Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B27/00—Layered products comprising a layer of synthetic resin
  • B32B27/06—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
  • B32B27/08—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
  • C08J5/18—Manufacture of films or sheets
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B27/00—Layered products comprising a layer of synthetic resin
  • B32B27/32—Layered products comprising a layer of synthetic resin comprising polyolefins
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B38/00—Ancillary operations in connection with laminating processes
  • B32B38/0012—Mechanical treatment, e.g. roughening, deforming, stretching
  • B32B2038/0028—Stretching, elongating
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2323/00—Polyalkenes
  • B32B2323/04—Polyethylene
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2439/00—Containers; Receptacles
  • B32B2439/70—Food packaging
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
  • C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
  • C08J2323/04—Homopolymers or copolymers of ethene
  • C08J2323/08—Copolymers of ethene

Definitions

• This invention relates to an improved method for preparing orienting polyolefin films.
• this invention relates to a method for biaxially orienting polyolefin films wherein stretching or orientation conditions are defined to maximize the unrestrained shrink response of the film.
• the invention also relates to a shrink film and to a shrink film made by the novel method wherein in each case the shrink film comprises as the shrink control layer at least one homogeneously branched ethylene interpolymer having a polymer density of less than 0.91 g/cc.
• Hot-blown shrink film is made by a hot-blown simple bubble film process and oriented shrink film is made by elaborate processes known as double bubble, tape bubble, trapped bubble or tenter framing.
• Heat shrink film can be monoaxial or biaxial oriented.
• the shrink packaging method generally involves placing an article(s) into a bag (or sleeve) fabricated from a heat shrink film, then closing or heat sealing the bag, and thereafter exposing the bag to sufficient heat to cause shrinking of the bag and intimate contact between the bag and article.
• the heat can be provided by conventional heat sources, such as heated air, infrared radiation, hot water, combustion flames, or the like.
• Heat shrink wrapping of food articles helps preserve freshness, is attractive, hygienic, and allows closer inspection of the quality of the packaged food.
• Heat shrink wrapping of industrial and retail goods which is alternatively referred to in the art and herein as industrial and retail bundling, preserves product cleanliness and also is a convenient means of bundling and collating for accounting purposes.
• the biaxial heat-shrink response of an oriented polyolefin film is obtained by initially stretching fabricated film to an extent several times its original dimensions in both the machine and transverse directions to orient the film.
• the stretching is usually accomplished while the fabricated film is sufficiently soft or molten, although cold drawn shrink films are also known in the art.
• the stretch orientation is frozen or set in by quick quenching of the film.
• Subsequent application of heat will then cause the oriented film to relax and, depending on the actual shrink temperature, the oriented film can return essentially back to its original unstretched dimensions, i.e., to shrink relative to its stretched dimension.
• Golike in US Patent 4,597,920.
• Golike teaches orientation should be carried out at temperatures between the lower and higher melting points of a copolymer of ethylene with at least one Cs-Ci8 ⁇ -olefin.
• Golike specifically teaches that the temperature differential is at least 10°C, however, Golike also specifically discloses that the full range of the temperature differential may not be practical because, depending on the particular equipment and technique used, tearing of the polymer film may occur at the lower end of the range.
• Golike teaches the structural integrity of the polymer film begins to suffer during stretching (and ultimately fails at higher temperatures) because the polymer film then is in a soft, molten condition. See, US Patent 4,597,920, Col. 4, lines 52-68 bridging to Col. 5., lines 1-6.
• the orientation temperature range defined by Golike (which is based on higher and lower peak melting points) generally applies to polymer blends and heterogeneously branched ethylene/ ⁇ -olefin interpolymers, i.e. compositions having two or more DSC melting points, and does not apply at all to homogeneously branched ethylene/ ⁇ -olefin interpolymers which have only a single DSC melting point.
• Golike also indicates that a person of ordinary skill can determine the tear temperature of a particular polymer and discloses that for heterogeneously branched interpolymers having a density of about 0.920 g/cc, the tear temperature occurs at a temperature above the lower peak melting point. See, US Patent 4,597,920, Col. 7, Example 4. However, Golike does not teach or suggest how a person of ordinary skill in the art of shrink film can optimize the orientation process as to stretching temperature at a given stretching rate and ratio to maximize the shrink response.
• Hideo et al. in EP 0359907 A2 teach the film surface temperature at the starting point of stretching should be within the range of from 20°C to about 30°C below the melting temperature of the polymer as determined in regards to the main DSC endothermic peak. While such teaching is considered applicable to homogeneously branched ethylene/ ⁇ -olefin interpolymers having a single DSC melting peak, the prescribed range is fairly general and broad. Moreover, Hideo et al. do not provide any specific teaching as to the optimum orientation temperature for a particular interpolymer respecting heat shrink response, nor any other desired film property.
• homogeneously branched substantially linear ethylene/ ⁇ -olefin interpolymers had densities that varied from about 0.896 to about 0.906 g/cc, all of the interpolymers (including the heterogeneously branched linear ethylene/ ⁇ -olefin interpolymer, AttaneTM 4203, supplied by The Dow Chemical Company, which had a density of 0.905 g/cc) were oriented at essentially the same orientation temperatures.
• orientation information regarding homogeneously branched ethylene polymers yet do not specify orientation conditions relative to respective lowest stretch temperatures include EP 0 600425A1 to Babrowicz et al. and EP 0 587502 A2 to Babrowicz et al.
• homogeneously branched ethylene interDolymers offer a variety of other useful property advantages, at equiva ent densities above about 0.907 g/cc
• the shrink response of multilayer film structures which contain a homogeneously branched ethylene interpolymer as the shrink control layer is generally viewed as essentially equivalent to multilayer film structures which contain a heterogeneously branched interpolymer as the shrink control layer. See FIG. 3. It is an object of the present invention to provide a method for defining the optimum stretching or orientation temperature to maximize the unrestrained (free) shrink response of polyolefins n general.
• a method of making a heat shrinkable polyolefin film comprising the steps of a. fabricating a polyolefin film structure in substantially unoriented form, and b. stretching the polyolefin film at a selected stretching rate, stretch ratio and stretching temperature, wherein the selected stretching temperature is no more than or equal to 5 C C above the lowest stretch temperature for the polyolefin film structure and for the selected stretching rate and stretching ratio and wherein the polyolefin film structure comprises at least one ethylene polymer having a polymer density less than 0.915 g/cc.
• Another aspect of the present invention is a heat shrinkable film structure which comprises, as the shrink control layer, at least one homogeneously branched ethylene interpolymer having a polymer density of less than 0.91 g/cc, wherein the film structure is characterized as having a shrink response at least 10 percent greater than the shrink response of a second film structure which comprises a heterogeneously branched ethylene interpolymer as the shrink control layer and wherein the film structure and the second film structure are fabricated and stretched under essentially the same conditions and the homogeneously branched and heterogeneously branched interpolymers have essentially the same polymer density and I 2 melt index.
• Still another aspect of the present invention is a heat shrink polyolefin film structure prepared by a method which comprises the steps of
• FIG. 1 is a first heat DSC curve illustrating the residual crystallinity portion of a heterogeneously branched polymer remaining at 100°C which is a temperature below the various melting peaks of the polymer illustrated.
• FIG. 2 is a x/y plot illustrating the shrink response of heterogeneously branched ethylene polymers and homogeneously branched ethylene polymer as a function of polymer density.
• the data used to generate the plot are reported in Table 2 hereinbelow.
• the heterogeneously branched ethylene polymer samples range in polymer densities from about 0.907 to about 0.932 g/cc while the homogeneously branched ethylene polymer samples range from about 0.91 to about 0.918 g/cc.
• FIG. 3 is another x/y plot illustrating the shrink response of heterogeneously branched ethylene polymers and homogeneously branched ethylene polymer as a function of polymer density.
• the data used to generate this plot are reported in Table 2 hereinbelow.
• the heterogeneously branched ethylene polymer samples range in polymer densities from about 0.907 to about 0.932 g/cc while the homogeneously branched ethylene polymer samples range from about 0.887 to about 0.918 g/cc.
• the double bubble and trapped bubble biaxial orientation methods can be simulated on a laboratory scale using a T. M. Long stretcher which is analogous to a tenter frame device.
• This device can orient polyolefin films in both the monoaxial and biaxial mode at stretching ratios up to at least 5:1.
• the device uses films having an original dimension of 2 inches x 2 inches.
• Biaxial stretching is usually performed by stretching in the machine direction and transverse direction of the film simultaneously, although the device can be operated to stretch sequentially.
• the residual crystallinity of polyolefin interpolymers measured using a DSC partial area method can be used to characterize the nature of polyolefin film at the stretch temperature.
• a stretching temperature 5°C above, preferably 3°C above, more preferably 2.5°C above the lowest stretch temperature is considered herein to be the optimum or near-optimum stretching or orientation temperature for the particular film.
• Stretching temperatures higher than 5°C above the lowest stretch temperature are not considered part of the present invention because such invariably yield lower shrink responses for a particular stretching rate, stretching ratio and shrink temperature. Stretching temperatures less than 2.5°C above the lowest stretch temperature are not preferred because they tend to yield inconsistent results, although such inconsistencies tend to depend on specific equipment and temperature control capabilities.
• heterogeneously branched ethylene interpolymers possess higher residual crystallinities at their respective optimum orientation temperature relative to homogeneously branched ethylene interpolymers.
• Heterogeneously branched interpolymers having a density in the range of from 0.90 to 0.93 g/cc have residual crystallinities at respective optimum orientation temperatures of from 20 to 24 percent, while homogeneously branched ethylene interpolymers having a density in the range of from 0.895 to 0.91 g/cc have residual crystallinities at their respective optimum orientation temperatures of from 14 to 17 percent.
• Stretched and oriented are used in the art and herein interchangeably, although orientation is actually the consequence of a film being stretched by, for example, internal air pressure pushing on the tube or by a tenter frame pulling on the edges of the film.
• low stretch temperature means the temperature below which the film either tears and/or stretches unevenly for a given stretching rate and stretching (draw) ratio during the stretching operation or step of an orientation technique.
• the lowest stretch temperature is below the melting point of the film, it is a temperature at or below which the film can not be stretched uniformly (i.e., without the occurrence of banding or thick and thin spots), and it is a temperature at or below which the film tears for a particular stretching rate and stretch ratio.
• the objective is to operate as close to the lowest stretch temperature as their equipment and capabilities will allow whether or not the significant stretching or orientation is accomplished in a single step or by a combination of sequential steps.
• optimum or near-optimum stretching temperature for maximized shrink response at a given shrink temperature will interrelate with stretching rate and ratio. That is, while a particular stretching temperature will be optimum or near-optimum at one combination of stretching rate and ratio, the same stretching temperature will not be optimum or near-optimum at a different combination of stretching rate and ratio.
• the shrink temperature should match or exceed the stretching temperature. That is, reduced shrink temperatures do not allow full relaxation or shrinkage of the film However, excessive shrink temperatures can diminish film integrity. Practitioners will further appreciate that for a given combination of stretching temperature, stretching rate and stretching ratio, increases in the shrink temperature to the point of film integrity failure will yield higher shrink response performance and higher levels of shrink tension. Stretching temperatures in the range of from 50 to about
• 120°C especially from 55 to 110°C, more especially from 60 to 95 C C, and most especially from 65 to 90°C are suitable in the present invention.
• Shrink temperatures in the range of from 70 to 140 C C, especially from 80 to 125°C, and more especially from 85 to 100 C C are suitable in the present invention.
• residual crystallinity is used herein to refer the crystallinity of a polymer film at a particular stretching temperature. Residual crystallinity is determined using a Perkm-Elmer DSC 7 set for a first heat at 10°C/m ⁇ n. of a water-quenched, compression molded film sample of the polymer. The residual crystallinity for an interpolymer at a particular temperature is determined by measuring heat of fusion between that temperature and the temperature of complete melting using a partial area technique and by dividing the heat of fusion by 292 Joules/gram. The heat of fusion is determined by computer integration of the partial area using Perkin-Elmer PC Series Software
• shrink control layer is used herein to refer to the film layer that provides or controls the shrink response Such a layer is inherent to all heat shrink films. In a monolayer heat shrink film, the shrink control layer will be the film itself. In a multilayer heat shrink film, the shrink control layer is typically the core or an inside film layer and is typically the thickest film layer. See, for example, WO 95/08441.
• substantially unoriented form is used herein in reference the fact that some amount of orientation is usually imparted to a film during ordinary fabrication. As such, it is meant that the fabrication step, in itself, is not used to impart the degree of orientation required for the desired or required shrink response.
• the present invention is thought to be generally applicable to operations where the fabrication and orientation steps are separable and occur simultaneously. However, the present invention is preferably directed to an additional and separate orientation step which is required beyond the making of tube, sock, web or layflat sheet whether or not such is soft, molten, or irradiated before substantial orientation is imparted.
• homogeneous ethylene interpolymer "homogeneously branched ethylene interpolymer” and “narrow short chain distribution” are used in the conventional sense in reference to an ethylene interpolymer in which the comonomer is randomly distributed within a given polymer molecule and wherein substantially all of the polymer molecules have the same ethylene to comonomer molar ratio.
• the terms refer to an ethylene interpolymer that is characterized by a relatively high short chain branching distribution index (SCBDI) or composition distribution branching index (CDBI) .
• SCBDI short chain branching distribution index
• CDBI composition distribution branching index
• the interpolymer has a SCBDI greater than or equal to 50 percent, preferably greater than or equal to 70 percent, more preferably greater than or equal to 90 percent and essentially lack a measurable high density (crystalline) polymer fraction.
• SCBDI or CDBI is defined as the weight percent of the polymer molecules having a comonomer content within 50 percent of the median total molar comonomer content and represents a comparison of the monomer distribution in the interpolymer to the monomer distribution expected for a Bernoullian distribution.
• the SCBDI of an interpolymer can be readily calculated from data obtained from techniques known in the art, such as, for example, temperature rising elution fractionation (abbreviated herein as "TREF") as described, for example, by Wild et al., Journal of Polymer Science, Poly. Phys. Ed., Vol. 20, p. 441 (1982), or in US Patent 4,798,081, or by L. D. Cady, "The Role of Comonomer Type and Distribution in LLDPE Product Performance, " SPE Regional Technical Conference, Quaker Square Hilton, Akron, Ohio, October 1-2, pp. 107-119 (1985).
• the preferred TREF technique does not include purge quantities in SCBDI calculations. More preferably, the monomer distribution of the interpolymer and SCBDI are
• heterogeneous, “ “heterogeneously branched” and “broad short chain distribution” are used herein in the conventional sense in reference to a linear ethylene interpolymer having a comparatively low short chain branching distribution index. That is, the interpolymer has a relatively broad short chain branching distribution.
• Heterogeneously branched linear ethylene interpolymers have a SCBDI less than 50 percent and more typically less than 30 percent.
• homogeneously branched linear ethylene interpolymer means that the interpolymer has a homogeneous (or narrow) short branching distribution but does not have long chain branching. That is, the ethylene interpolymer has an absence of long chain branching and a linear polymer backbone in the conventional sense of the term "linear.”
• Such interpolymers can be made using polymerization processes (e.g., as described by Elston in USP 3,645,992) which provide uniform (narrow) short branching distribution (i.e., homogeneously branched) . In his polymerization process, Elston uses soluble vanadium catalyst systems to make such polymers, however others such as Mitsui
• homogeneously branched linear ethylene interpolymer does not refer to high pressure branched polyethylene which is known to those skilled in the art to have numerous long chain branches.
• the homogeneously branched linear ethylene interpolymer is an ethylene/ ⁇ -olefin interpolymer, wherein the ⁇ —olefin is at least one C3-C20 ⁇ -olefin (e.g., 1-propylene, 1-butene, 1-pentene, 4-methyl-l-pentene, 1-hexene, 1-octene and the like) , preferably wherein at least one of the ⁇ -olefins is 1-octene.
• the ⁇ —olefin is at least one C3-C20 ⁇ -olefin (e.g., 1-propylene, 1-butene, 1-pentene, 4-methyl-l-pentene, 1-hexene, 1-octene and the like) , preferably wherein at least one of the ⁇ -olefins is 1-octene.
• the ethylene/ ⁇ -olefin interpolymer is a copolymer of ethylene and a C3-C20 ct- olefin, especially an ethylene/C 4 -C6 ⁇ -olefin copolymer.
• ethylene/ ⁇ -olefin interpolymers are sold by Mitsui Chemical under the designation "TAFMER” and by Exxon Chemical under the designation "EXACT”.
• VLDPE and LLDPE are well known among practitioners of the linear polyethylene art . They are prepared using conventional Ziegler-Natta solution, slurry or gas phase polymerization processes and coordination metal catalysts as described, for example, by Anderson et al. in U.S. Pat. No. 4,076,698. These conventional Ziegler-type linear polyethylenes are not homogeneously branched, do not have any long-chain branching and have a linear polymer backbone m the conventional sense of the term "linear.” Also, these polymers do not show any substantial amorphism at lower densities since they inherently posses a substantial high density (crystalline) polymer fraction.
• ultra low density polyethylene ULDPE
• very low density polyethylene VLDPE
• LVLDPE linear very low density polyethylene
• ULDPE ultra low density polyethylene
• VLDPE very low density polyethylene
• LVLDPE linear very low density polyethylene
• LLDPE linear low density polyethylene
• ATTANETM ULDPE polymers supplied by the Dow Chemical Company and FLEXOMERTM VLDPE polymers supplied by Union Carbide Corporation.
• the novel method of the present invention is useful for preparing shrink film structures comprised of heterogeneously branched ethylene polymers, and homogeneously branched ethylene polymers and these polymers are also suitable for claimed shrink film prepared by the novel method, not all of the above polymers are suitable for use in the novel film of the present invention That is, while the method and the shrink film by the method are generally applicable to all of the above ethylene polymers, only homogeneously branched substantially linear ethylene polymers and homogeneously branched linear ethylene polymers are suitable for all aspects of the present invention including the novel film.
• substantially linear ethylene/ ⁇ -olefin interpolymer is used herein to refer to homogeneously branched ethylene/ ⁇ -olefin interpolymers that contain long chain branches as well as short chain branches attributable to homogeneous comonomer incorporation.
• the long chain branches are of the same structure as the backbone of the polymer and are longer than the short chain branches.
• the polymer backbone of substantially linear ⁇ -olefin polymers is substituted with an average of 0.01 to 3 long chain branch/1000 carbons.
• Preferred substantially linear polymers for use in the invention are substituted with from 0.01 long chain branch/1000 carbons to 1 long chain branch/1000 carbons, and more preferably from 0.05 long chain branch/1000 carbons to 1 long chain branches/1000 carbons.
• Long chain branching is defined herein as a chain length of at least 6 carbons, above which the length cannot be distinguished using ⁇ C nuclear magnetic resonance spectroscopy.
• the long chain branch can be as long as about the same length as the length of the polymer backbone to which it is attached. Long chain branches are obviously of greater length than of short chain branches resulting from comonomer incorporation.
• deGroot and Chum found that the presence of octene does not change the hydrodynamic volume of the polyethylene samples in solution and, as such, one can account for the molecular weight increase attributable to octene short chain branches by knowing the mole percent octene in the sample. By deconvoluting the contribution to molecular weight increase attributable to 1-octene short chain branches, deGroot and Chum showed that GPC-DV may be used to quantify the level of long chain branches in substantially linear ethylene/octene copolymers.
• substantially linear ethylene/ ⁇ -olefin interpolymers used in the present invention are a unique class of compounds that are further defined in US Patent 5,272,236, serial number 07/776,130 filed October 15, 1991 and in US patent 5,278,272, serial number 07/939,281 filed September 2, 1992.
• Substantially linear ethylene/ ⁇ -olefin interpolymers differ significantly from the class of polymers conventionally known as homogeneously branched linear ethylene/ ⁇ -olefin interpolymers described, for example, by Elston in US Patent 3,645,992, in that substantially linear ethylene interpolymers do not have a linear polymer backbone in the conventional sense of the term "linear.”
• Substantially linear ethylene/ ⁇ -olefin interpolymers also differ significantly from the class of polymers known conventionally as heterogeneously branched traditional Ziegler polymerized linear ethylene interpolymers (for example, ultra low density polyethylene, linear low density polyethylene or high density polyethylene made, for example, using the technique disclosed by Anderson et al.
• substantially linear ethylene interpolymers are homogeneously branched interpolymers.
• Substantially linear ethylene/ ⁇ -olefin interpolymers also differ significantly from the class known as free-radical initiated highly branched high pressure low density ethylene homopolymer and ethylene interpolymers such as, for example, ethylene-acrylic acid (EAA) copolymers and ethylene-vinyl acetate (EVA) copolymers, in that substantially linear ethylene interpolymers do not have equivalent degrees of long chain branching and are made using single site catalyst systems rather than free-radical peroxide catalysts systems.
• EAA ethylene-acrylic acid
• EVA ethylene-vinyl acetate
• Single site polymerization catalyst for example, the monocyclo-pentadienyl transition metal olefin polymerization catalysts described by Canich in US Patent 5,026,798 or by Canich in US Patent
• the substantially linear ethylene interpolymers are preferably made by using suitable constrained geometry catalysts, especially constrained geometry catalysts as disclosed in US Application Serial Nos.: 545,403, filed July 3, 1990; 758,654, filed September 12, 1991; 758,660, filed September 12, 1991; and 720,041, filed June 24, 1991.
• Suitable cocatalysts for use herein include but are not limited to, for example, polymeric or oligomeric aluminoxanes, especially methyl aluminoxane or modified methyl aluminoxane (made, for example, as described in US Patent 5,041,584, US Patent 4,544,762, US Patent 5,015,749, and/or US Patent 5,041,585) as well as inert, compatible, non-coordinating, ion forming compounds.
• Preferred cocatalysts are inert, non-coordinating, boron compounds.
• the polymerization conditions for manufacturing the substantially linear ethylene interpolymers used in the present invention are preferably those useful in the continuous solution polymerization process, although the application of the present invention is not limited thereto. Continuous slurry and gas phase polymerization processes can also be used, provided the proper catalysts and polymerization conditions are employed.
• the single site and constrained geometry catalysts mentioned earlier can be used, but for substantially linear ethylene polymers the polymerization process should be operated such that the substantially linear ethylene interpolymers are formed. That is, not all polymerization conditions inherently make the substantially linear ethylene polymers, even when the same catalysts are used.
• a continuous process is used, as opposed to a batch process.
• a gas extrusion rheology such that the critical shear rate at onset of surface melt fracture for the substantially linear ethylene interpolymer is at least 50 percent greater than the critical shear rate at the onset of surface melt fracture for a linear ethylene interpolymer, wherein the substantially linear ethylene interpolymer and the linear ethylene interpolymer comprise the same comonomer or comonomers, the linear ethylene interpolymer has an I2 M w /M n and density within ten percent of the substantially linear ethylene interpolymer and wherein the respective critical shear rates of the substantially linear ethylene interpolymer and the linear ethylene interpolymer are measured at the same melt temperature using a gas extrusion rheometer, and
• the substantially linear ethylene interpolymers used in this invention are homogeneously branched interpolymers and essentially lack a measurable "high density" fraction as measured by the TREF technique (i.e., have a narrow short chain distribution and a high SCBD index) .
• the substantially linear ethylene interpolymer generally do not contain a polymer fraction with a degree of branching less than or equal to 2 methyls/1000 carbons.
• the "high density polymer fraction" can also be described as a polymer fraction with a degree of branching less than 2 methyls/1000 carbons.
• the substantially linear ethylene interpolymers for use in the novel method and the film made from the novel method of the present invention are interpolymers of ethylene with at least one C3-C20 ⁇ olefin and/or C4-C]_g diolefm. Copolymers of ethylene and an ⁇ -olefin of C3-C20 carbon atoms are especially preferred.
• interpolymer is used herein to indicate a copolymer, or a terpolymer, or the like, where, at least one other comonomer is polymerized with ethylene to make the interpolymer.
• Suitable unsaturated comonomers useful for polymerizing with ethylene include, for example, ethylenically unsaturated monomers, conjugated or non-conjugated dienes, polyenes, etc.
• comonomers include C3-C20 ⁇ -olefins as propylene, isobutylene, 1-butene,
• 1-hexene 4-methyl-l-pentene, 1-heptene, 1-octene, 1-nonene, 1-decene, and the like.
• Preferred comonomers include propylene, 1-butene, 1- hexene, 4-methyl-l-pentene and 1-octene, and 1-octene is especially preferred.
• Suitable comonomers include styrene, halo- or alkyl- substituted styrenes, tetrafluoroethylene, vmylbenzocyclobutane, 1,4- hexadiene, 1, 7-octad ⁇ ene, and cycloalkenes, e.g., cyclopentene, cyclohexene and cyclooctene.
• Determination of the critical shear rate and critical shear stress in regards to melt fracture as well as other rheology properties such as "rheological processing index" (PI) is performed using a gas extrusion rheometer (GER) .
• GER gas extrusion rheometer
• the PI is the apparent viscosity (in kpoise) of a material measured by GER at an apparent shear stress of about 2.15 x 10° dyne/cm 2 .
• the substantially linear ethylene polymer for use in the invention are ethylene interpolymers having a PI in the range of 0.01 kpoise to 50 kpoise, preferably 15 kpoise or less.
• the substantially linear ethylene polymers used herein have a PI less than or equal to 70 percent of the PI of a linear ethylene interpolymer (either a conventional Ziegler polymerized interpolymer or a linear homogeneously branched interpolymer as described by Elston in US Patent 3,645,992) having an I2, M w /M n and density, each within ten percent of the substantially linear ethylene interpolymer.
• a linear ethylene interpolymer either a conventional Ziegler polymerized interpolymer or a linear homogeneously branched interpolymer as described by Elston in US Patent 3,645,992
• I2 I2
• M w /M n linear homogeneously branched interpolymer
• the critical shear rate at the onset of surface melt fracture for the substantially linear ethylene interpolymers is at least 50 percent greater than the critical shear rate at the onset of surface melt fracture of a linear ethylene interpolymer having essentially the same I2 and M w /M n .
• Gross melt fracture occurs at unsteady extrusion flow conditions and ranges m detail from regular (alternating rough and smooth, helical, etc.) to random distortions. For commercial acceptability and maximum abuse properties of films, coatings and profiles, surface defects should be minimal, f not absent.
• the critical shear stress at the onset of gross melt fracture for the substantially linear ethylene interpolymers used in the invention that is those having a density less than 0.91 g/cc, is greater than 4 x 10 ⁇ dynes/cm ⁇ .
• the critical shear rate at the onset of surface melt fracture (OSMF) and the onset of gross melt fracture (OGMF) will be used herein based on the changes of surface roughness and configurations of the extrudates extruded by a GER.
• the substantially linear ethylene interpolymer will be characterized by its critical shear rate, rather than its critical shear stress.
• Substantially linear ethylene/ ⁇ -olefin interpolymers like other homogeneously branched ethylene/ ⁇ -olefin interpolymers that consist of a single polymer component material, are characterized by a single DSC melting peak.
• the single melting peak is determined using a differential scanning calorimeter standardized with indium and deionized water. The method involves about 5-7 mg sample sizes, a "first heat" to about 180°C which is held for about 4 minutes, a cool down at about 10°/min.
• the single melting peak may show, depending on equipment sensitivity, a "shoulder” or a "hump” on the low melting side that constitutes less than 12 percent, typically, less than 9 percent, and more typically less than 6 percent of the total heat of fusion of the polymer.
• Such an artifact is observable for other homogeneously branched polymers such as ExactTM resins and is discerned on the basis of the slope of the single melting peak varying monotonically through the melting region of the artifact.
• Such an artifact occurs within 34°C, typically within 27°C, and more typically within 20°C of the melting point of the single melting peak.
• the heat of fusion attributable to an artifact can be separately determined by specific integration of its associated area under the heat flow vs. temperature curve.
• the molecular weight determination is deduced by using narrow molecular weight distribution polystyrene standards (from Polymer Laboratories) in conjunction with their elution volumes.
• the equivalent polyethylene molecular weights are determined by using appropriate Mark- Houwink coefficients for polyethylene and polystyrene (as described by
• Weight average molecular weight, M w , and number average molecular weight, M n is calculated in the usual manner according to the following formula:
• the M w /M n is preferably less than 3, more preferably less than 2.5, and especially from 1.5 to about 2.5 and most especially from 1.8 to 2.3.
• substantially linear ethylene interpolymers are known to have excellent processability, despite having a relatively narrow molecular weight distribution.
• the melt flow ratio (Il ⁇ /l2) of substantially linear ethylene interpolymers can be varied essentially independently of the molecular weight distribution, M w /M n .
• the preferred ethylene ⁇ -olefin interpolymer for use in the present invention is a substantially linear ethylene interpolymer.
• Homogeneously branched substantially linear ethylene interpolymers are available from The Dow Chemical Company as AffinityTM polyolefin plastomers, and as Engage TM polyolefin elastomers.
• Homogeneously branched substantially linear ethylene polymers can be prepared by the continuous solution, slurry, or gas phase polymerization of ethylene and one or more optional ⁇ -olefin comonomers in the presence of a constrained geometry catalyst, such as is disclosed in European Patent Application 416,815-A.
• the density of the polyolefin polymer (as measured in accordance w th ASTM D-792) for use in the presently claimed method is generally greater than 0.85 g/cc, especially from 0.86 g/cc to 0.93 g/cc, more preferably, from about 0.88 g/cc to 0.92 g/cc and most preferably, from 0.88 to 0.91.
• the preferred polymer density of the polyolefin polymer is less than 0.915 g/cc.
• the density of the homogeneously branched ethylene polymer for use in all aspects of the present invention is less than 0.91 g/cc, generally in the range of 0.85 to 0.91 g/cc, preferably less than 0.907 g/cc, more preferably less than or equal to 0.905 g/cc, most preferably less than or equal to 0.902 g/cc, and especially in the range of 0.880 to 0.90 g/cc.
• the molecular weight of polyolefin polymers is conveniently indicated using a melt index measurement according to ASTM D-1238, Condition 190°C/2.16 kg (formerly known as "Condition E” and also known as I2) • Melt index is inversely proportional to the molecular weight of the polymer. Thus, the higher the molecular weight, the lower the melt index, although the relationship is not linear.
• the melt index for the polyolefin polymers useful herein is generally from 0.01 g/10 mm. to 20 g/10 min., preferably from 0.01 g/10 mm. to 10 g/10 min., and especially from 0.1 g/10 min. to 2 g/10 mm.
• melt index determinations with higher weights, such as, for common example, ASTM D-1238, Condition 190°C/10 kg (formerly known as "Condition N” and also known as I]_n) .
• the ratio of a higher weight melt index determination to a lower weight determination is known as a melt flow ratio, and for measured Iio and the I2 melt index values the melt flow ratio is conveniently designated as I ⁇ o l2-
• the melt flow ratio indicates the degree of long chain branching, i.e., the higher the I10/I2 melt flow ratio, the more long chain branching in the polymer.
• the I10/I2 ratio of the substantially linear ethylene polymers is preferably at least 7, and especially at least 9.
• antioxidants e.g., hindered phenolics
• phosphites e.g., Irgafos® 168
• cling additives e.g., PIB
• PEPQTM a trademark of Sandoz Chemical, the primary ingredient of which is believed to be a biphenylphosphonite
• pigments, colorants, fillers, and the like can also be included in the polyolefin polymers, to the extent that they do not interfere with the method and the enhanced shrink response discovered by Applicants.
• the fabricated film may also contain additives to enhance its antiblocking and coefficient of friction characteristics including, but not limited to, untreated and treated silicon dioxide, talc, calcium carbonate, and clay, as well as primary and secondary fatty acid amides, silicone coatings, etc.
• additives to enhance the film's anti-fogging characteristics may also be added, as described, for example, in US Patent 4,486,552 (Niemann) .
• Film structures of the present invention can be made using conventional simple bubble or cast extrusion techniques, however, preferred film structures are prepared using more elaborate techniques such as "tenter framing" or the "double bubble, " "tape bubble” or “trapped bubble” process.
• the double bubble technique is described by Pahkle in US Patent 3,456,044.
• the presently claimed method for preparing shrink film structures and the novel film structures of the present invention are more fully described in the following examples, but are not limited to the examples shown.
• the homogeneously branched substantially linear ethylene polymers used in the following examples were prepared according to procedures and techniques described in the Examples of U.S. Patent 5,272,236 and 5,278,272.
• the homogeneously branched linear ethylene interpolymer used in the following Examples was made by the Exxon Chemical Company.
• Example 1 utilized a substantially linear ethylene/1-octene copolymer having a density of 0.90 g/cc, a melt index (I 2 ) of 0.8 g/10 minutes, a molecular weight distribution (Mw/Mn) of 2.2, and a melt flow ratio (I ⁇ n/12) of 8.5.
• Example 2 utilized the polymer of Example 1 which had been irradiated at 5.0 Mrad.
• Comparative Run 3 utilized a heterogeneously branched ULDPE ethylene/1-octene copolymer having a density of 0.905 g/cc, a melt index (I2) of 0.8, a molecular weight distribution (M w /M n ) of 3.5 and a melt flow ratio (I10/I2) of 8 - Comparative Run 4 utilized the polymer of Comparative Run 3 which had been irradiated at 5.0 Mrad. Irradiation was performed on pellets of the respective interpolymers by exposure to electron beam radiation at E Beam Services, Inc. (Canterbury, NJ) .
• the DSC melting point for the non-irradiated interpolymers was determined, all four samples were prepared into sheeting (18.5 ⁇ 1.5 mil thick) (0.47 mm ⁇ 0.04 mm) and subsequently biaxially stretched using a T.M. Long laboratory stretching frame.
• the stretching temperature utilized was a temperature below the DSC melting point of the copolymer but 5°C above the temperature at which tearing of the sheet occurs during stretching.
• These stretched sheets were tested for unrestrained (free) shrink at 95°C in accordance with procedures in ASTM D-2732 by cutting four inch by four inch (10.2 cm x 10.2 cm) samples from each of the stretched sheets and carefully placing them flat into the bottom of silicone-coated metal pans.
• the metal pans had sides 1 inch (2.5 cm) high and were well-coated with 200 centipoise silicone oil.
• the pans containing the film samples were then placed into a forced-air convection oven at 95°C for ten minutes. After ten minutes, the pans were removed from the oven and allowed to cool to an ambient temperature. After cooling, the film samples were removed and the dimensions in both the machine and transverse directions were measured. The Vicat softening point was measured in accordance with ASTM D1525. Table 1 summarizes the shrink response data as well as provides the stretch ratio information for each sample:
• the data in Table 1 show that the sheets fabricated from the homogeneously branched substantially linear ethylene interpolymer exhibited superior shrink response performance (at least 14 percent greater) over comparable sheets fabricated from the conventional heterogeneously branched linear ethylene interpolymer.
• the superior shrink response is exhibited even when the amount of biaxial stretching is significantly lower for the Inventive Examples relative to the comparative examples (i.e., 3 x 3 versus x 4) .
• the Inventive Examples even show superior free shrink performance regardless of whether the comparative examples were irradiated or nonirradiated prior to orientation (stretching) .
• the stretching temperature for the homogeneously branched substantially linear ethylene interpolymer was 7°C below its single DSC melting point.
• the stretching temperature for the heterogeneously branched linear ethylene interpolymer was 25°C below its highest DSC melting peak, 21°C below its intermediate melting peak and 2°C above its lowest melting peak.
• the stretching temperature for the homogeneously branched substantially linear ethylene polymer is considered the optimum or near-optimum stretching temperature for the polymer and for the particular stretch ratio and stretching rate. That is, the shrink response is the maximum obtainable for the sample at a 95°C shrink temperature wherein a higher stretching temperature would yield a reduced shrink response.
• LLCPEs heterogeneously branched linear low density polyethylenes
• DOWLEX heterogeneously branched ultra or very low density polyethylenes
• ULDPEs or VLDPEs ultra or very low density polyethylenes
• FLEXOMER homogeneously branched substantially linear ethylene interpolymers supplied by The Dow Chemical Company under the trademarks "AFFINITY” and “ENGAGE;” homogeneously branched linear ethylene interpolymers supplied by Exxon Chemical
• the stretching temperature was raised for subsequent sample sheets of the same polymer sample in 3°C intervals until or such that a corresponding sample sheet could be consistently and uniformly oriented at a stretching ratio of 4.5 x 4.5 and a stretching rate 5 inches/second (12.7 cm/second) .
• the first interval of a higher temperature where the polymer sample could be consistently and uniformly oriented was taken as the optimum stretching temperature for the particular polymer sample, stretch ratio and stretching rate and, as such, provides the highest residual crystallinity that the particular polymer sample sheet could be oriented.
• TafmerTM A4090 could not be uniformly stretched apparently due its relatively high melt index.
• the hot-water shrinkage at 90°C for the biaxially oriented sheets are also shown in Table 2.
• Shrinkage values were obtained by measuring the unrestrained shrink in a water bath kept at 90°C. The samples were cut into 12 cm x 1.27 cm pieces. The samples were marked 10 cm. from one end for identification. Each sample was completely immersed in the water bath for five seconds and then removed. Film shrinkage was obtained from the calculation using ASTM method D 2732-83. The average of four samples was calculated and the data are also reported in Table 2. Since the samples were equi-biaxially oriented (i.e., 4.5 x 4.5), the shrinkage in the machine and transverse directions were equivalent as expected. Also, the shrink response at 90 ° C for the various heterogeneously branched and homogeneously branched ethylene interpolymers as a function of polymer density are shown in FIG. 2 and FIG. 3.
• the orientation (stretching) temperatures shown in Table 2 represent the low end of the orientation window for each sample.
• the high end of an orientation window is usually ust below the higher melting peak of the polymer.
• heterogeneously branched ethylene interpolymers have a much broader orientation window than homogeneously branched ethylene interpolymers (i.e., Affinity, Engage and Exact resins) .
• the homogeneously branched AffinityTM polymer sample has a single DSC melting point and, as such, Golike' s teachings are not specifically applicable to such polymers.
• the homogeneously branched AffinityTM polymer sample can also be oriented for a maximized shrink response at a stretching temperature below its respective lower melting peak.
• Table 2 indicates heterogeneously branched LLDPE and ULDPE polymers having a density in the range from 0.907 g/cc to 0.937 g/cc can be oriented at a maximum residual crystallinity of from 20 weight percent to 24 weight percent and that the maximum residual crystallinity for optimum or near-optimum orientation of these polymers is predominately influenced by polymer crystallinity or crystalline polymer fractions.
• Table 2 also indicates homogeneously branched ethylene interpolymers in the density range from 0.899 g/cc to 0.918 g/cc can be oriented at a maximum residual crystallinity of from 14 weight percent to 17 weight percent.
• FIG. 2 indicates that at polymer densities greater than 0.91 g/cc, heterogeneously branched polymers show a higher shrink response than homogeneously branched polymers at an equivalent density
• FIG. 3 indicates that at densities less than 0.91 g/cc for interpolymers stretched in accordance with the present invention, homogeneously branched ethylene polymers show greater than or equal to 10 percent greater, especially 15 percent greater, more especially 20 percent greater and most especially 25 percent greater shrink response than heterogeneously branched ethylene polymers having equivalent densities in that range and fabricated (including orientation) at essentially the same conditions.
• interpolymer densities are less than 0.907 g/cc, more especially equal to or less than 0.905 g/cc, more especially less than or equal to 0.902 g/cc and most especially equal to or less than 0.90 g/cc.
• the shrink response of the homogeneously branched ethylene polymers as shown in FIG. 3 is especially surprising since reasonable extrapolation of the data shown in FIG. 2 as well as the data disclosed in WO Publication 95/08441 suggest the shrink response of homogeneously branched ethylene polymers are expected to be inferior to or, at best, essentially equivalent to heterogeneously branched ethylene polymers at densities less than 0.91 g/cc.

Landscapes

• Chemical & Material Sciences (AREA)
• Engineering & Computer Science (AREA)
• Manufacturing & Machinery (AREA)
• Medicinal Chemistry (AREA)
• Health & Medical Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Materials Engineering (AREA)
• Polymers & Plastics (AREA)
• Organic Chemistry (AREA)
• Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
• Manufacture Of Macromolecular Shaped Articles (AREA)
• Laminated Bodies (AREA)
• Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Priority Applications (5)

Applications Claiming Priority (2)

Publications (2)

Family

ID=21752331

Family Applications (1)

Country Status (14)

Cited By (2)

Families Citing this family (8)

Citations (2)

• 1997
  • 1997-02-19 JP JP9529582A patent/JP2000504771A/ja not_active Ceased
  • 1997-02-19 ZA ZA971401A patent/ZA971401B/xx unknown
  • 1997-02-19 AU AU19628/97A patent/AU1962897A/en not_active Abandoned
  • 1997-02-19 WO PCT/US1997/002585 patent/WO1997030111A1/en not_active Application Discontinuation
  • 1997-02-19 CA CA002247082A patent/CA2247082A1/en not_active Abandoned
  • 1997-02-19 BR BR9707592A patent/BR9707592A/pt unknown
  • 1997-02-19 CN CN97193277A patent/CN1214709A/zh active Pending
  • 1997-02-19 TR TR1998/01619T patent/TR199801619T2/xx unknown
  • 1997-02-19 EP EP97907693A patent/EP0882087A1/en not_active Withdrawn
  • 1997-02-19 KR KR1019980706484A patent/KR19990087096A/ko not_active Application Discontinuation
  • 1997-02-20 TW TW086102025A patent/TW358819B/zh active
  • 1997-02-20 ID IDP970505A patent/ID17762A/id unknown
  • 1997-02-20 AR ARP970100671A patent/AR005920A1/es not_active Application Discontinuation
• 1998
  • 1998-08-19 NO NO983793A patent/NO983793L/no not_active Application Discontinuation

Patent Citations (2)

Also Published As

Similar Documents

Legal Events