch films are available under the trademarks Yuka Wrap from Mitsubishi and Aliprot from Crocco. Yuka Wrap is described in four page brochure from Mitsubishi Petrochemical Co. Ltd. as an "environmentally sound/safe/non-PVC film" that has no plasticizer, yet provides ample extendibility and good restoration, a wide sealing range, well-balanced cling and slipperiness for use in high speed wrapping machines, and good optical properties. Aliprot is described in a 13 page brochure from Crocco as "the recyclable film" which is polyolefin-based containing no chlorine and no plasticizers and which is suitable for food cling wrap applications. Aliprot film purportedly is suitable for use with automatic wrapping machines and has high puncture resistance and good printability. Disadvantageously, both Yuka Wrap and Aliprot cling wrap films have poor elastic recovery from finger pokes when compared to PVC film. It would be desirable to provide a multilayer, flexible, stretchable blown film having a combination of physical properties making it suitable as a substitute or replacement film for PVC film in food contact applications. It would be advantageous for such film to be transparent, clear, have low haze and high gloss in combination with having a high degree of deformation recovery, rapid elastic recovery, good oxygen permeability which is sufficient to facilitate red bloom in fresh meat, heat sealability and good machinability. One object of this invention is to provide an improved multilayer stretch film suitable for use as a trayed food overwrap material. A further object is to provide such a stretch film in the form of three or more layers which has excellent puncture resistance and elastic recovery. Another object is to provide a polyolefin-containing multiple layer stretch film having low permanent deformation. Another object of this invention is to provide such a film which is capable of forming a sealed trayed food package as a stretch overwrap material. Still another object is to provide such a film having high abuse resistance. Yet another object of the invention is to provide a film which may be used on automatic packaging machinery. A further object of the invention is to provide a film in roll form which may easily be cut for use in packaging, particularly on automated equipment. An additional object is to provide such a film which can be heat sealed as a stretch wrap material around a food-containing tray at low temperature and energy. A further additional object of this invention is to provide an improved heat sealed food-containing tray package overwrapped by a film having good deformation recovery. Another additional object of the invention is to provide a chlorine free, polyolefin stretch film that is substantially free of heat shrinkage at 90°C, but having a combination of excellent extensibility, finger poke recovery, optical properties, and heat sealability. Yet another object of this invention is to provide a film which achieves one or more of the above objects and which may be made by a blown film or slotcast process. These and other objects and advantages may be found in various embodiments of the present invention. It is not necessary that each and every object or advantage be found in all embodiments of the present invention. It is sufficient that the present invention may be advantageously employed. Other objects and advantages of this invention will be apparent from the ensuing disclosure and appended claims. Summary of the Invention One aspect of this invention relates to a polyolefin, multilayer flexible film comprising at least a first outer layer, a second outer layer, and a core layer between the first and second outer layers. Preferably, the film is a slot cast film or a blown film which has at least three layers including a core layer disposed between first and second outer layers, and the film must have less than 10% unrestrained shrinkage at 90°C in at least one direction. The first outer layer of the inventive film comprises at least one copolymer of ethylene and at least one C 4 -C 8 alpha-olefin, and this copolymer has at least 75 weight percent of its polymer units derived from ethylene. This copolymer also has a density of at least 0.900 g/cm 3 and below 0.915 g/cm 3 , and a melting point of 85-125°C, preferably of 85-110°C. Optionally, and preferably the first outer layer also comprises a copolymer of propylene and ethylene having at least 80 wt.% of its polymer units derived from propylene. The core layer of all inventive film comprises at least one copolymer of ethylene and at least one C 4 -C 8 alpha-olefin, with the copolymer having at least 75 weight percent of its polymer units derived from ethylene. This core layer copolymer has a density below 0.900 g/cm 3 , and a melting point less than 80°C. The core layer may also optionally comprise a second and/or third copolymer as described above for the first outer layer. Preferably, the core layer will comprise the first copolymer in combination with suitably additives such as antifog agents, slip agents, nonionic surfactants, oleamides and/or fluoroelastomers. The second outer layer comprises at least one copolymer of ethylene and at least one C 4 -C 8 alpha-olefin. The copolymer has at least 75 weight percent of its polymer units derived from ethylene, and has a density below 0.915 g/cm 3 , and a melting point of 85-125°C, preferably of 85-110°C. Fundamental to the present invention is polyolefin film having a composition and made by a process whereby the film thus produced may be stretched taut over a trayed product (especially eg. fresh meat) heat sealed to itself and have good and rapid elastic recovery from depressions made eg. by poking a finger against the film overwrapped product. Desirably, the film will have good properties when stretch wrapped over articles without requiring a heat shrinkage operation. An especially preferred embodiment of the invention has at least three layers. Advantageously, film of preferred embodiments of the present invention may be substantially free of chlorine, substantially free of nonpolymeric plasticizers and/or substantially free of heat shrinkage at 90°C (≤ 10% shrinkage in both machine and transverse direction) and in an especially preferred embodiment may be essentially free of shrinkage at 90°C (less than 5% shrinkage) in the transverse direction. Low transverse direction shrinkage is a characteristic of slot cast or blown film. Films having a composition according to the present invention and made by a blown film (single bubble) or slot cast process may have highly desirable properties including excellent recovery from finger pokes in combination with other desirable properties including those related to film optics, extensibility, strength, sealability, gas permeability, cling, machinability, a surface tension and friction. A preferred embodiment of the invention may also be easily cut preferably in the transverse direction. Another aspect of the invention relates to a sealed food package comprising a tray with a bottom section surrounded by upwardly extending side walls, an article (especially perishable food) supported on the upper surface of the bottom section, and a stretched polyolefin film extending over each of the article, the upper edges of the side walls and at least part of the lower surface of the tray bottom section and heat sealed to itself in flattened relationship against the lower surface of the bottom section of the tray so as to form with the tray a sealed enclosure for the food. In this aspect of the invention, the improvement is a trayed article, eg. fresh meat (either cut portions or ground) covered with a polyolefin composition as a stretched film comprising a structure as further defined below. The preferred multilayer film comprises at least a first outer layer, a second outer layer and a core layer between the first and second outer layers as further described below. Brief Description of the Drawings Figure 1 is a schematic representation of a blown film process for making a thin flexible film according to the present invention. Figure 2 is a sectional view of a tubular film made according to the process of Figure 1. Figure 3 is a sectional view of a sheet film according to the present invention. Figure 4 is a view of a trayed article overwrapped with a multilayer film in accordance with the invention. Detailed Description of the Invention The invention in all of its embodiments comprises or utilizes a thermoplastic polymeric flexible film of 10 mils (254 µm (microns)) or less. The invention may be used as an industrial wrap or to wrap, cover, or enclose various non-food or food articles but has particular utility as a food overwrap stretch or cling film. Such films for wrapping foodstuffs will preferably have a thickness of less than about 2 mils (50.8 µm (microns)) more preferably less than 1 mil (25.4 µm (microns)). Typically the inventive films will be between about 0.3-1.2 mil (8-30 µm (microns)). Especially preferred for use as films for packaging trayed articles including foodstuffs, e.g., fresh red meat, are films of the invention wherein the film has a thickness of between about 12 to 20 µm (microns). Such films have good finger poke recovery, puncture resistance, and machinability. Films thinner than 10 µm (microns) are more difficult to make and handle in packaging processes without forming pin holes. Advantageously, films according to the present invention may be made thinner than 10 µm (microns) e.g., in the range of 8-10 µm (microns) for use as an overwrap by caterers or households. The inventive films may also be made in thicknesses of 12-14 µm (microns) for produce wrapping and 16-25 microns for poultry applications. The present inventive multilayer film comprises at least three essential layers viz a first outer layer, a core layer, and a second outer layer where the core layer is between the first and second layers. The layer ratios for relative thicknesses of each of these three essential layers may vary widely. Suitable ratios of from 2:1 or lesser to 14:1 or greater may be used for either the first outer layer or the core layer thickness relative to the thickness for the individual remaining layers. For example, typically either the first outer layer will be about 12-14 times thicker than individual core and second outer layers, or the core layer will be similarly thicker relative to the individual first and second outer layers. Individual layer thicknesses may also vary widely. Generally, the thickness of the first outer layer will be greater than any other layer. Typical preferred embodiments have a core layer thickness of from 15 to 70%. More preferably at least one of the first outer layer and core layer will comprise 50 to 70% of the total film thickness. The thickness for the core layer and the second outer layer in typical preferred embodiments ranges from 15 to 35% (more preferably 15 to 25%) of the total film thickness. Advantageously, preferred films do not require heat shrink tunnels or apparatus for effective use. Preferred films also provide a beneficial combination of two or more or all of the following properties including low permanent deformation, low haze, high gloss, heat sealability, good elastic memory and finger poke recovery, good machinability, easy to cut (especially in transverse direction), high puncture resistance, good mechanical strength and relatively low water vapor permeability properties with desirably high gas (O 2 and CO 2 ) permeabilities. The inventive film is used to cover, wrap or enclose articles including perishable products such as food and has similar optical and mechanical properties to PVC film. For storage the enclosed article may be overwrapped (with or without evacuation of air) and sealed e.g., by tacking or by a continuous hermetic seal. The sealing is typically by heat, i.e., the film has adjoining portions heated to a range between the heat seal initiation temperature and the burn-through temperature. Preferred films of the invention are food contact films suitable for wrapping meat, fruit, vegetables and for contact with food at room temperature or lower. These preferred films will have low extractable contents and meet government regulations, for extractable limits in the intended uses. Multilayer films of the present invention are polyolefin, flexible films having at least three layers and preferably consisting essentially of three polymeric layers. Desirably, the first and second outer layers are directly adhered to opposing sides of the core layer. The three or more layers of the multilayer film may be laminated but preferably are coextruded. Each layer of the first outer layer, core layer and second outer layer utilizes at least one copolymer of ethylene and at least one C 3 -C 8 alpha-olefin having a density below 0.915 g/cm 3 and having at least 75 wt.% and preferably at least 80 wt.% of its polymer units derived from ethylene. Advantageously, ethylenic polymer units of the ethylene alpha-olefin copolymers are nonpolar and hydrophobic which imparts moisture barrier properties to the film. Advantageously, ethylenic copolymers, in addition to polymeric units derived from ethylene monomer, will have at least about 3% by weight, preferably at least about 8% of its polymeric units derived from at least one other α-olefin monomer. Suitable α-olefin monomers include C 3 -C 8 monomers. In one preferred embodiment of the invention, this other monomer comprises butene-1, hexene-1, octene-1, or a combination thereof. Preferably at least one copolymer of the film will be of ethylene and a C 6 -C 8 alpha-olefin. Such copolymer may be the same or different from layer to layer, and more than one such copolymer may be used in each layer. The necessary polymeric formulations for the required film layers are discussed in detail below. Such copolymers which are useful in the present invention include polymers known as very low density polyethylene, as well as copolymers characterized as plastomers or elastomers. "Polyolefin" as that term is used herein refers to a hydrocarbon polymer derived from a simple olefin for example such as polyethylene or polypropylene and copolymers of such olefins. Polyolefins used in the present invention unless otherwise noted are substantially free (except for incidental amounts e.g., trace residues of catalysts or process related contaminants) of halogens, oxygen or other elements apart from carbon and hydrogen. However, these polyolefins may optionally have other polymers or substances such as processing aids, ultraviolet light stabilizers or antioxidants in admixture therewith. The term "Polyethylene" as used herein is the name for a polymer whose basic structure is characterized by the chain {CH 2 CH 2 } n . Polyethylene homopolymer is generally described as being a solid at room temperature which has a partially amorphous phase and partially crystalline phase with a density of between 0.915 to 0.970 g/cm 3 . The relative crystallinity of polyethylene is known to affect its physical properties. The amorphous phase imparts flexibility and high impact strength while the crystalline phase imparts a high softening temperature and rigidity. One form of linear polyethylene is generally referred to as high density homopolymer and has crystallinity of 70 to 90 percent with a density between about 0.96 to 0.97 g/cm 3 . Most commercially utilized polyethylenes are not linear homopolymer but instead have C 2 -C 8 alkyl groups attached to the basic chain. These substituted polyethylenes are also known as branched chain polyethylenes. Branching with alkyl groups generally reduces crystallinity, density and melting point. The density of polyethylene is recognized as being closely connected to the crystallinity. The physical properties of commercially available polyethylenes are also affected by average molecular weight and molecular weight distribution, branching length and type of substituents. People skilled in the art generally refer to several broad categories of polymers and copolymers as "polyethylene." Placement of a particular polymer into one of these categories of "polyethylene" is frequently based upon the density of the polyethylene and often by additional reference to the process by which it was made since the process often determines the degree of branching, crystallinity and density. In general, the nomenclature used is nonspecific to a compound but refers instead to a range of compositions. This range often includes both homopolymers and copolymers. For example, "high density" polyethylene (HDPE) is ordinarily used in the art to refer to both (a) homopolymers of densities between about 0.960 to 0.970 g/cm 3 and (b) copolymers of ethylene and an alpha-olefin (usually 1-butene or 1-hexene) which have densities between 0.940 and 0.958 g/cm 3 . HDPE includes polymers made with Ziegler or Phillips type catalysts and is also said to include high molecular weight "polyethylenes." In contrast to HDPE, whose polymer chain has some branching, are "ultra high molecular weight polyethylenes" which are essentially unbranched specialty polymers having a much higher molecular weight than the high molecular weight HDPE. Hereinafter, the term "polyethylene" will be used (unless indicated otherwise) to refer to ethylene homopolymers as well as copolymers of ethylene with alpha-olefins and the term will be used without regard to the presence or absence of substituent branch groups. Another broad grouping of polyethylene is "high pressure, low density polyethylene" (LDPE). The polyethylene industry began in the 1930's as a result of the discovery of a commercial process for producing LDPE by Imperial Chemical Industries, Ltd. researchers. LDPE is used herein to denominate branched homopolymers having densities between 0.915 and 0.930 g/cm 3 . LDPEs typically contain long branches off the main chain (often termed "backbone") with alkyl substituents of 2 to 8 carbon atoms on these branches. Another type of polyethylene is Linear Low Density Polyethylene (LLDPE). Only copolymers of ethylene with higher alpha-olefins are in this group. LLDPEs are presently recognized by those skilled in the art as having densities from 0.915 to 0.940 g/cm 3 . The alpha-olefin utilized is usually 1-butene, 1-hexene, or 1-octene and Ziegler-type catalysts are usually employed (although Phillips catalysts are also used to produce LLDPE having densities at the higher end of the range). LLDPEs typically do not have many long branches off the main chain as exhibited by LDPE. Another grouping of polyethylene is Very Low Density Polyethylene (VLDPE) which is also called "Ultra Low Density Polyethylene" (ULDPE). This grouping like LLDPEs comprise copolymers of ethylene with alpha-olefins, usually 1-butene, 1-hexene, or 1-octene and are recognized by those skilled in the art as having a high degree of linearity of structure with short branching rather than the many long side branches characteristic of LDPE. However, VLDPEs have lower densities than LLDPEs. The densities of VLDPEs are recognized by those skilled in the art to range between 0.860 and 0.915 g/cm 3 . The expression very low density polyethylene (VLDPE") sometimes called ultra low density polyethylene ("ULDPE"), refers to linear polyethylenes having densities below about 0.915 g/cm 3 , but this expression does not include ethylene alpha olefin copolymers of densities below about 0.90 g/cm 3 with elastomeric properties and referred to as elastomers. Some elastomers are also referred to by at least one manufacturer as "ethylene alpha olefin plastomers", but other manufacturers have characterized VLDPE as an ethylene α-olefin with plastomeric properties. VLDPE does not include linear low density polyethylenes (LLDPE) which have densities in the range of 0.915 - 0.930 gm/cm 3 . VLDPE's as the term is used herein may be made by solution or fluidized bed processes using a variety of catalysts including Ziegler-Natta, metallocene, or single site constrained geometry catalysts. VLDPE comprises copolymers (including terpolymers) of ethylene with C 3 -C 10 (preferably C 4 -C 8 ) alpha olefins, usually bipolymers of ethylene with 1-butene, 1-hexene or 1-octene, and in some instances terpolymers, as for example of ethylene, 1-butene and 1-hexene. A process for making VLDPEs is described in European Patent Document publication number 120,503 whose text and drawing are hereby incorporated by reference into the present document. Some ethylene alpha-olefin copolymers are also manufactured with elastomeric properties. Some of these have densities in the same range as VLDPE's, but may have greatly different physical properties due to differences in manufacturing processes. As used herein, ethylene alpha-olefin copolymers include bipolymers and terpolymers of ethylene and higher alpha-olefin comonomers and also include both elastomers and VLDPES. Suitable ethylene alpha olefin copolymers (including VLDPEs) for use in forming films according to the present invention include those manufactured by Dow Chemical Company, Exxon Chemical Company, Mitsui Petrochemicals Ltd., and Union Carbide Corporation. These copolymers are commercially available in dry resin form as powder, pellets or granules. Suitable ethylene alpha-olefin copolymers useful in the present invention include those manufactured using metallocene single site catalysts by Exxon Chemical Company of Houston, Texas under the trademark EXACT™ such as Exact 3027, Exact 3006, and Exact 4011, and also include those manufactured using Ziegler-Natta catalysts by Dow Chemical Company of Midland, Michigan under the trademark Attane® such as Attane 4203, Attane 4201, Attane XU 61520.01 and made using metallocene or single site constrained geometry catalysts under the trademark Affinity™ such as Affinity PL 1845, Affinity PL 1840, Affinity PL 1880, and Affinity FW 1650. Reported and/or measured properties of suitable ethylene alpha olefin copolymers are presented in Table A. In an especially preferred embodiment, the core layer comprises a blend of the above described copolymer(s) with at least one of a different type of copolymer i.e., a second copolymer of ethylene and at least one C 3 -C 8 alpha-olefin where this second copolymer has at least 75 weight percent of its polymer units derived from ethylene, and has a density less than 0.900 g/cm 3 , and a melting point less than about 80°C. Useful in films according to the present invention as an optionally polymeric constituent in admixture with the aforementioned ethylene alpha-olefin copolymers are propylene-based or butene-based copolymers with ethylene or ethylene propylene rubbers (EPRs) having less than 75 wt.% ethylene. Such propylene ethylene (C 3 C 2 ) copolymers or butene-1 ethylene (C 4 C 2 ) copolymers have at least 50 weight % of their polymeric units derived from either propylene or butene comonomer and have an ethylene content of less than 50 weight percent. A preferred polymer is a copolymer of propylene and ethylene having at least 80 weight percent of its polymer units derived from propylene. Such polymer is advantageously used in a blend with at least one layer, preferably the first outer layer. Beneficially such copolymer is present in an amount between about 2 to 15 weight percent of said first outer layer. An especially preferred C 3 C 2 copolymer has a melting point of at least 130°C in addition to having at least 80 weight percent of its polymer units derived from propylene. Examples of suitable C 3 C 2 or C 4 C 2 copolymers, or C 2 C 3 rubbers include propylene- ethylene random copolymers e.g. as sold by Shell Chemical Company of Atlanta, Georgia (Shell) under the trademark Shell DS6-281 and ethylene propylene rubbers e.g. as sold by the Polysar Rubber Division of Mobay Corporation at Akron, Ohio under the trademark Polysar EPM-306 (Polysar is a trademark of Bayer AG of Germany), and also include butene ethylene copolymers sold by Shell under the trademark Duraflex® polybutylene 8640 and Duraflex™ 8310. Reported and/or measured properties of these C 4 C 2 , C 3 C 2 , or C 2 C 3 copolymers are reported in Table B. Table B also includes properties of other polymers used in the examples including comparative examples below. The films of the present invention may also contain other polymers blended therein to modify film properties. It is contemplated that such polymers as: linear low density polyethylene (LLDPE); copolymers of ethylene and unsaturated esters such as vinyl esters e.g. ethylene vinyl acetate copolymer; ethylene alkyl acrylates such as ethylene-methylacrylate, ethylene-ethylacrylate and ethylene-butene acrylate; copolymers of ethylene and carboxylic acids such as ethylene acrylic acid copolymer (EAA); low density polyethylene (LDPE); high density polyethylene (HDPE); or ionomers may be blended into one or more of the individual layers including e.g., the first outer layer, core layer, or second outer layer of the multilayer film or may be added in optional additional layers. Preferred embodiments of the present invention have less than 20% by weight of such added nonethylene alpha-olefin copolymers. Also, any or all of the layers of the inventive films may be free of such aforementioned polymers. Inventive films which are substantially free (i.e. ≤5% by weight of total film) from such polymers have been found to be useful and have a very desirable combination of properties without inducing disadvantageous properties or the additional trouble and expense of purchasing, storing, measuring and blending another resin and such further adjustments as would be required by addition of another resin to a film structure. Similarly, layers of the inventive film, which are substantially free (i.e., ≤5% by weight of the total layer) from non ethylene alpha-olefin copolymers are useful. The present invention may utilize commercially available resins. As generally recognized in the art, these resins may be melt blended or mechanically mixed by well known methods using commercially available equipment including tumblers, mixers or blenders. Also, if desired, well known additives such as processing aids, slip agents, antifog agents, cling agents, antiblocking agents, pigments, antioxidants, and mixtures thereof may be incorporated into the film, by blending prior to extrusion. Such additives are typically present in the inventive film in an amount less than 10 wt.% of the total film weight, and less than 10 wt.% for individual layers based on the individual layer weights. Preferred embodiments of the present invention suitable for stretch overwrapping refrigerated food items such as meat or cheese typically employ antifog agents, and slip agents, and commercially available polymer resins often contain either or both primary and secondary antioxidants which are added by the manufacturers (generally to inhibit degradation or crosslinking during storage and transit of the resin). Advantageously, in certain embodiments of the present invention either or both of the first outer layer and core layer comprises an antifog agent in an amount up to 4 weight percent of each layer. Certain additives which were used in the examples below are identified in Table C. As will be explained hereinafter in more detail, the three-layer film of the present invention overcomes the aforedescribed limitations of prior polyolefin films as a PVC replacement in overwrapping trayed foods. It also performs as well as or better than many other commercially employed multilayer polyolefin films, and provides greater recovery from thumb depressions than other polyolefin films. Moreover, this three layer film has been demonstrated to provide an unexpected combination of good optical properties and low permanent deformation percentages. All of these properties are advantages in food packaging and other applications and especially for retail food packaging such as for stretch wrapping trayed fresh red meat with plastic film. As previously noted, the multilayer inventive film comprises at least three layers. All three essential layers (i.e. the first and second outer layers and the core layer) are believed to cooperate together to provide a thermoplastic flexible film having a superior combination of optical and mechanical properties, particularly stretch properties, especially film recovery after deformation e.g. high thumb depression elastic recovery values, relative to other polyolefin type, non-PVC stretch film having less than 10% shrinkage at 90°C in at least one direction. Preferred films of the present invention have at least one C 2 C 8 copolymer (preferably a substantially linear ethylene octene-1 copolymer) having at least 75 wt.% of its polymer units (more preferably at least 80%) derived from ethylene in at least one layer in an amount of at least 50 wt.% (more preferably at least 60 wt.%) of the layer. It is believed that such C 2 C 8 copolymer adds strength to the film, particular when said C 2 C 8 copolymer has a density of at least 0.900 g/m 3 or higher. Beneficially, films of the present invention may have a first outer layer, core layer and/or second outer layer comprising at least one copolymer of ethylene and at least one C 3 -C 8 alpha-olefin, with the copolymer having at least 75 weight percent of its polymer units derived from ethylene, and having a density of at least about 0.900 g/cm 3 and below 0.915 g/cm 3 , and a melting point of at least 90°C, and having a narrow average molecular weight distribution M w / M n <3. Preferred heat sealable films according to the present invention have at least one layer (preferably at least the first outer layer) containing a blend of broad (≥ 3.0) and narrow (<3.0) molecular weight distribution ( M w / M n ) ethylene alpha-olefin copolymers. Preferably at least 15 wt.% of a narrow molecular weight material will be blended with at least 30% and preferably from 30 to 70 wt.% of a broad molecular weight material. Such blends are believed to expand the temperature range over which heat sealing of the inventive film to itself may be accomplished. Advantageously, in some embodiments of the present invention a hot bar sealing range of at least 25°C is obtained or preferably at least 50°C. Advantageously, some preferred embodiments of the present invention obtain a hot bar sealing range of at least 50°C without resort to expensive crosslinking operations e.g. by irradiation using electron beam curing units. However, if desired the film may be crosslinked to further broaden the heat sealing range. Also, although not essential in the practice of this invention, it may be desirable to cross-link one or more layers of the inventive film for improved abuse and/or puncture resistance and other physical characteristics. This for example may be accomplished by irradiation using e.g. any electron beam generator operating in a range of about 150 kilovolts to about 6 megavolts with a power output capable of supplying the desired dosage. Many devices for irradiating films are known to those of skill in the art. The irradiation is usually carried out at a dosage up to about 2 x 10 5 Gy (20 MR), typically between about 10 4 Gy (1 MR) and about 2 x 10 5 Gy (20 MR), with a preferred dosage range of about 2 x 10 4 Gy (2 MR) to about 1,2 x 10 5 Gy (12 MR). Irradiation can be carried conveniently at room temperature, although higher and lower temperatures, for example, 0°C. to 60°C. may be employed. Alternatively, crosslinking may be performed using a chemical crosslinking agent or by a combination of chemical and irradiative means. Advantageously, inventive films which are substantially uncrosslinked may be suitably made and used. Preferably films of the present invention are blown films made by a blown film process. As the term "blown film" is used herein is meant a film produced by extruding a polymer melt from an annular die into a tube which is simultaneously pulled away from the die and over a bubble of air trapped between the die and collapsing means such as nip rolls while air is blown around the outer film tube surface to stabilize and quench the tube. Generally, the film resins and any additives are introduced to an extruder (generally one extruder per layer) where the resins are melt plastified by heating and then transferred to an extrusion (or coextrusion) die for formation into a tube. Extruder and die temperatures will generally depend upon the particular resin or resin containing mixtures being processed and suitable temperature ranges for commercially available resins are generally known in the art, or are provided in technical bulletins made available by resin manufacturers. Processing temperatures may vary depending upon other process parameters chosen. In extrusion of the ethylene alpha-olefin copolymer outer layer blends of the present invention, barrel and die temperatures, for example, may range between about 175 to 210°C. However, depending upon such factors as other resins which may be employed, the manufacturing process used and particular equipment and other process parameters utilized, variations are expected. Actual process parameters including process temperatures will be set by one skilled in the art without undue experimentation. In the blown film process, contact of the outer film surface and optionally also the inner film tube surface with room temperature or cooler air cools the radially expanding tubular polymer melt as it leaves the die and travels over the trapped bubble thereby causing it to solidify. The point of transition from polymer melt to solid is commonly known as the frost line. Above the frost line, the blown or inflated tube is collapsed and fed through nip rolls which trap air within the tube to maintain an expanded bubble of fluid (typically air). Optionally, this air bubble may be used to internally cool the expanded film tube by continuously delivering cool air (e.g. at about 45-55°F (7-13°C)) while simultaneously removing warm air from inside the bubble via the die. This exchange of air is usually performed at a constant rate to produce a final blown film of uniform size. The internal bubble cooling assists in quenching the film and may also produce film having improved optical properties (i.e. lower haze and higher gloss). The blow up ratio is the ratio of the film circumference after radial expansion and cooling to the die opening circumference and may be determined from the known annular die opening dimensions and by measuring the transverse width of the flattened, expanded and cooled tubular film. Typical blow up ratios range from 2:1 to 5:1. Dimensions and properties of the blown film may be adjusted by altering the blow up ratio and/or the haul off (or draw) speed of the film as it is pulled out of the die in the machine direction e.g. by driven nip rolls. Referring now to the drawings, Figure 1 depicts a schematic view of a typical preferred process 10 which according to the present invention may be utilized to produce a multilayer, coextruded, blown film of the invention. In the depicted process 10 a first polyolefin polymer resin feed 11 is placed in a hopper 12 of a screw-type extruder 13 wherein it is heated to an appropriate temperature above the melting point of the first polymer feed to cause melting thereof. The extruder may also be provided with a jacketed chamber through which a cooling medium is circulating. The rotation of a screw within the extruder 13 forces melt plastified polymer through a connecting pipe 14 into a coextrusion die 15. Simultaneous with the introduction of the melt plastified first resin feed 11 to the die 15, a second resin feed 16 (which has been placed in a hopper 17 of a second extruder 18) is similarly heat plastified and forced by extruder 18 through a pipe 19 to coextrusion die 15. A third resin feed 20 is similarly introduced to die 15 through a third hopper 21, extruder 22 and pipe 23. In a preferred embodiment of the present invention, three extruders are utilized to produce the three film layers. However, in the coextrusion art it is known that where the same polymer melt is used in more than one layer of a multilayer construction, that the melt from one extruder may be divided e.g. at the die and used for multiple layers. In this manner a tubular five layer film of the invention for example, may be made utilizing three or four extruders. The coextrusion die 15 has an annular, preferably circular, opening and is designed to bring together the first, second and third polymer melts to form a tubular multilayer polymeric melt having a first outer layer (inner layer of the tube) comprising at least one copolymer of ethylene and at least one C 4 -C 8 alpha-olefin, said copolymer having at least 75 weight percent of its polymer units derived from ethylene, and said copolymer having a density of at least 0.900 g/cm 3 and below 0.915 g/cm 3 , and a melting point of 85-125°C; and a second outer layer (outermost layer of the tube) comprising a copolymer of ethylene and at least one C 4 -C 8 alpha-olefin said second copolymer having at least 75 weight percent of its polymer units derived from ethylene, and having a density below 0.915 g/cm 3 , and a melting point of 85-125°C; the first and second outer layers being separated by a core layer comprising at least one copolymer of ethylene and at least one C 4 -C 8 alpha-olefin, said copolymer having at least 75 weight percent of its polymer units derived from ethylene, and said copolymer having a density below 0.900 g/cm 3 , and a melting point less than 80°C. Preferably the first outer layer also comprises a copolymer of propylene and ethylene having at least 80 wt.% of its polymer units derived from propylene. The multilayer melt is coextruded out of an annular die opening as a tube and the die 15 is equipped, as is known in the art, with a central orifice through which a fluid such as air is typically introduced to radially expand the diameter of the extrudate forming a blown tubular film 24 having an exterior surface 25 and interior surface 26. The blown film tube 24 is externally cooled by cooling means such as an air ring 27 which blows cooling air along the lower outer surface 28 of the tube 24. Simultaneously, the internal surface 26 is preferably cooled e.g. by contact with refrigerated air (e.g. at 5-15°C) delivered through an internal bubble cooling unit having a perforated pipe 29. The perforated pipe 29 is concentrically disposed around a longer pipe 30 of narrower diameter which is open at its distal end 31 to receive and remove warmer air which has risen to an upper end 32 of the film bubble 24. The streams of external and internal cooling fluids such as air and/or water constitutes a cooling zone serving to chill or set the extruded and radially expanded plastic tube at the desired diameter. The blown film bubble 24 is optionally stabilized by an external concentric cage 33 which helps maintain the bubble along a straight path to a collapsing ladder comprising a series of converging rolls 34. The blown bubble 24 is collapsed in rolls 34 and flattened by driven nip rolls 35 which may also serve to collapse the tube which can be reeled as a tube or slit. The stabilizing cage is particularly useful to stabilize films made using an internal bubble cooling apparatus. For making sheet film rolls suitable for use as an overwrap to package articles such as fresh red meat and processed meats, the flattened film tube 36 is slit open into one or more sheets which may be wound on paperboard or plastic cores for subsequent dispensing or use. In the embodiment depicted in Fig. 1, the flattened tube 36 is conveyed through a slitting or cutting means such as slitter 37 where the film tube is slit by knives into two sheets 38 and 39. First multilayer sheet 38 is conveyed by rollers 40 to wind up reel 41 and second multilayer sheet 39 is conveyed by rollers 42 to wind up reel 43. Thus the film may be wound in a roll with the first outer layer comprising either the interiorly or exteriorly disposed surface of the roll. It will be appreciated that the flat width of the sheet produced may be in a variety of sizes depending upon the circumference of the blown film and the number and placement of cuts made in the tube. Also, for production of flexible films, typical film wall thicknesses in the range of about 10 mil (254 mm) or less may be produced. Advantageously, according to the present invention, this multilayer blown film may be extruded, blown, cooled, collapsed, slit and reeled using well known and available equipment. In the above description, reference is made to use of nip rolls which function to either or both pull or transport the tube and also to collapse an expanded tube to a flattened condition. However, it will be apparent to those skilled in the art that other transport means and collapsing means may be employed and are known in the art including such apparatus as collapsing ladders, drive belts, and the like and use of such mechanisms is contemplated by the present invention. Furthermore, it will be appreciated by those skilled in the art that such parameters as the die opening diameter, nip roll speed, amount and temperature of fluid such as air introduced and captured between the die and nip rolls, rate of flow of extrudate from the die opening, melt temperatures, type of cooling medium e.g. water or air, and internal and external bubble cooling temperatures may all be adjusted to optimize process conditions. For example, the circumference or flat width of the blown film tube may be increased to varying degrees above that of the die gap opening by modification of one or more of the above parameters. Similarly, the blown film tube may be conditioned or modified e.g. by interior, internal and/or external application and variation of the types and amounts and characteristics of materials, including gaseous or liquid fluids contacted therewith as well as setting and changing such parameters as pressures and temperatures. It will be understood in the art that such parameters may vary and will depend upon practical considerations such as the particular polymer resins comprising the tube as well as the presence or absence of modifying agents, the equipment utilized, and desired rates of production, desired tube size (including diameter and thickness), the quality and desired performance characteristics of the tubular article for the use intended. These and other process parameters including process temperatures are expected to be set by one skilled in the art without undue experimentation in view of the present disclosure. Also, certain non-uniformities in processing, such as variation in film thickness, unequal heating or cooling of the tubing, non-uniform air flows, and the like can be obviated by rotation with or without oscillation, either alone or in combination, of the die, the air ring, or tubing winder(s) (reeler) with respect to the vertical axis of the tubing. It should also be understood that while manufacture of blown film has been described above with respect to a coextrusion process which utilized vertical upward transport of the tube during bubble formation, that those skilled in the art may extrude the tube and form a bubble in other directions including vertically downward. Referring now to Fig. 2, a cross-section of the tubular blown film 24 of Fig. 1 is shown having an outer, exterior surface 25 and an inner, interior surface 26. The film 24 has three layers 50, 51 and 52 whose thicknesses are exaggerated here for clarity. A first outer layer 50 is the inner surface layer of the film tube 24 and has an interior surface 26. Disposed next to said first outer layer 50 is a core layer 51 which is preferably directly adhered by melt coextrusion to said layer 50 on one side and on the opposing side to a second outer layer 52. Second outer layer 52 is the outer surface layer of said tube 24 and has an exterior surface 25. Preferably the film of the present invention consists essentially of three layers, but additional layers may be laminated or coextruded on either side of the above three layers or interspersed between layers. A monolayer embodiment of the invention is also claimed. Referring now to Fig. 3, a sheet 60 is shown in exaggerated cross-section. Such sheet 60 may be made by cutting open tubular film 24 of Fig. 2 forming a sheet 60 having opposing ends 61 and 62 with three layers 50, 51 and 52 which correspond to the same layers discussed above with respect to tubular film 24 in Figs. 1 and 2. The exterior surface 25 and interior surface 26 of tube 24 are now opposing surfaces 25 and 26 of sheet 60. Referring now to Fig. 4, an overwrapped tray 70 is depicted. Film sheet 60 overwraps an article such as ground meat or a cut of meat that is placed on a tray 71. The film sheet 60 is stretched over the article and support tray 71 and the ends (not shown) of the film sheet 60 are gathered together along a bottom surface (not depicted) of the tray 71 and tacked or heat sealed together to provide a tray 70 covered by a protective stretch film 60 having an exterior film surface 25. It should be understood that in the manufacture of film sheet 60, either the inner or outer surface of the film tube 24 of Fig. 2 may be constructed to function as a food contact layer or as the exterior layer of an overwrapped article. Also, sheet 60 may be wound on a roll and portions of said sheet 60 cut off at desired lengths for use. Such rolls may contain many meters of film. The following are examples and comparative examples given to illustrate the present invention. Experimental results of the following examples are based on tests similar to the following test methods unless noted otherwise. All ASTM test methods noted herein are incorporated by reference into this disclosure. Tensile Strength: ASTM D-882, method A % Elongation: ASTM D-882, method A 1% Secant Modulus: ASTM D-882, method A Oxygen Gas Transmission Rate (O 2 GTR): ASTM D-3985-81 at 23°C and 0% relative humidity Water Vapor Transmission Rate (WVTR): ASTM F-1249-90 at 38°C Elmendorf Tear Strength: ASTM D-1992 Gauge: ASTM D-2103 Haze: ASTM D-1003-52 Gloss: ASTM D-2457, 45°C Angle Melting Point: ASTM D-3418, DSC with 5°C./minute heating rate Melt Index: ASTM D-1238, Condition E Molecular Weight Distribution: ASTM D-3593 Vicat Softening Point: ASTM D-1525-82 Shrinkage Values: Shrinkage values are defined to be values obtained by measuring restrained shrink at 90°C. for five seconds. Four test specimens are cut from a given sample of the film to be tested. The specimens are cut into square of 10 cm length in the machine direction by 10 cm. length in the transverse direction. Each specimen is completely immersed for 5 seconds in a 90°C. water bath. The specimen is then removed from the water bath and the distance between the ends of the shrunken specimen is measured for both the M.D. and T.D. directions. The difference in the measured distance for the shrunken specimen and the original 10 cm. side is multiplied by 10 to obtain the percent of shrinkage for the specimen in each direction. The shrinkage for the four specimens is averaged for the MD shrinkage value of the given film sample, and the shrinkage for the four specimens is averaged for the TD shrinkage value. Elastic Recovery (Thumb Depression) A rigid hollow paperboard circular cylinder having an inner diameter of 7.5 cm, an outer diameter of 9.4 cm, a thickness of 0.95 cm, and a depth of 1.5 cm is overwrapped with a test film. The test film is placed over one of two opposing, parallel, planar, circular surfaces (faces) of the cylinder and manually pulled taut about the radial edge of the cylinder face with the minimum force necessary to produce a smooth planar surface and the film is secured to the outer cylinder wall by adhesive tape applied around the outer cylinder surface. The overwrapped cylinder is placed on a flat, smooth rigid surface of a table so that the open face of the cylinder is against the table and the opposing film covered face is above the table. The center part of the portion of the test film which is held in the plane of the circular face of the cylinder is quickly pushed perpendicular to the cylinder face into the interior of the cylinder 1.5 cm by a thumb until the thumb firmly presses against the table surface with only the stretched film interposed therebetween. The thumb is then quickly removed from contact with the film and the degree of elastic recovery of the film to its former planar state is evaluated one minute after removal of the deforming force and assigned a number form 0.0 to 5.0. An assigned value of 0.0 indicates a film having total deformation with no recovery after one minute from removal of the depressing thumb force. An assigned value of 5.0 indicates a film having a complete recovery similar to that of a commercially available PVC film sold for use as a fresh red meat stretch wrap. Assignment of numbers between 0.0 and 5.0 reflect the rate of recovery, with faster recovery times having higher numbers. All evaluations are made by an observer relative to a control film of plasticized PVC. Permanent Deformation The procedure used in the following examples for measuring permanent deformation was derived from ASTM D621 and employs an Instron table model tensile testing machine or equivalent. Four samples are tested for MD permanent deformation, and each cut to 12,7 cm (5 inches) MD length and 2,54 cm (1 inch) TD length. Likewise, four samples are tested for TD permanent deformation and each cut to 12,7 cm (5 inches) TD length and 2,54 cm (1 inch) MD length. The chart speed for both the A and B jaws is set at 50,8 cm (20 inches)/minute. The A jaws crosshead speed is set at 5,08 cm (2 inches)/minute and the B jaw crosshead speed is set at 50,8 cm (20 inches)/minute. The chart pen settings are adjusted so that the crosshead will return to gauge length of 5,08 cm (2 inches) after stretching the film 50% of its initial length, i.e. 2,54 cm (1 inch). The B jaw speed of 50,8 cm (20 inches)/minute is run and the cross heat returns to its original position after the 50% stretch. This original position is maintained for 30 seconds. Then the jaw speed of 5,08 cm (2 inches)/minute is run in like manner. When force begins to reappear on the chart, the crosshead is returned to the initial gauge length. The chart is read in cm (inches), from the beginning of the test to where force reappears, i.e. the pen leaves the baseline. The percent permanent deformation is obtained by multiplying the cm (inches) on the chart by 5. The procedure is repeated with the remaining samples, and an arithmetic average is calculated. The procedure is otherwise identical to ASTM 621. Hot Bar Sealing Range The hot bar sealing range test determines the acceptable temperature ranges for heat sealing plastic films using a thermal bar heat sealer. A Sencorp Systems Model 24-AS laboratory sealer manufactured by Sencorp Systems, Inc. Hyannis, Massachusetts, U.S.A. was used. The thermal bar heat sealer is equipped with an upper 0,635 cm (1/4 inch) wide sealing bar which may be heated to variably controlled temperatures. In this test, two 2,54 cm (one inch) wide and 10,16 cm (four inch) long (long in the TD direction) samples are cut from a tubular film. The thermal bar heat sealer is equipped with controls for temperature, time, and seal bar pressure. These controls except for temperature are set at the following conditions: 1.0 seconds dwell time (time that the upper heated jaw is held against the lower one inch (2.54 cm) wide and 0,9525 cm (3/8 inch) thick fixed platen made of silicone rubber) 50 psi (345 kPa) jaw pressure The two film samples are held together with the first outer surfaces of each film in contact with each other for use in determining the minimum sealing temperature. The two samples are held together and placed between the upper jaw and lower sealing platen of the sealer. The upper jaw and lower platen have glass fiber reinforced covers which are coated with a high temperature resistant, non-stick coating of a fluorocarbon polymer. By trial and error the minimum temperature to seal the two film portions to each other was determined by pressing the jaw against the platen at the prescribed pressure for the indicated time using various temperature settings. The maximum temperature was then determined for a similar film sample having two film portions in first outer layer to first outer layer contact by placing the adjoining film portions between the covered sealer jaw and platen, and then closing the upper seal bar down on the lower platen. The film sample is observed after trial and error applications of higher temperatures and the temperature which does not cause a break in the seal, burn-through, or significant distortion of the seal is determined. The maximum temperature is the last noted temperature obtained before observing a break in the seal integrity. Molecular Weight/Size Distribution Ethylene alpha-olefin copolymers may be partially characterized by their weight average molecular weight ( M w ) which is determined by multiplying the weight of each chain of a given number of repeat units by the number of such chains and dividing by the total weight of chains. Ethylene alpha-olefin copolymers may also be partially characterized by a number average molecular weight ( M n ), which is derived from the total weight of polymer molecules divided by the total number. When both of these are known, they can be used to characterize the shape of the molecular weight distribution curve for the copolymer, i.e., the number of polymer chains in a molecular weight interval as the ordinate and the molecular weight as the abscissa. Qualitatively, a high M w / M n connotes a wide distribution of molecular weights whereas a low M w / M n connotes a narrow distribution. M w / M n can be measured by several different techniques, but as used herein the gel permeation chromatography ("GPC") procedure outlined in ASTM D-3593-80 is used. In general, relatively narrow M w / M n distribution (and low ratio) permits sharper control of physical properties and superior optical properties, i.e. relatively high gloss and low haze. However, relatively low M w / M n ratio value polymers are also difficult to process and have a narrow heat sealing range. More particularly, certain specific ethylene alpha-olefin copolymers known to applicant as useful in this invention, particularly with respect to film recovery properties, are characterized by relatively narrow molecular weight distribution and M w / M n values below about 3.0. Relatively broad (≥3.0) M w / M n distribution, i.e. high ratio, ethylene alpha-olefin copolymers generally have better processing characteristics and a broader heat sealing range. These broad distribution materials are also preferably used in the invention in combination with the narrow molecular weight materials. Unless otherwise indicated, average molecular weight values M w , M n , M z are reported values and may be measured by a gel permeation chromatography method similar to that of ASTM D-3593-80. In all of the following examples, unless otherwise indicated herein, the film compositions were produced generally utilizing typical blown film manufacturing apparatus and methods as further described in the detailed description above and with respect to the drawings and the first outer layer was the inner surface layer of the film if made by the above described tubular process. The polymers and additives used were those described in Tables A-C. All percentages are by weight unless indicated otherwise. Examples 20-21 Examples 20 and 21 are polyolefin multilayer films of the present invention. The film of Example 20 has an identical composition to that of Example 21 except that the layer thickness ratio is different. The coextruded film of Example 20 had a first outer:core:second outer layer thickness ratio of 15:70:15, whereas the layer ratio for Example 21 was 25:50:25. The films of Examples 20 and 521 each had a core layer sandwiched between first and second outer layers. Each core layer comprised a blend of three polymers with 2 wt.% of an antifog agent. The first polymer is an ethylene octene-1 (C 2 C 8 ) copolymer having at least 75 wt.% of its polymer units derived from ethylene and having a melting point of 85-125°C and a density of at least 0.900 g/cm 3 and below 0.915 g/cm 3 . The first copolymer used in the core layer of Examples 20 and 21 was commercially available under the trademark designation DOW XU 61520.01 from Dow Chemical Company (Dow) of Midland, Michigan, U.S.A. and is similar to another product sold by Dow under the trademark Attane 4201 except that XU 61520.01 has no added secondary antioxidant. The XU 61520.01 polymer, which does contain primary antioxidant, has been reported to have the properties listed in Table A. The second polymer present in the core layer was a copolymer of ethylene and butene-1 (C 2 C 4 ) having at least 75 wt.% its polymer units derived from ethylene, a density less than 0.900 g/cm 3 and a melting point less than 80°C. This second polymer is commercially available under the trademark Exact™ 4011 from Exxon Chemical Co. (Exxon) of Houston, Texas, U.S.A. The Exact 4011 copolymer has been reported to have the properties listed in Table A. The third polymer present in the core layer was a copolymer of propylene and ethylene (C 3 C 2 )having at least 80 wt.% of its polymer units derived from propylene (available as Shell 056-081). The core layer of Examples 20 and 21 is a blend of 68 wt.% XU 61520.01 (C 2 C 8 ) copolymer with 15 wt.% Exact 4011 (C 2 C 4 ) copolymer, 15 wt.% Shell 056-081, and 2% of an antifog agent-containing additive sold by the ICI Specialty Chemicals unit of ICI America Inc. of Wilmington, Delaware under the trademark Atmer® 8112. This additive is believed to contain up to about 20 wt.% of a nonionic surfactant in an LDPE base. Thus, the core layer contains a polymeric blend of a higher density, higher melting point, broad molecular weight distribution, higher vicat softening point VLDPE with a lower density, lower melting point, narrow molecular weight distribution, lower vicat softening point, ethylene alpha-olefin copolymer. The first outer layer of the films of Examples 20 and 21 comprised a blend of 96 wt.% of an ethylene-butene-1 copolymer available under the trademark Exact 3027 with 2% of the aforementioned Atmer 8112 additive and 2% of a slip agent containing-additive (antiblock polyethylene master batch) which is sold under the trademark Ampacet 50914 by Ampacet Corporation of Tarrytown, New York, U.S.A. Ampacet 50914 contains 5% ethylene-bis-oleamide in an LDPE base and functions as a slip and antiblock agent. The second outer layer of the films of Examples 20 and 21 comprise a blend of 80% of Exact 3027, 15% of Exact 4011, and 2% of Ampacet A/B 50914 and 3% of a second additive which is available from Ampacet Corporation under the trademark Ampacet 10926. Ampacet 10926 contains about 2% of an oleamide in an LDPE base, and functions as a slip agent. In making the multilayer films of Examples 20 and 21, one extruder was used for each layer and the heat plastified resins from each extruder were introduced to a coextrusion die from which the resins were coextruded into a blown film. For each of the above three layers, the layer blend constituents preblended in a drum mixer, placed in a hopper, then fed from the hopper into an attached standard single screw extruder where the resin and/or mixture was heat plastified and extruded through a three layer coextrusion die and inflated into a blown film. The extruder barrel temperature profile for each of the three layers was about 149-177°C (300-350°F). The extrusion die had an annular exit opening of 20 cm (8 inch) diameter with 1.14 mm (45 mil) gap. The coextrusion die temperature was set at about 204°C (400°F). The extruded multilayer melt was pulled from the die with a pair of opposing nip rolls so that the tube passed over a single trapped bubble of air located between the die and nip rolls thereby causing radial expansion of the tube; simultaneously, the inflated tube was externally and internally cooled. The blow up ratio was about 2:1. The external and internal cooling was with refrigerated air about 7-13°C (45-55°F) and an internal bubble cooling unit was used. The apparatus and process used was similar to that described above with respect to the drawings. The cooled blown film was flattened by passage through a pair of nip rollers whose speed was controlled relative to the extrusion rate. In Examples 20 and 21, a flattened tube of about 71 cm (28 inches) flat width and 15 µm (0.6 mil) thickness was produced. Such variables as the blow up ratio, nip roll speeds, extrusion screw speeds, extrusion rates, bubble cooling, are generally adjusted to maximize bubble stability and throughput for the desired amount of film expansion and size. The resultant films of Examples 20 and 21 were easily made and had an excellent appearance. The tubular film was slit into two sheets and wound on reels. The physical properties of the films were measured and are reported in Tables 1 and 2. Internal and external cooling air temperatures ranged from about 10-19°C (50-66°F) for examples 20-21 was about 63.5 cm (25 inches). Physical properties for the resultant blown films were measured and are reported in Tables 1 and 2 below. Examples 20-21 all demonstrate good physical properties. In particular, example 20 which utilizes the core layer as the thickest layer, has a desirably broad hot bar sealing range of about 32°C (90°F) and advantageously has a high maximum temperature before burn-through or breaking. The higher content of component (e) which has a high melting point and broad molecular weight distribution is believed to contribute to a higher value for the maximum sealing range temperature of example 20. The higher content of component (a) which has a narrow molecular weight distribution and a lower melting point than (e) is believed to produce a lower minimum temperature for the sealing range. Also, notable are the excellent thumb depression elastic recovery values for all samples. Further modifications of the invention will be apparent to those skilled in the art and all such modifications are deemed to be within the scope of the invention as defined in the following claims.

Claims: A polyolefin, multilayer flexible film having at least three layers comprising: a first outer layer comprising at least one copolymer of ethylene and at least one C 4 -C 8 alpha-olefin, said copolymer having at least 75 weight percent of its polymer units derived from ethylene, and said copolymer having a density of at least 0.900 g/cm 3 and below 0.915 g/cm 3 , and a melting point between 85 to 125°C; a core layer comprising at least one copolymer of ethylene and at least one C 4 -C 8 alpha-olefin, said copolymer having at least 75 weight percent of its polymer units derived from ethylene, and said copolymer having a density below 0.900 g/cm 3 , and a melting point of less than 80°C; and a second outer layer comprising a copolymer of ethylene and at least one C 3 -C 8 alpha-olefin, said copolymer having at least 75 weight percent of its polymer units derived from ethylene, and said copolymer having a density below 0.915 g/cm 3 , and a melting point between 85-125°C wherein said core layer is disposed between said first and second outer layers and said multilayer film has less than 10% unrestrained shrinkage at 90°C in at least one direction. A film, as defined in claim 1, wherein said melting point of said copolymer in said first outer layer, and said copolymer in said second outer layer is between 85 to 110°C.

Inventors: VELAZQUEZ ALBERTO, VELAZQUEZ, ALBERTO
Applicants: VISKASE CORP, VISKASE CORPORATION
Application year: 1995
Main classification: B32B27
IPC codes: B32B27