FILM HAVING MODIFIED SURFACE CHARACTERISTICS THROUGH USE OF COMBINATION OF SPHERICAL AND LAMELLAR PARTICULATES

Abstract: A combination of lamellar and spherical particulates provides a film with desired slip and antiblock characteristics, in the absence of loose dust on the surface of the film. The film exhibits improved Machinability over comparative films having either lamellar or spherical particulates. The invention is also directed to a composition of matter comprising a polymer having the mixture of lamellar and spherical particulates.

Description: FILM HAVING MODIFIED SURFACE CHARACTERISTICS THROUGH USE OF COMBINATION OF SPHERICAL AND LAMELLAR PARTICULATES FIELD OF THE INVENTION The present invention relates generally to films, both monolayer hlms and multilayer films, and particularly to packaging films. The present invention also relates to packages comprising products packaged in a film. The present invention is particularly related to films having a relatively low film-to-film coefficient of friction as well as a high resistance to blocking. BACKGROUND OF THE INVENTION For some time it has been known to provide loose dust, e.g., loose corn starch dust, on an outer surface of a film, in order to facilitate its subsequent processing on high speed packaging machines. That is, dust applied to the surface of the him lowers the film-to-film coefficient of friction, ι.e., acts as a slip agent (lubricant), as well as improving the resistance of the film to "blocking", ι.e, as an anti-blocking agent. Blocking is an undesirable adhesion between layers of plastic, particularly rolled up film, that may develop duπng storage. For some ume it has also been known to incorporate particulate antiblocking agent into the resin. The incoφorated antiblocking agent functions by forming minute protrusions that maintain separating air spaces that interfere with adhesion, i e , blocking. However, the application of dust to the film is detrimental to the quality of the atmosphere in which the film is manufactured and used, and the dust is subject to sloughing off of the film during shippage, etc., and other undesirable effects Furthermore, films having antiblocking agent incorporated into the resin do not possess a desired combination of slip and antiblock properties. Thus, it would be desirable to reduce or eliminate dust on the surface of the him, while providing the film with desired sbp and antiblock properties. It has also been known to provide the film with a sbp agent, which is generaUy provided in at least the outer layer(s) of the film. The sbp agent migrates to one or more outer surface(s) of the film, i.e, "blooms" to one or more outer surfaces, thereby decreasing the film-to-film coefficient of friction, ι.e., resulting in a film which sbdes more easily against itself and other materials. However, it has been found that: (1) the desired coefhcient of friction is not obtained until the sbp agent is given adequate time to bloom to the film surface, and (2) the blooming of the sbp agent to the surface of the film can adversely affect the pπntabibty of the film, as ink adhesion can be reduced by the presence of the sbp agent. Thus, it would be desirable to provide a ftlm which exhibits a low film-to-film coefficient of friction, as well as a low film-to-equipment/ metal coefficient of fπchon, along with good antiblock properties, without having loose dust on the surface of the im. It would be shll more desirable to provide a film which exhibits low film-to-film coefhcient of fπchon without fhe presence of a sbp agent which interferes with the pπntabibty of the film. SUMMARY OF THE INVENTION It has been discovered that a desired combination of slip and antiblock characteristics can be achieved by providing the outer surface(s) of a film with a combination of substantially lamellar parhculates and substanhally spherical parhculates. Although inorganic parhculates are believed to be preferred, it is believed that substantially spherical and substanhally lamellar organic par culates could also be beneficially used. The substantially lamellar particulates are believed to provide the desired slip characteristics, while the substanhally spherical parhculates are believed to provide the desired anhblock charactenstics. Furthermore, if a convenhonal wax-type slip agent is not used in the him of the invention, the slip characteristics can be obtained immediately upon formation of the film, rather than requiring time to bloom to the surface of the film As a hrst aspect, the present invention is directed to a film containing a composihon. The composihon comprises a mixture which compπses inorganic substanhally spherical parhculates, and inorganic substanhally lamellar particulates The substanhally spheπcal parhculates and the substantially lamellar particulates are present in an outer film layer and on an outer surface of the him. The substantially spherical parhculates preferably have an average particle size of from about 0.1 to 30 microns; more preferably, from about 1 to 20 microns; shll more preferably, from about 3 to 10 microns, and yet still more preferably, from about 3 o 4 microns. Preferably, the inorganic substantially lamellar parhculates have an average aspect ratio, based on either length to thickness, or on diameter to thickness, of at least about 5:1, and preferably the average aspect ratio is as high as possible. Presently, the available lamellar parhculates have an average aspect ratio of from about 5:1 to 20.1 However, if available, preferably the lamellar parhculates preferably have an average aspect ratio of from about 5:1 to 100.1, more preferably, from about to 10:1 to 50:1; still more preferably, about 20 1 (as 20:1 is the most common average aspect ratio currently available). Preferably, the inorganic substanhally lamellar particulates also have a major dimension, i.e., largest dimension, of from about 0.1 to 15 microns; more preferably, from about 1 to 10 microns; still more preferably, from about 1 to 8 microns. The substantially spherical particulates and the substantially lamellar particulates are present together in an outer film layer and on an outer surface of the film. Preferably, the mixture is a substantially homogeneous mixture of the substantially spherical particulates and the substantially lamellar particulates. Preferably, the substantially lamellar particulates have a hardness of from about 1 to 7, on a Mohs hardness scale; more preferably, from about 1 to 5; still more preferably from about 1 to 3. Preferably, the composition further comprises a slip enhancer comprising at least one member selected from the group consisting of fatty acid amide, oxidized polyethylene, fatty acid ester, and fatty acid alcohol. More preferably, the slip enhancer comprises at least one member selected from the group consisting of erucamide, oleamide, stearamide, behenamide, oxidized polyethylene wax, glycerol monostearate, metallic stearate. Calcium stearate is a particularly preferred metallic stearate, and ethylene bis-stearamide is a particularly preferred stearamide. Preferably, the slip enhancer is present in the outer film layer in an amount of from about 50 to 10,000 parts per million, based on the weight of the outer layer; more preferably, from about 100 to 5,000 ppm; still more preferably, from about 200 to 1000 ppm; and yet still more preferably, from about 200 to 800 ppm. The composition may further comprise a printability enhancer comprising a polar polymer. Preferably, the polar polymer compπses at least one member selected from the group consisting of ethylene/ ester/ maleic anhydride terpolymer, ethylene/ ester/ glycidyl methacrylate terpolymer, and ethylene/ acrylic acid copolymer. Preferably, the printability enhancer is present in the outer film layer in an amount of from about 1 to 25 percent, based on the weight of the outer film layer; more preferably, from about 2 to 20 percent; still more preferably, from about 5 to 15 percent; yet still more preferably, from about 5 to 10 percent. Preferably, the substantially spherical particulates are present in the outer layer of the film at a concentration of from about 500-50,000 parts per million, based on the weight of the outer film layer; more preferably, from about 1,000 to 30,000 ppm; still more preferably, from about 2,000 to 20,000 ppm; and yet still more preferably, from about 4,000 to 8,000 ppm. Preferably, the substantially lamellar particulates are present in the outer layer of the film at a concentration of from about 500 to 50,000 parts per million, based on the weight of the outer film layer; more preferably, from about 1000 to 30,000 ppm; still more preferably, from about 1,000 to 20,000 ppm; and yet still more preferably, from about 2,000 to 4,000 ppm. Preferably, the substantially spherical particulates comprise at least one member selected the group consisting of silica and silicate; more preferably, at least one member selected the group consisting of natural silica, synthetic silica, and silicate; and still more preferably, at least one member selected the group consisting of diatomaceous earth, fumed synthetic silica, precipitated synthetic silica, gelled synthetic silica, sodium calcium silicate, and sodium calcium aluminum silicate. Preferably, the substantially lamellar particulates comprise silicate; more preferably, at least one member selected the group consisting of magnesium silicate and hydrated aluminum silicate; still more preferably, at least one member selected from the group consisting of talc and kaolin. Although the him of the present invention can be a monolayer film, preferably the film is a multilayer film. More preferably, the multilayer film comprises an 0 2 -barrier layer comprising at least one member selected from the group consisting of polyvinylidene chloride, ethylene/ vinyl alcohol copolymer, polyamide, and polyester. More preferably, the multilayer film comprises an outer first layer, an inner second layer, and an outer third layer. The outer first layer preferably comprises at least one member selected from the group consisting of ethylene/vinyl acetate copolymer, ethylene/alpha-olefin copolymer, and polyamide; the inner second layer is the 0 2 -barπer layer, and comprises at least one member selected from the group consisting of polyvinylidene chloride, ethylene/vinyl alcohol copolymer, polyamide, and polyester. The outer third layer preferably comprises at least one member selected from the group consisting of ethylene/vinyl acetate copolymer, ethylene/alpha-olefin copolymer, and polyamide. A preferred embodiment of this preferred multilayer film further comprises a fourth layer between the first layer and the second layer. The fourth layer comprises at least one member selected from the group consisting of ethylene/vinyl acetate copolymer, ethylene/alpha-olefin copolymer, and polyamide. In this film, the first layer and the fourth layer preferably each comprise crosslmked polymer, and the second layer and the third layer do not compπse crosslmked polymer. In yet another embodiment, the multilayer film further comprises a fifth layer and a sixth layer. The fifth layer is a hrst e layer compnsmg at least one member selected from the group consisting of ethylene/ carboxyhc acid copolymer, ethylene/ ester copolymer, and anhydride-modified ethylene/ alpha-olefm copolymer. The sixth layer is a second he layer comprising at least one member selected from the group consistmg of ethylene/carboxybc acid copolymer, ethylene/ ester copolymer, and anhydride-modified ethylene/alpha-olefin copolymer. The fifth layer is between the fourth layer and the second layer, and the sixth layer is between the second layer and the third layer. Preferably, all layers of the multilayer film compose crosslinked polymer. Another preferred embodiment of the three-layer film described above further comprises a fourth layer. The fourth layer is a he layer and comprises at least one member selected from the group consisting of ethylene/carboxybc acid copolymer, ethylene/ ester copolymer, and anhydride modihed ethylene/alpha-olefin copolymer. Preferably, the fourth layer is a first he layer and is between the hrst layer and the second layer, and the film further comprises a hfth layer, the fifth layer bemg a second he layer, the fifth layer compnsmg at least one member selected from the group consisting of ethylene/carboxybc acid copolymer, ethylene/ester copolymer, and anhydride modihed ethylene/ alpha-olefm copolymer, the fifth layer bemg between the second layer and the third layer. One preferred multilayer him according to the present mvention is substanhally symmetrical with respect to both layer thickness and layer chemical composition. Preferably, the film has a total free shrink, at 185°F, of from about 10 to 100 percent; more preferably, from about 10 to 80 percent; shll more preferably, from about 20 to 60 percent. Preferably, the im is biaxially oπented. Preferably, the film comprises crosslmked polymer As a second aspect, the present mvention is directed to a film tube compnsmg the him as set forth above. One preferred him tube has a dustless tube outside surface havmg the composihon as set forth above, and a tube inside surface havmg dust thereon. Preferably, the dust comprises at least one member selected from the group consisting of alummum silica, silicon dioxide, sodium calcium alumino silicate, magnesium silicate, and calcium silicate; more preferably, the dust comprises at least one member selected from the group consisting of corn starch, potato starch, talc, and silica. The tube can be seamless or comprise a longitudmal seam. The longitudmal seam can comprise a lap seal, a fin seal, or a butt seal with a backseaming tape. As a third aspect, the present invention is directed to bags (both end-seal bags and side- seal bags) and casmgs (both seamless casings and backseamed casings) compnsmg the film or tube accordmg to the invention. The present invention is also directed to packages compnsmg a product packaged in a bag or casing compnsmg the film or tube accordmg to the present invention. Typical products mclude meat, preferably beef, pork, foul, hsh, lamb, etc., both fresh as well as processed, e.g., sausage. As a fourth aspect, the present mvention relates to a composihon of matter compnsmg a thermoplastic polymer, inorganic substantially spherical particulates, and inorganic substantially lamellar particulates. The inorganic substantially spherical particulates have an average particle size of from about OJ to 30 microns. The inorganic substantially lamellar particulates have an average aspect ratio of from about 5:1 to 40:1, and a major dimension of from about OJ to 15 microns. Preferably, the polymer comprises ethylene/alpha-olefin copolymer, more preferably, the polymer consists of ethylene/alpha- olefin copolymer. For a dispersion concentrate, preferably the polymer is present in an amount of from about 70 to 99.9 weight percent, based on the weight of the composition, with the inorganic particulates present in an amount of from about OJ to 30 weight percent, based on the weight of the composition. More preferably, the polymer is present in an amount of from about 85 to 95 weight percent, based on the weight of the composition, with the inorganic particulates present in an amount of from about 5 to 15 weight percent, based on the weight of the composition. In a final product, preferably the polymer is present in an amount of from about 95 to 99.9 weight percent, based on the weight of the composition, with the inorganic particulates are present in an amount of from about 0.1 to 5 weight percent, based on the weight of the composition. More preferably, the polymer is present in an amount of from about 98.5 to 99.5 weight percent, based on the weight of the composition, with the inorganic particulates present in an amount of from about 0.5 to 1.5 weight percent, based on the weight of the composition. BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 illustrates a schematic cross-sectional view of a preferred multilayer film according to the present invention. Figure 2 illustrates a schematic view of a process for producmg multilayer films in accordance with the present invention. DETAILED DESCRIPTION OF THE INVENTION As used herein, the term "film" is used in a generic sense to include plastic web, regardless of whether it is film or sheet. As used herein, the term "package" refers to a product packaged in a packaging material, such as a film. As used herein, the phrases "seal layer", "sealing layer", "heat seal layer", and "sealant layer", refer to an outer film layer, or layers, involved in the sealing of the film to itself, another film layer of the same or another im, and/ or another article which is not a film. It should also be recognized that in general, up to the outer 3 mils of a film can be involved m the sealing of the fibn to itself or another layer. With respect to packages havmg only fin-type seals, as opposed to lap- type seals, the phrase "sealant layer" generally refers to the mside film layer of a package, as well as supporting layers withm 3 mils of the mside surface of the sealant layer, the mside layer frequently also serving as a food contact layer in the packaging of foods. As used herem, the term "seal" refers to any seal of a first region of a film surface to a second region of a film surface, wherem the seal is formed by heatmg the regions to at least their respective seal initiation temperatures. The heatmg can be performed by any one or more of a wide vaπety of manners, such as usmg a hot wire, hot knife, heated bar, hot air, mfrared radiahon, ultrasonic sealing, etc. More preferably, the seal is formed by hot wire and/ or hot knife. As is known to those of skill in the art, a static lap seal is another seal useful in forming a package from the film of the present mvenhon. As used herem, the phrase "...present an outer film layer and on an outer surface of the film..." refers to an outer fibn layer which has the recited components withm the cross-section of the layer, as well as on the outer surface of the him As used herem, the term "oriented" refers to a polymer-contammg material which has been stretched at an elevated temperature (the onentation temperature), followed by bemg "set" m the stretched configuration by cooling the mateπal while substanhally retammg the stretched dimensions. Upon subsequently heatmg unrestrained, unannealed, oπented polymer-contammg matenal to its onentation temperature, heat shrinkage is produced More particularly, the term "onented", as used herem, refers to onented films, wherein the orientation can be produced m one or more of a vaπety of manners. As used herem, the phrase "onentation ratio" refers to the mulhphcation product of the extent to which the plashc film material is expanded in several direchons, usually two direchons perpendicular to one another Expansion in the machine direction is herem referred to as "drawing", whereas expansion the transverse direction is herein referred to as "stretching". For hlms extruded through an annular die, stretching is obtained by "blowing" the film to produce a bubble. For such films, drawing is obtamed by passing the him through two sets of powered nip rolls, with the downstream set havmg a higher surface speed than the upstream set, with the resulting draw raho bemg the surface speed of the downstream set of nip rolls divided by the surface speed of the upstream set of nip rolls. The degree of orientation is also referred to as the onentation raho, or sometimes as the "racking ratio" As used herein, the term "monomer" refers to a relatively simple compound, usually containing carbon and of low molecular weight, which can react to form a polymer by combining with itself or with other similar molecules or compounds. As used herein, the term "comonomer" refers to a monomer which is copolymerized with at least one different monomer in a copolymerization reaction, the result of which is a copolymer. As used herein, the term "polymer" refers to the product of a polymerization reaction, and is inclusive of homopolymers, copolymers, terpolymers, etc. In general, the layers of a fibn can consist essentially of a single polymer, or can have still additional polymers together therewith, i.e., blended therewith. As used herein, the term "copolymer" refers to polymers formed by the polymerization reaction of at least two different monomers. For example, the term "copolymer" includes ti e copolymerization reaction product of ethylene and an alpha-olefin, such as 1-hexene. However, the term "copolymer" is also inclusive of, for example, the copolymerization of a mixture of ethylene, propylene, 1-hexene, and 1-octene. As used herein, a copolymer identified in terms of a plurahty of monomers, e.g., "propylene/ethylene copolymer", refers to a copolymer in which either monomer may copolymerize in a higher weight or molar percent than the other monomer or monomers. However, the first hsted monomer preferably polymerizes in a higher weight percent than the second listed monomer, and, for copolymers which are terpolymers, quadripolymers, etc., preferably the first monomer copolymerizes in a higher weight percent than the second monomer, and preferably the second monomer copolymerizes in a higher weight percent than the third monomer, etc. As used herein, copolymers are identified, i.e, named, in terms of the monomers from which the copolymers are produced. For example, the phrase "propylene/ethylene copolymer" refers to a copolymer produced by the copolymerization of both propylene and ethylene, with or without additional comonomer(s). As used herein, the word "mer" refers to a unit of a polymer, as derived from a monomer used in the polymerization reaction. For example, the phrase "alpha-olehn polymerization units" refers to a unit in, for example, an ethylene/ alpha-olehn copolymer, the polymerization unit bemg that "residue" which is derived from the alpha-olefin monomer after it reacts to become a portion of the polymer chain, i.e., that portion of the polymer contributed by an individual alpha-olehn monomer after it reacts to become a portion of the polymer chain. As used herein, terminology employing a "/" with respect to the chemical identity of a copolymer (e.g., "an ethylene/alpha-olefin copolymer"), identifies the comonomers which are copolymerized to produce the copolymer. As used herein, "ethylene alpha-olefin copolymer" is the equivalent of "ethylene/alpha-olefin copolymer." As used herein, the phrase "heterogeneous polymer" refers to polymerization reaction products of relatively wide variation in molecular weight and relatively wide variation in composition distribution, i.e., typical polymers prepared, for example, using conventional Ziegler- Natta catalysts. Heterogeneous polymers are useful in various layers of the film used in the present invention. Although there are a few exceptions (such as TAFMER (TM) linear homogeneous ethylene/alpha-olefin copolymers produced by Mitsui Petrochemical Coφoration, using Ziegler-Natta catalysts), heterogeneous polymers typically contain a relatively wide variety of chain lengths and comonomer percentages. As used herein, the phrase "homogeneous polymer" refers to polymerization reaction products of relatively narrow molecular weight distribution and relatively narrow composition distribution. Homogeneous polymers are useful in various layers of the multilayer film used in the present invention. Homogeneous polymers are structurally different from heterogeneous polymers, in that homogeneous polymers exhibit a relatively even sequencing of comonomers within a chain, a mirroring of sequence distribution in all chains, and a similarity of length of all chains, i.e., a narrower molecular weight distribution. Furthermore, homogeneous polymers are typicaUy prepared using metallocene, or other single-site type catalysis, rather than using Ziegler Natta catalysts. More particularly, homogeneous ethylene/ alpha-olehn copolymers may be characterized by one or more methods known to those of skill in the art, such as molecular weight distribution (M„/M n ), composition distribution breadth index (CDBI), and narrow melting point range and single melt point behavior. The molecular weight distribution (M w /M n ), also known as polydispersity, may be deterrnined by gel permeation chromatography. The homogeneous ethylene/alpha-olefin copolymers useful in this invention generally has (M w /M n ) of less than 2.7; preferably from about 1.9 to 2.5; more preferably, from about 1.9 to 2.3. The composition distribution breadth index (CDBI) of such homogeneous ethylene/alpha-olefin copolymers will generally be greater than about 70 percent. The CDBI is defined as the weight percent of the copolymer molecules having a comonomer content within 50 percent (i.e., plus or minus 50%) of the median total molar comonomer content. The CDBI of linear polyethylene, which does not contain a comonomer, is defined to be 100% . The Composition Distribution Breadth Index (CDBI) is determined via the technique of Temperature Rising Elution Fractionation (TREF). CDBI determination clearly distinguishes the homogeneous copolymers used in the present invention (narrow composition distribution as assessed by CDBI values generally above 70%) from heterogeneous polymers such as VLDPE's which are available commercially which generally have a broad composition distribution as assessed by CDBI values generally less than 55%. The CDBI of a copolymer is readily calculated from data obtained from techniques known in the art, such as, for example, TREF as described, for example, in Wild et. al., }. Poly. Sci. Poly. Phvs. Ed.. Vol. 20, p.441 (1982). Preferably, the homogeneous ethylene/alpha-olefin copolymers have a CDBI greater than about 70%, i.e., a CDBI of from about 70% to 99%. Such homogeneous polymers exhibit a relatively narrow melting point range, in comparison with "heterogeneous copolymers", i.e., polymers having a CDBI of less than 55%. Preferably, the homogeneous ethylene/alpha-olefin copolymers exhibit an essentially singular melting point characteristic, with a peak melting point (T m ), as determined by Differential Scanning Colorimetry (DSC), of from about 60°C to 105°C. Preferably the homogeneous copolymer has a DSC peak T m of from about 80°C to 100°C. As used herein, the phrase "essentially single melting point" means that at least about 80%, by weight, of the material corresponds to a single T m peak at a temperature within the range of from about 60°C to 105°C, and essentially no substantial fraction of the material has a peak melting point in excess of about 115°C, as determined by DSC analysis. DSC measurements are made on a Perkin Elmer System 7 Thermal Analysis System. Melting information reported are second melting data, i.e., the sample is heated at a programmed rate of 10°C./min. to a temperature below its critical range. The sample is then reheated (2nd melting) at a programmed rate of 10°C/min. The presence of higher melting peaks is detrimental to film properties such as haze, and compromises the chances for meaningful reduction in the seal initiation temperature of the final film. A homogeneous ethylene/alpha-olefin copolymer can, in general, be prepared by the copolymerization of ethylene and any one or more alpha-olefin. Preferably, the alpha-olefin is a C3- 0 alpha-monoolefin, more preferably, a Cj-Cι 2 alpha-monoolehn, still more preferably, a Q- Cβ alpha-monoolefin. Still more preferably, the alpha-olehn compπses at least one member selected from the group consisting of butene-1, hexene-1, and octene-1, i.e., l-butene, 1-hexene, and 1-octene, respectively. Most preferably, the alpha-olehn comprises octene-1, and/ or a blend of hexene-1 and butene-1. Processes for preparing and using homogeneous polymers are disclosed in U.S. Patent No. 5,206,075, U.S. Patent No. 5,241,031, and PCT lntemational Apphcation WO 93/03093, each of which is hereby incoφorated by reference thereto, in its entirety. Further details regarding the production and use of homogeneous ethylene/alpha-olefin copolymers are disclosed in PCT International Publication Number WO 90/03414, and PCT International Pubhcation Number WO 93/03093, both of which designate Exxon Chemical Patents, Inc. as the Apphcant, and both of which are hereby incoφorated by reference thereto, their respective entireties. Still another genus of homogeneous ethylene/ alpha-olehn copolymers is disclosed in U.S. Patent No. 5,272,236, to LAI, et. al, and U.S Patent No. 5,278,272, to LAI, et al., both of which are hereby incoφorated by reference thereto, in their respective entireties. As used herem, the term "polyolefin" refers to any polymeπzed olefin, which can be hnear, branched, cychc, ahphatic, aromatic, substituted, or unsubstituted More specifically, mcluded in the term polyolefin are homopolymers of olefin, copolymers of olefm, copolymers of an olefin and a non-olefinic comonomer copolymerizable with the olef , such as vmyl monomers, modified polymers thereof, and the bke Specific examples include polyethylene homopolymer, polypropylene homopolymer, polybutene, ethylene/alpha-olehn copolymer, propylene/ alpha- olehn copolymer, butene/alpha-ole n copolymer, ethylene/vinyl acetate copolymer, ethylene/ ethyl acrylate copolymer, ethylene/ butyl acrylate copolymer, ethylene/ methyl acrylate copolymer, ethylene/ aery he acid copolymer, ethylene/ methacryhc acid copolymer, modified polyolefin resm, ionomer resm, polymethylpentene, etc Modihed polyolefin resm is mclusive of modified polymer prepared by copolymerizing the homopolymer of the olefm or copolymer thereof with an unsaturated carboxyhc acid, e g , maleic acid, fumanc acid or the like, or a denvative thereof such as the anhydride, ester or metal salt or the like. It could also be obtamed by incoφorating mto the olefm homopolymer or copolymer, an unsaturated carboxyhc acid, e.g., maleic acid, fumanc acid or the like, or a deπvative thereof such as the anhydnde, ester or metal salt or the like. As used herem, terms identifymg polymers, such as "polyamide", "polyester", "polyurethane", etc. are mclusive of not only polymers comprising repeatmg units deπved from monomers known to polymerize to form a polymer of the named type, but are also mclusive of comonomers, denvahves, etc. which can copolymerize with monomers known to polymerize to produce the named polymer. For example, the term "polyamide" encompasses both polymers compnsmg repeating units derived from monomers, such as caprolactam, which polymerize to form a polyamide, as well as copolymers denved from the copolymerization of caprolactam with a comonomer which when polymeπzed alone does not result in the formation of a polyamide. Furthermore, terms identifying polymers are also inclusive of mixtures, blends, etc. of such polymers with other polymers of a different type More preferably, however, the polyolefin is a the polymerization product of one or more unsubstituted olefins, the polyamide is ti e polymerization product of one or more unsubstituted amides, etc As used herein, the phrase "ethylene alpha-olehn copolymer", and "ethylene/alpha-olefin copolymer", refer to such heterogeneous materials as linear low density polyethylene (LLDPE), and very low and ultra low density polyethylene (VLDPE and ULDPE); and homogeneous polymers such as metallocene-catalyzed EXACT (TM) linear homogeneous ethylene/ alpha olefin copolymer resins obtainable from the Exxon Chemical Company, of Baytown, Texas, and TAFMER (TM) linear homogeneous ethylene/alpha-ole n copolymer resins obtainable from the Mitsui Petrochemical Coφoration. All these materials generally include copolymers of ethylene with one or more comonomers selected from Ct to Cio alpha-olefin such as butene-1 (Le., 1- butene), hexene-1, octene-1, etc. in which the molecules of the copolymers comprise long chains with relatively few side chain branches or cross-linked structures. This molecular structure is to be contrasted with conventional low or medium density polyethylenes which are more highly branched than their respective counteφarts. The heterogeneous ethylene/alpha-olefin commonly known as LLDPE has a density usuaUy in the range of from about 0.91 grams per cubic centimeter to about 0.94 grams per cubic centimeter. Other ethylene/alpha-olehn copolymers, such as the long chain branched homogeneous ethylene/alpha-ole n copolymers available from The Dow Chemical Company, known as AFFINITY (TM) resms, are also included as another type of homogeneous ethylene/ alpha-olefin copolymer useful in the present invention. In general, the ethylene/alpha-olefin copolymer comprises a copolymer resulting from the copolymerization of from about 80 to 99 weight percent ethylene and from 1 to 20 weight percent alpha-olefin. Preferably, the ethylene/alpha-olehn copolymer comprises a copolymer resulting from the copolymerization of from about 85 to 95 weight percent ethylene and from 5 to 15 weight percent alpha-olehn. As used herein, the phrases "inner layer" and "internal layer" refer to any layer, of a multilayer film, having both of its principal surfaces directly adhered to another layer of the film. As used herein, the phrase "outer layer" refers to any film layer of film having less than two of its principal surfaces directly adhered to another layer of the him. The phrase is mclusive of monolayer and multilayer films. In multilayer films, there are two outer layers, each of which has a principal surface adhered to only one other layer of the multilayer film. In monolayer films, there is only one layer, which, of course, is an outer layer in that neither of its two principal surfaces are adhered to another layer of the film. As used herein, the phrase "inside layer" refers to the outer layer, of a multilayer film packaging a product, which is closest to the product, relative to the other layers of the multilayer film. "Inside layer" also is used with reference to the innermost layer (which is also an outer layer) of a plurahty of concentricaUy arranged layers extruded through one or more annular dies. As used herem, the phrase "outside layer" refers to the outer layer, of a multilayer fibn packaging a product, which is furthest from the product relahve to the other layers of the multilayer film. "Outside layer" also is used with reference to the outermost layer of a plurahty of concentncaUy arranged layers extruded through one or more annular dies. As used herem, the phrase "machine direction", herem abbreviated "MD", refers to a direction "along the length" of the im, i.e., the direction of the film as the him is formed dunng extrusion and/ or coating. As used herem, the phrase "transverse direction", herem abbreviated "TD", refers to a direction across the film, peφendicular to the machine direction. As used herem, the phrase "free shnnk" refers to the percent dimensional change m a 10 cm x 10 cm specimen of film, when shrunk at 200°F, with the quantitative determination bemg earned out accordmg to ASTM D 2732, as set forth in the 1990 Annual Book of ASTM Standards, Vol. 08.02, pp.368-371, which is hereby incoφorated, in its entirety, by reference thereto. Although the him preferably has a film-to-film coefhcient of fπchon of from about 0.1 to 0.9, more preferably the fibn has a film-to-film coefhcient of fnction of from about 0J to 0.7, stiU more preferably, from about OJ-0.6, and yet stiU more preferably, from about 0.1 to 0.5. Although the film of the present mvention can be either a monolayer film or a multilayer film, preferably the im is a multilayer him. Preferably, the him has a total thickness of less than about 20 mils, more preferably the im has a total thickness of from about 0.2 to 10 mils, still more preferably from about 0.3 to 5 mils, and yet still more preferably, from about 1.5 to 4 mils Some of the multilayer films of the present invention are preferably irradiated to mduce crosslinking. In the irradiation process, the fibn is subjected to an energetic radiation treatment, such as corona discharge, plasma, flame, ultraviolet, X-ray, gamma ray, beta ray, and high energy electron treatment, which mduce cross-lmkmg between molecules of the irradiated material. The irradiation of polymeπc films is disclosed in U.S. Patent No 4,064,296, to BORNSTEIN, et. al., which is hereby incoφorated m its entirety, by reference thereto BORNSTEIN, et. al. discloses the use of ionizing radiahon for crosslinking the polymer present m the him. To produce crosslinking, a suitable radiation dosage of high energy electrons, preferably usmg an electron accelerator, with a dosage level bemg determined by standard dosimetry methods. Other accelerators such as a Van de Graaf generator or resonating transformer may be used. The radiahon is not limited to electrons from an accelerator smce any ionizing radiahon may be used. The ionizing radiahon can be used to crosslink the polymers m the film. Preferably, the film is irradiated at a level of from 2-15 MR, more preferably 2-10 MR. As can be seen from the descriptions of preferred films for use m the present mvention, the most preferred amount of radiahon is dependent upon the film composihon, thickness, etc., and its end use. Figure 1 illustrates a cross-sectional view of a preferred multilayer film 20. First layer 21 is an outer fi n layer which preferably serves as an mside food-contact layer which is irradiated so that it is grease-resistant. Second layer 22 serves as a bulk layer, and is preferably irradiated. Third layer 23 serves as a to O 2 . Fourth layer 24 is an outer layer which preferably serves as an outside abuse layer, and which, preferably, is also grease-resistant. One preferred embodiment of multilayer im 20 has a physical structure, in terms of number of layers, layer thickness, and layer arrangement, and a chemical composihon terms of the various polymers, etc. present in each of the layers, as set forth m Table I, below. This film is herem designated "Film No. 1", and is an example of a multilayer im accordmg to the present invention. TABLE 1 (Identity of Films of Examples 1-9) Figure 1 Layer Layer Function Layer Chemical Identity Layer Thickness (mils) Designation 24 outside, grease-resistant, 90% EVA; 9% 0.35 and abuse-resistant ethylene/alpha-olehn copolymer; 1 % sbp and antiblock inorganic parhculates 23 0 2 -barner PVDC Blend 0.2 22 bulk irradiated EVA 1.21 21 grease-resistance & irradiated EVA 0.54 sealing EVA was ELVAX 3128 (TM) ethylene/ v yl acetate copolymer havmg a vmyl acetate content of 8.9%, a melt mdex of 2.0, and a density of 0.928 g/cc, obtamed from EJ DuPont de Nemours, of Wilmington, Delaware. PVDC Blend was a composihon comprising: (a) about 96 weight percent DOW MA134 (TM) vinylidene chloride/ methyl acrylate copolymer havmg a methyl acrylate content of 8.5%, obtained from The Dow Chemical Company, of Midland, Michigan; (b) about 2 weight percent PLAS CHEK 775 (TM) epoxidized soybean oil, obtamed from Ferro Chemicals, of Bedford, Ohio; and, (c) about 2 weight percent METABLEN L1000 (TM) acrylate blend, obtamed from Elf Atochem, of Philadelphia, Pennsylvania. METABLEN L1000 (TM) compπses about 53 weight percent methyl methacrylate ("MMA"), 29 weight percent butylmethacrylate ("BMA"), and 19 weight percent butyl acrylate ("BA"). In Table 1 above, im layer 24 was formed by providmg an extruder with 90% EVA and 10% of a preblended mixture compnsmg the 9% ethylene/alpha-olehn copolymer and the 1% sbp and antiblock inorganic particulates. The ethylene/alpha-olehn copolymer was ESCORENE LD203.48 (TM) low density polyethylene homopolymer, obtamed from Exxon Chemicals, Incoφorated, of Baytown, Texas. The preblend of the ethylene/alpha-olehn copolymer and inorganic particulates can be compounded usmg a twin-screw compounder, a Banbury mixer, or any other blending apparatus as known to those of skill in the art Film No. 1 was produced m accordance with a process schemafacaUy illustrated m Figure 2. In the process lUustrated in Figure 2, sohd polymer beads (not illustrated) are fed to a plurahty of extruders 28 (for simplicity, only one extruder is illustrated) Inside extruders 28, the polymer beads are forwarded, melted, and degassed, foUowing which the resulting bubble-free melt is forwarded mto die head 30, and extruded through an annular die, resulting m tubmg 32 which is preferably about 24 mils thick. After cooling or quenching by water from coolmg ring 34, tubmg 32 is coUapsed by pmch roUs 36, and is thereafter fed through irradiation vault 38 surrounded by shielding 40, where tubmg 32 is irradiated with high energy elections (I e , ionizing radiation) from iron core transformer accelerator 42. Tubmg 32 is guided through irradiation vault 38 on roUs 44. Preferably, tubmg 32 is irradiated to a level of from about 3 to 8 MR After irradiation, irradiated tubing 46 is directed through pinch roUs 48, foUowmg which irradiated tubmg 46 is slightly mflated, resulting in trapped bubble 50 However, at trapped bubble 50, the tubmg is not significantly drawn longitudinally, as the surface speed of nip roUs 52 are about the same speed as nip roUs 48 Furthermore, irradiated tubmg 46 is mflated only enough to provide a substanhaUy circular tubmg without significant transverse onentation, ι.e., without stretching. Slightly mflated, irradiated tubmg 50 is passed through vacuum chamber 54, and thereafter forwarded through coatmg die 56 Second tubular him 58 is melt extiuded from coatmg die 56 and coated onto slightly mflated, irradiated tube 50, to form two-ply tubular film 60. Second tubular him 58 preferably comprises an 0 2 barner layer, which does not pass through the ionizing radiahon. Further details of the above-described coating step are generaUy as set forth U.S. Patent No 4,278,738, to BRAX et. al , which is hereby incoφorated by reference thereto, m its entirety. After irradiation and coating, two-ply tubing film 60 is wound up onto windup roU 62. Thereafter, windup roU 62 is removed and installed as unwind roU 64, on a second stage in the process of making the tubing film as ultimately desired. Two-ply tubular film 60, from unwind roll 64, is unwound and passed over guide roU 66, after which two-ply tubular film 60 passes into hot water bath tank 68 containing hot water 70. The now coUapsed, irradiated, coated tubular film 60 is submersed in hot water 70 (having a temperature of about 185°F) for a retention time of at least about 30 seconds, i.e., for a time period in order to bring the film up to the desired temperature for biaxial orientation. Thereafter, irradiated tubular film 60 is directed through nip rolls 72, and bubble 74 is blown, thereby transversely stretching tubular film 60. Furthermore, while being blown, i.e., transversely stretched, nip roUs 76 dra w tubular film 60 in the longitudinal direction, as nip roUs 76 have a surface speed higher than the surface speed of nip rolls 72. As a result of the transverse stretching and longitudinal drawing, irradiated, coated biaxiaUy-oriented blown tubing fibn 78 is produced, this blown tubing preferably having been both stretched in a ratio of from about 1:1.5 - 1:6, and drawn in a ratio of from about 1:1.5-1:6. More preferably, the stretching and drawing are each performed a ratio of from about 1:2 - 1:4. The result is a biaxial orientation of from about 1:2.25 - 1:36, more preferably, 1:4 - 1:16. WhUe bubble 74 is maintained between pinch roUs 72 and 76, blown tubing 78 is collapsed by rolls 80, and thereafter conveyed through pinch roUs 76 and across guide roU 82, and then rolled onto wind-up roU 84. Idler roU 86 assures a good wind-up. A total of 9 films were made in accordance with the film of Table 1, using the process as schematicaUy iUustiated in Figure 2, as described immediately above. The films of Examples 1-9 varied in the content of the inorganic particulate additives, i.e., the him of Control Example No. 1 contained no inorganic particulates in outer layer 24, while Comparative Examples 2-4 contained only one type of inorganic particulate (i.e., either spheπcal or l mellar, but not both) in outer layer 24, with working Examples 5-9 containing a mixture of spherical and lameUar inorganic particulates in outer layer 24. Each of the hlms of Examples 1-9 was a 4-layer with each layer consisting of the polymers as set forth in Table 1. TABLE 2 Example No. Identity of Additive Static Coefficient of Kinetic Coefficient Machin-ability Friction of Friction Score (x/15; x= ) 1 (Control) None Blocked 1.5 3 2 (Comparative) talc 0.65 0.38 3 3 (Comparative) sihca 0.35 0.25 6 4 (Comparative) sιbcate-1 0.38 0.25 10 5 talc + sibca 0.45 0.25 15 6 talc + sύica 0.54 0.42 15 7 talc + sιhcate- 0.41 0.27 13 8 talc + sihca + EA 0.42 0.25 15 9 talc + silicate + 0.37 0.24 15 EA In each of Examples 1-9, the addihves were incoφorated mto the outside layer of the him tube, and m each case the film structure was as set forth in Table 1 above. Examples 2-4 contamed 5,000 ppm of each addihve. Examples 5-7 contamed 2,000 ppm talc and 5,000 ppm of the second addihve, ι.e., sihca for Examples 5 and 6, and sιhcate-1 for Example 7. Examples 8 and 9 contamed 800 ppm erucarrude (EA) m addition to 2,000 ppm talc and 5,000 ppm sihca. The talc used was ABT-2500 (TM) Mg3(Sι 2 0 5 ).[OH] 2 or MICROBLOC (TM) Mgι(Sι 2 θ5).[OH] 2/ obtamed from Barretts Mmerals Inc., of Ddlon, Montana. The sihca used was SYLOBLOC 47 (TM) Sι0 2 , obtamed from W.R. Grace & Co. - CONN. Davison Division. The sιhcate-1 used was NaCaAl(Sι 2 C>7), obtamed from Mizusawa Industrial Chemicals, sold through International Resources of Columbia, Maryland Machinability was determmed on a bag converting machine operating at a commercial speed. Machinabihty score represents a quabtahve assessment of performance dunng the feed g of the tubmg, seahng of the tubmg duπng conversion to bags, the stacking of the bags, and conveymg of the bags. Regarding the feeding of the tubing it is important that the him passes freely through the seahng station without jamming due to drag force between the film and the support (which is usuaUy stamless steel) which is too high, or due to sticking on the seal jaws. Bags are "stacked" in a shmgled relahonship to one another after they are formed by seahng and cutting. These stacked bags need to maintain a relatively straight, ahgned relationship, ι.e., without bags bemg shifted sideways, out of ahgnment along the length of the stream of shmgled bags. Regardmg the conveymg of the bags, it is important to be able to sample the bags without disturbing the straight hne relahonship of the shmgled bags If the coefhcient of fnction between the bags is too high, removmg one or more bags results m disruption of the stiaight hne relahonship of the hne of shmgled bags. For each of these three cπtena, a qualitative score of 1-5 is assessed, with 1 representing poor performance and 5 representing exceUent performance. As can be seen m Table 2, the Machmabihty score is a total of these three ratings for the performance of the film of the respective example. The coefficient of fnction (COF) was determined per ASTM D 1894, hereby incoφorated by reference thereto, in its entirety. The data provided m Table 2, above, demonstrates that films accordmg to the present mvention, ι.e., the hlms of Examples 5-9, exhibit a higher Machmabihty score than the hlms of Comparative Examples 1-4. Thus, Table 2 provides evidence that hlms according to the present invention provide improved performance in the area of Machmabihty, which is believed to be related to the combmahon of sbp and antiblock charactenshcs derived from the combmahon of lameUar and spheπcal particulates present m the outside film layer. The comparative films of Examples 1-4 were substantiaUy identical except that they had, with respect to the presence of inorganic parhculates m the outer layer and on the outer surface of the film: (a) no parhculates, (b) only spheπcal particulates, or (c) only lameUar parhculates. The results set forth in Table 2 demonstrate that without loose dust on the outside surface of the film, the combmation of spherical and lamellar particulates in the outer layer and on the outer surface of the him provides the film with slip and antiblock properties which are improved over no parhculates in the outer layer and on the outer surface, the presence of spheπcal parhculates on the outer surface, without lamellar particulates; and the presence of lameUar parhculates on the outer surface, without spherical particulates Other preferred multilayer hlms which could have the mixture of morganic parhculates on one or more outer layers are set forth m copending application U.S.S.N. (42383), to Babrowicz, which is hereby incorporated by reference thereto, in its entirety Although the present invention has been descπbed in connection with the preferred embodiments, it is to be understood that modifications and variations may be utilized without departing from the pπnciples and scope of the invention, as those skiUed in the art wdl readdy understand. Accordmgly, such modifications may be practiced within the scope of the foUowmg claims.

Claims: WHAT IS CLAIMED IS: 1. A film comprising a composition comprising a mixture comprising: (A) inorganic substantially spherical particulates having an average particle size of from about OJ to 30 microns; and (B) inorganic substantially lamellar particulates having an average aspect ratio of from about 5:1 to 40:1, and a major dimension of from about OJ to 15 microns; wherein the substantiaUy spherical particulates and the substantially lamellar particulates are present in an outer film layer and on an outer surface of the film. 2. The film according to claim 1, wherein the substantially lamellar particulates have a hardness of from about 1 to 7, on a Mohs hardness scale. 3. The film according to claim 2 wherein the hardness of the substantially lamellar particulates is from about 1 to 5, on the Mohs hardness scale. 4. The film according to claim 3, wherein the hardness of the substantially lamellar particulates is from about 1 to 3, on the Mohs hardness scale. 5. The film accordmg to claim 1, wherein the composition further comprises a slip enhancer comprising at least one member selected from the group consistmg of fatty acid amide, oxidized polyethylene, fatty acid ester, and fatty acid alcohol. 6. The film accordmg to claim 5, wherem the slip enhancer is present in the outer film layer in an amount of from about 50 to 10,000 parts per million, based on the weight of the outer layer. 7. The film according to claim 5, wherein the slip enhancer comprises at least one member selected from the group consistmg of erucamide, oleamide, stearamide, behenamide, oxidized polyethylene wax, glycerol monostearate, metallic stearate. 8. The him according to claim 5, wherein the composition further comprises a printability enhancer, wherein the printability enhancer comprises a polar polymer. 9. The film according to claim 8, wherein the polar polymer comprises at least one member selected from the group consisting of ethylene/ ester/ maleic anhydride teφolymer, ethylene/ ester/ glycidyl methacrylate terpolymer, and ethylene/ acrylic acid copolymer. 10. The film according to claim 8, wherein the printability enhancer is present in the outer film layer in an amount of from about 1 to 25 percent, based on the weight of the outer film layer. 11. The film according to claim 1, wherein: the substantially spherical particulates are present in the outer layer of the film at a concentration of from about 500-50,000 parts per million, based on the weight of the outer film layer; and the substantially lamellar particulates are present in the outer layer of the film at a concentration of from about 500 to 50,000 parts per million, based on the weight of the outer film layer. 12. The film according to claim 1, wherein: the substantially spherical particulates comprise at least one member selected the group consisting of silica and silicate; and the substantially lamellar particulates comprise silicate. 13. The film according to claim 12, wherein: the substantially spherical particulates comprise at least one member selected the group consisting of natural silica, synthetic silica, and silicate; and the substantially lamellar particulates comprise at least one member selected the group consisting of magnesium silicate and hydrated aluminum silicate. 14. The film according to claim 13, wherein: the substantially spherical particulates comprise at least one member selected the group consisting of diatomaceous earth, fumed synthetic silica, precipitated synthetic silica, gelled synthetic silica, sodium calcium silicate, and sodium calcium aluminum silicate; and the substantially lamellar particulates comprise at least one member selected from the group consisting of talc and kaolin. 15. The film according to claim 1, wherein the film is a multilayer film comprising two outer layers, and wherein the composition is present m at least one of the outer layers. 16. The multilayer film according to claim 15, wherem the multilayer film comprises an O 2 -barrier layer compnsmg at least one member selected from the group consisting of polyvinylidene chloride, ethylene/vinyl alcohol copolymer, polyamide, and polyester. 17. The film accordmg to claim 15, wherem the multilayer film comprises: an outer first layer compnsmg at least one member selected from the group consisting of ethylene/vinyl acetate copolymer, ethylene/alpha-ole n copolymer, and polyamide; an mner second layer, the second layer bemg an 0 2 -barπer layer, the second layer comprismg at least one member selected from the group consisting of polyvinylidene chloride, ethylene/ vmyl alcohol copolymer, polyamide, and polyester; and an outer third layer compnsmg at least one member selected from the group consisting of ethylene/ vmyl acetate copolymer, ethylene/alpha-olefin copolymer, and polyamide. 18. The him accordmg to claim 17, further comprising a fourth layer between the first layer and the second layer, the fourth layer comprising at least one member selected from the group consisting of ethylene/ vmyl acetate copolymer, ethylene/alpha-olefm copolymer, and polyamide. 19. The film according to claim 18, wherem the first layer and the fourth layer each comprise crosslmked polymer, and wherem the second layer and the third layer do not comprise crosslmked polymer. 20. The film accordmg to claim 18, wherem the multilayer film further comprises: a fifth layer, the fifth layer bemg a first tie layer, the fifth layer compnsmg at least one member selected from the group consisting of ethylene/carboxybc acid copolymer, ethylene/ ester copolymer, and anhydride-modified ethylene/alpha-olefm copolymer; and a sixth layer, the sixth layer bemg a second tie layer, the sixth layer comprises at least one member selected from the group consistmg of ethylene/carboxybc acid copolymer, ethylene/ ester copolymer, and anhydride-modified ethylene/alpha-olehn copolymer; and wherem the fifth layer is between the fourth layer and the second layer, the sixth layer is between the second layer and the third layer, and all layers of the mulhlayer film compnse crosslinked polymer. 21. The film accordmg to claim 17, further compnsmg an mner fourth layer, the fourth layer bemg a he layer, the fourth layer compnsmg at least one member selected from the group consisting of ethylene/carboxybc acid copolymer, ethylene/ ester copolymer, and anhydride modihed ethylene/alpha-olefm copolymer. 22. The film accordmg to claim 21, wherem: the fourth layer is between the hrst layer and the second layer; and the film further comprises an mner fifth layer, the fifth layer bemg a second e layer, the fifth layer compnsmg at least one member selected from the group consisting of ethylene/carboxybc acid copolymer, ethylene/ ester copolymer, and anhydride modified ethylene/alpha-olefm copolymer, the fifth layer bemg between the second layer and the third layer. 23. The film according to claim 15, wherein the multilayer him is substantiaUy symmetrical with respect to both layer thickness and layer chemical composihon. 24. The film accordmg to claim 1, wherein the film is has a total free shrmk, at 185°F, of from about 10 to 100 percent 25. The film accordmg to claim 1, wherein the film compπses crosslmked polymer. 26. The film accordmg to claim 1, wherem the film is a monolayer film. 27. The film accordmg to claim 1, wherem the film is biaxially oriented and heat- shrinkable. 28. A film tube compnsmg a film compnsmg a composition compnsmg a mixture comprising- (A) morganic substanhally spherical parhculates havmg an average particle size of from about 0.1 to 30 microns, and (B) inorganic substantially lameUar particulates having an average aspect ratio of from about 5:1 TO 40:1, and a major dimension of from about OJ TO 15 microns; wherein the substantially spherical particulates and the substantially lameUar particulates are present in an outside film layer and on the outside surface of the fibn. 29. The film tube according to claim 28, wherein the tube further comprises an inside surface having dust thereon, and wherein the outside surface of the film is substantiaUy dust- free. 30. The film tube according to claim 29, wherein the dust comprises at least one member selected from the group consisting of aluminum silica, silicon dioxide, sodium calcium alumino silicate, magnesium silicate, and calcium silicate. 31. The film tube according to claim 30, wherein the dust comprises at least one member selected from the group consisting of corn starch, potato starch, talc, and silica. 32. A bag comprising a film comprising a film comprising a composition comprising a mixture comprising: (A) inorganic substantially spherical particulates having an average particle size of from about 0.1 to 30 microns; and (B) inorganic substantially lamellar particulates having an average aspect ratio of from about 5:1 to 40:1, and a major dimension of from about 0J to 15 microns; wherein the substanhally spherical particulates and the substantially lamellar particulates are present in an outside film layer and on the outside surface of the film. 33. A composition comprising: (A) a thermoplastic polymer; (B) inorganic substantially spherical particulates having an average particle size of from about 0.1 to 30 microns; and (C) inorganic substantially lamellar particulates having an average aspect ratio of from about 5:1 to 40:1, and a major dimension of from about 0J to 15 microns. 34. The composition according to claim 33, wherein the polymer comprises ethylene/alpha-olefin copolymer. 35. The composition according to claim 33, wherein: the polymer is present in an amount of from about 70 to 99.9 weight percent, based on the weight of the composition; and the inorganic particulates are present in an amount of from about OJ to 30 weight percent, based on the weight of the composition. 36. The composition according to claim 35, wherein: the polymer is present in an amount of from about 85 to 95 weight percent, based on the weight of the composition; and the inorganic particulates are present in an amount of from about 5 to 15 weight percent, based on the weight of the composition. 37. The composition according to claim 35, wherem: the polymer is present in an amount of from about 95 to 99.9 weight percent, based on the weight of the composition; and the inorganic particulates are present in an amount of from about OJ to 5 weight percent, based on the weight of the composition. 38. The composition according to claim 37, wherein: the polymer is present in an amount of from about 98.5 to 99.5 weight percent, based on the weight of the composition; and the inorganic particulates are present in an amount of from about 0.5 to 1.5 weight percent, based on the weight of the composition.

Inventors: BEKELE SOLOMON, BEKELE, SOLOMON
Applicants: GRACE W R & CO, W.R. GRACE & CO.-CONN.
Application year: 1996
Main classification: C08J5
IPC codes: B32B27, C08J5, C08K3, C08K7, C08L23, C08L101