POLYETHYLENE MIXTURES AND FILMS

Description

FIELD OF THE INVENTION

[0001] The present disclosure relates to films made of polyethylene blends.BACKGROUND OF THE INVENTION

[0002] When blending two polyethylene compositions having narrow molecular weight distributions or narrow composition distributions, trade-off patterns are often observed amongst various film properties with the variations in molecular weight distribution and / or composition distribution. For instance, certain polyethylene blends are found to be superior in dart impact but inferior in Elmendorf Tear when compared to the primary polyethylene blend or conventional counterpart. Such trade-off paradigm has been one of the major hurdles for the breakthrough of new polyethylene product technology. WO 01 / 60907 A1 relates to a blend of metallocene produced polyethylenes (mPE), one of which has a narrow molecular weight distribution and narrow composition distribution, the other has a broader molecular weight distribution and a more narrow composition distribution.

[0003] A need exists, therefore, for polyethylene blends which overcome this trade-off paradigm and provide improved film properties to produce new products.SUMMARY OF THE INVENTION

[0004] Provided herein are films having an Elmendorf tear in MD greater than or equal to 14.2 g / µm (360 g / mil) and a puncture peak force greater than or equal to 214 g / µm (12.0 lb / mil) or a puncture break energy greater than or equal to 165 N-m / mm (37.0 in-lb / mil) comprising a polyethylene blend as described in the attached claims.BRIEF DESCRIPTION OF THE DRAWINGS

[0005] <a href='javascript:;' class="see-img-anchor" img-id="IMGF0001" img-title="FIG. 1 ("Fig. 1">FIG. 1 ("Fig. 1") shows the polyethylene compositions used as blending components to produce the primary polyethylene blends and the secondary polyethylene blends described herein, or those compositions used as a control. FIG. 2A and Fig. 2B are graphs showing the unexpected synergistic effects of the secondary polyethylene blends over the primary polyethylene blends leading to unprecedented combination of desirable features over the controls. FIG. 3 is a graph of puncture of the secondary polyethylene blends and the primary polyethylene blends described herein. FIG. 4 is a graph of a Temperature Rising Elution Fractionation ("TREF") curves of the secondary polyethylene blend described herein and the primary polyethylene blends. Co-crystallization (change of crystallization behavior) is shown between polyethylene compositions F5 and B5 in the secondary blend. This may explain the unexpected synergistic effectors in puncture for example. FIG. 5A is a graph of heat seal curves of film at 1 mil and shows heat seal strength as a function of seal temperature for films made from the secondary polyethylene blend 4CB-15. This secondary polyethylene blend exhibits 10 to 20 °C lower seal initiation temperature than the control of the same nominal density and MI. FIG. 5B is a graph of hot tack curves at 1 mil, showing hot tack seal strength as a function of seal temperature for films made of the secondary polyethylene blend 4CB-15. This secondary polyethylene blend exhibits 20+°C lower seal initiation temperature than the control of the same nominal density and MI. DESCRIPTION OF THE PREFERRED EMBODIMENTS

[0006] For the purposes of this disclosure, the following definitions will apply: As used herein, the terms "a" and "the" as used herein are understood to encompass the plural as well as the singular.

[0007] The term "alpha-olefin" refers to an olefin having a terminal carbon-to-carbon double bond in the structure thereof (R 1< R 2< )-C=CH 2 , where R 1< and R 2< can be independently hydrogen or any hydrocarbyl group. In an aspect, R 1< is hydrogen, and R 2< is an alkyl group. A "linear alpha-olefin" is an alpha-olefin as defined in this paragraph wherein R 1< is hydrogen, and R 2< is hydrogen or a linear alkyl group.

[0008] The term "average," when used to describe a physical property measured in multiple directions, means the average value of the property in each direction. For example, secant modulus can be measured by straining an object in the machine direction (MD) or in the transverse direction (TD). For example, the "average MD / TD 1% secant modulus" or "average 1% secant modulus" refers to the average of the MD secant modulus and the TD secant modulus at 1% strain.

[0009] The term "broad orthogonal comonomer distribution" ("BOCD") is used herein to mean across the molecular weight range of the ethylene polymer, comonomer contents for the various polymer fractions are not substantially uniform and a higher molecular weight fraction thereof generally has a higher comonomer content than that of a lower molecular weight fraction. Both a substantially uniform and an orthogonal comonomer distribution may be determined using fractionation techniques such as gel permeation chromatography-differential viscometry (GPC-DV), temperature rising elution fraction-differential viscometry (TREF-DV) or cross-fractionation techniques.

[0010] A "catalyst system" as used herein may include one or more polymerization catalysts, activators, supports / carriers, or any combination thereof.

[0011] The terms "catalyst system" and "catalyst" are used interchangeably herein.

[0012] The term "composition distribution breadth index" ("CDBI") refers to the weight percent of the copolymer molecules having a comonomer content within 50% of the median total molar comonomer content. The CDBI of any copolymer is determined utilizing known techniques for isolating individual fractions of a sample of the copolymer. Exemplary is Temperature Rising Elution Fraction ("TREF") described in Wild, et al., J. Poly. Sci., Poly. Phys. Ed., Vol. 20, pg. 441 (1982) and U.S. Pat. No. 5,008,204.

[0013] As used herein, the term "copolymer" refers to polymers having more than one type of monomer, including interpolymers, terpolymers, or higher order polymers.

[0014] The term "C n group" or "C n compound" refers to a group or a compound with total number carbon atoms "n." Thus, a C m -C n group or compound refers to a group or a compound having total number of carbon atoms in a range from m to n. For example, a C 1 -C 50 alkyl group refers to an alkyl compound having 1 to 50 carbon atoms.

[0015] As used herein, the terms "cyclopentadiene" and "cyclopentadienyl" are abbreviated as "Cp."

[0016] All numerical values within the detailed description and the claims herein are modified by "about" or "approximately" the indicated value, taking into account experimental error and variations.

[0017] Unless otherwise specified, the term "density" refers to the density of the polyethylene composition or polyethylene blend independent of any additives, such as antiblocks, which may change the tested value.

[0018] As used herein, in reference to Periodic Table Groups of Elements, the "new" numbering scheme for the Periodic Table Groups are used as in the CRC HANDBOOK OF CHEMISTRY AND PHYSICS (David R. Lide ed., CRC Press 81st ed. 2000).

[0019] As used herein, the term "heat seal initiation temperature" means the temperature at which a heat seal forms immediately after the sealing operation, the strength of the heat seal being measured at a specified time interval (milliseconds) after completion of the sealing cycle and after the seal has cooled to ambient temperature and reached maximum strength. The strength of the seal is often specified - for example, the "heat seal initiation temperature at 5 N" refers to the temperature at which a seal is formed that will have a strength of 5 N after cooling. Heat seal initiation temperature can be measured by ASTM F1921.

[0020] As used herein, the term "hot tack seal initiation temperature" means the temperature at which a heat seal forms immediately after the sealing operation, the strength of the heat seal being measured at a specified time interval (milliseconds) after completion of the sealing cycle and before the seal has cooled to ambient temperature and reached maximum strength. The strength of the seal is often specified - for example, the "heat seal initiation temperature at 1 N" refers to the temperature at which a hot 1 N seal is formed. Hot tack seal initiation temperature can be measured by ASTM F1921.

[0021] The term "hot tack" refers to the peel force of a sealing area when it is not completely cooled down. The term "heat seal strength" refers to the peel force when the sealing area is completely cooled down. Hot tack force and heat seal strength of the same material are typically different from each other.

[0022] As used herein, the term "linear low density polyethylene" ("LLDPE") means polyethylene having a significant number of short branches. LLDPEs can be distinguished structurally from conventional LDPEs because LLDPEs typically have minimal long chain branching and more short chain branching than LDPEs.

[0023] The term "metallocene catalyzed linear low density polyethylene" ("mLLDPE") refers to an LLDPE composition produced with a metallocene catalyst.

[0024] The term "linear medium density polyethylene" ("MDPE") refers to a polyethylene having a density from about 0.930 g / cm 3< to about 0.950 g / cm 3< .

[0025] As used herein, the term "metallocene catalyst" refers to a catalyst having at least one transition metal compound containing one or more substituted or unsubstituted Cp moiety (typically two Cp moieties) in combination with a Group 4, 5, or 6 transition metal. A metallocene catalyst is considered a single site catalyst. Metallocene catalysts generally require activation with a suitable co-catalyst, or activator, in order to yield an "active metallocene catalyst", i.e., an organometallic complex with a vacant coordination site that can coordinate, insert, and polymerize olefins. Active catalyst systems generally include not only the metallocene complex, but also an activator, such as an alumoxane or a derivative thereof (preferably methyl alumoxane), an ionizing activator, a Lewis acid, or a combination thereof. Alkylalumoxanes (typically methyl alumoxane and modified methylalumoxanes) are particularly suitable as catalyst activators. The catalyst system can be supported on a carrier, typically an inorganic oxide or chloride or a resinous material such as, for example, polyethylene or silica. When used in relation to metallocene catalysts, the term "substituted" means that a hydrogen group has been replaced with a hydrocarbyl group, a heteroatom, or a heteroatom containing group. For example, methylcyclopentadiene is a Cp group substituted with a methyl group.

[0026] The term "melt index" ("MI") is the number of grams extruded in 10 minutes under the action of a standard load and is an inverse measure of viscosity. A high MI implies low viscosity and a low MI implies high viscosity. In addition, polymers are shear thinning, which means that their resistance to flow decreases as the shear rate increases. This is due to molecular alignments in the direction of flow and disentanglements.

[0027] As provided herein, MI (I 2 ) is determined according to ASTM D-1238-E (190 °C / 2.16 kg), also sometimes referred to as I 2 or I 2.16 .

[0028] As provided herein, MI (I 21 ) is determined according to ASTM D-1238-E (190 °C / 21.6 kg), also sometimes referred to as I 21 or I 21.6 .

[0029] The "melt index ratio" ("MIR") provides an indication of the amount of shear thinning behavior of the polymer and is a parameter that can be correlated to the overall polymer mixture molecular weight distribution data obtained separately by using Gel Permeation Chromatography ("GPC") and possibly in combination with another polymer analysis including TREF. MIR is the ratio of I 21 / I 2 .

[0030] The term "melt strength" is a measure of the extensional viscosity and is representative of the maximum tension that can be applied to the melt without breaking. Extensional viscosity is the polyethylene composition's ability to resist thinning at high draw rates and high draw ratios. In melt processing of polyolefins, the melt strength is defined by two key characteristics that can be quantified in process-related terms and in rheological terms. In extrusion blow molding and melt phase thermoforming, a branched polyolefin of the appropriate molecular weight can support the weight of the fully melted sheet or extruded portion prior to the forming stage. This behavior is sometimes referred to as sag resistance.

[0031] As used herein, "M n " is number average molecular weight, "M w " is weight average molecular weight, and "M z " is z-average molecular weight. Unless otherwise noted, all molecular weight units (e.g., M w , M n , M z ) including molecular weight data are in the unit of g·mol -1< .

[0032] As used herein, unless specified otherwise, percent by mole is expressed as "mole %," and percent by weight is expressed as "wt%."

[0033] Molecular weight distribution ("MWD") is a measure of the spread of a polymer's molecular weight. A given polymer sample comprises molecules of varying chain length, and thus molecular weight, so the molecular weight of a polymer is represented as a distribution rather than as a single value. MWD is typically characterized as "broad" or "narrow." MWD is equivalent to the expression M w / M n and is also referred to as polydispersity index ("PDI"). The expression M w / M n is the ratio of M w to M n . M w is given by M w = ∑ i n i M i 2 ∑ i n i M i M n is given by M n = ∑ i n i M i ∑ i n i M z is given by M z = ∑ i n i M i 3 ∑ i n i M i 2 where n i in the foregoing equations is the number fraction of molecules of molecular weight M i . Measurements of M w , M z , and M n are typically determined by Gel Permeation Chromatography as disclosed in Macromolecules, Vol. 34, No. 19, pg. 6812 (2001). The measurements proceed as follows. Gel Permeation Chromatography (Agilent PL-220), equipped with three in-line detectors, a differential refractive index detector ("DRI"), a light scattering (LS) detector, and a viscometer, is used. Experimental details, including detector calibration, are described in: T. Sun, P. Brant, R. R. Chance, and W. W. Graessley, Macromolecules, Volume 34, Number 19, pp. 6812-6820, (2001). Three Agilent PLgel 10µm Mixed-B LS columns are used. The nominal flow rate is 0.5 mL / min, and the nominal injection volume is 300 µL. The various transfer lines, columns, viscometer and differential refractometer (the DRI detector) are contained in an oven maintained at 145°C. Solvent for the experiment is prepared by dissolving 6 grams of butylated hydroxytoluene as an antioxidant in 4 liters of Aldrich reagent grade 1,2,4-trichlorobenzene (TCB). The TCB mixture is then filtered through a 0.1 µm Teflon filter. The TCB is then degassed with an online degasser before entering the GPC-3D. Polymer solutions are prepared by placing dry polymer in a glass container, adding the desired amount of TCB, then heating the mixture at 160°C with continuous shaking for about 2 hours. All quantities are measured gravimetrically. The TCB densities used to express the polymer concentration in mass / volume units are about 1.463 g / ml at about 21°C and about 1.284 g / ml at about 145°C. The injection concentration is from 0.5 to 2.0 mg / ml, with lower concentrations being used for higher molecular weight samples. Prior to running each sample, the DRI detector and the viscometer are purged. The flow rate in the apparatus is then increased to 0.5 ml / minute, and the DRI is allowed to stabilize for 8 hours before injecting the first sample. The LS laser is turned on at least 1 to 1.5 hours before running the samples. The concentration, c, at each point in the chromatogram is calculated from the baseline-subtracted DRI signal, I DRI , using the following equation: c = K DRI I DRI / dn / dc , where K DRI is a constant determined by calibrating the DRI, and (dn / dc) is the refractive index increment for the system. The refractive index, n = 1.500 for TCB at 145°C. Units on parameters throughout this description of the GPC-3D method are such that concentration is expressed in g / cm 3< , molecular weight is expressed in g / mole, and intrinsic viscosity is expressed in dL / g.

[0034] The LS detector is a Wyatt Technology High Temperature DAWN HELEOS. The molecular weight, M, at each point in the chromatogram is determined by analyzing the LS output using the Zimm model for static light scattering (M.B. Huglin, LIGHT SCATTERING FROM POLYMER SOLUTIONS, Academic Press, 1971): K o c ΔR θ = 1 MP θ + 2 A 2 c .

[0035] Here, ΔR(θ) is the measured excess Rayleigh scattering intensity at scattering angle θ, c is the polymer concentration determined from the DRI analysis, A 2 is the second virial coefficient. P(θ) is the form factor for a monodisperse random coil, and K o is the optical constant for the system: K o = 4 π 2 n 2 dn / dc 2 λ 4 N A , where N A is Avogadro's number, and (dn / dc) is the refractive index increment for the system, which take the same value as the one obtained from DRI method. The refractive index, n = 1.500 for TCB at 145°C and λ = 657 nm. A high temperature Viscotek Corporation viscometer, which has four capillaries arranged in a Wheatstone bridge configuration with two pressure transducers, can be used to determine specific viscosity. One transducer measures the total pressure drop across the detector, and the other, positioned between the two sides of the bridge, measures a differential pressure. The specific viscosity, η s , for the solution flowing through the viscometer is calculated from their outputs. The intrinsic viscosity, [η], at each point in the chromatogram is calculated from the following equation: η S = c η + 0.3 c η 2 , where c is concentration and was determined from the DRI output.

[0036] The branching index (g' vis ) is calculated using the output of the GPC-DRI-LS-VIS method as follows. The average intrinsic viscosity, [η] avg of the sample is calculated by: η avg = ∑ c i η i ∑ c i , where the summations are over the chromatographic slices, i, between the integration limits.

[0037] The branching index g' vis is defined as: g ′ vis = η avg kM v α . M V is the viscosity-average molecular weight based on molecular weights determined by LS analysis. Z average branching index (g' Zave ) is calculated using Ci = polymer concentration in the slice i in the polymer peak times the mass of the slice squared, Mi 2< . All molecular weights are weight average unless otherwise noted. All molecular weights are reported in g / mol unless otherwise noted. This method is the preferred method of measurement and used in the examples and throughout the disclosures unless otherwise specified. See also, Macromolecules, Vol. 34, No. 19, Effect of Short Chain Branching on the Coil Dimensions of Polyolefins in Dilute Solution, Sun et al., pg. 6812-6820 (2001).

[0038] As used herein, the term "olefin" refers to a linear, branched, or cyclic compound comprising carbon and hydrogen and having a hydrocarbon chain containing at least one carbon-to-carbon double bond in the structure thereof, where the carbon-to-carbon double bond does not constitute a part of an aromatic ring. The term olefin includes all structural isomeric forms of olefins, unless it is specified to mean a single isomer or the context clearly indicates otherwise.

[0039] As used herein, the term "polymer" refers to a compound having two or more of the same or different "mer" units. A "homopolymer" is a polymer having mer units that are the same. A "copolymer" is a polymer having two or more mer units that are different from each other. A "terpolymer" is a polymer having three mer units that are different from each other. "Different" in reference to mer units indicates that the mer units differ from each other by at least one atom or are different isomerically.

[0040] As used herein, the term "comonomer" refers to the unique mer units in a copolymer. Since comonomers in a copolymer have non-identical MWDs, the composition of the copolymer varies at different molecular weights. As with MWD, comonomer composition must be represented as a distribution rather than as a single value. The term "composition distribution," or "comonomer distribution," is a measure of the spread of a copolymer's comonomer composition. Composition distribution is typically characterized as "broad" or "narrow."

[0041] As used herein, when a polymer or copolymer is referred to as comprising an olefin, the olefin present in such polymer or copolymer is the polymerized form of the olefin. For example, when a copolymer is said to have a "propylene" content of 35 wt% to 55 wt%, it is understood that the mer unit in the copolymer is derived from propylene in the polymerization reaction and said derived units are present at 35 wt% to 55 wt%, based upon the weight of the copolymer. A copolymer can be terpolymers and the like.

[0042] As used herein, the terms "polymerization temperature" and "reactor temperature" are interchangeable.

[0043] The term "substantially uniform comonomer distribution" is used herein to mean that comonomer content of the polymer fractions across the molecular weight range of the ethylene-based polymer vary by < 10.0 wt%. In an aspect, a substantially uniform comonomer distribution refers to < 8.0 wt%, < 5.0 wt%, or < 2.0 wt%.

[0044] As used herein, the term "supported" refers to one or more compounds that are deposited on, contacted with, vaporized with, bonded to, incorporated within, adsorbed or absorbed in, or on, a support or carrier. The terms "support" and "carrier" can be used interchangeably and include any support material including, but not limited to, a porous support material or inorganic or organic support materials. Non-limiting examples of inorganic support materials include inorganic oxides and inorganic chlorides. Other carriers include resinous support materials such as polystyrene, functionalized or cross-linked organic supports, such as polystyrene, divinyl benzene, polyolefins, or polymeric compounds, zeolites, talc, clays, or any other organic or inorganic support material and the like, or mixtures thereof.

[0045] In an extrusion process, "viscosity" is a measure of resistance to shearing flow. Shearing is the motion of a fluid, layer-by-layer, like a deck of cards. When polymers flow through straight tubes or channels, the polymers are sheared and resistance is expressed in terms of viscosity.

[0046] "Extensional" or "elongational viscosity" is the resistance to stretching. In fiber spinning, film blowing and other processes where molten polymers are stretched, the elongational viscosity plays a role. For example, for certain liquids, the resistance to stretching can be three times larger than in shearing. For some polymeric liquids, the elongational viscosity can increase (tension stiffening) with the rate, although the shear viscosity decreased.

[0047] Various film property measurements described herein may be based on certain standardized testing procedures. For example, measurements of tensile strength in the machine direction ("MD") and transverse direction ("TD") can be made using the standard test method of ASTM D882. Measurements of yield strength in MD and TD can be made using the standard test method of ASTM D882. Measurements of Elmendorf tear in MD can be made using the standard test method of ASTM D1922 and / or ASTM 1424. Measurements for 1% secant modulus can be made using the standard test method of ASTM D790A. Measurements for puncture peak force and puncture break energy can be measured using the standard test method of ASTM F1306. Measurements of dart-drop (sometimes referred to herein as "dart impact") can be made using the standard test method of ASTM D1709 and / or the protocol of ISO 7765. Gloss can be measured using the procedure of ASTM D523. Light transmission percent (or haze) measurements can be made using the procedure of ASTM D1003 using a haze meter Haze-Guard Plus AT-4725 from BYK Gardner and defined as the percentage of transmitted light passing through the bulk of the film sample that is deflected by more than 2.5°.

[0048] The "secant modulus" is the slope of a line connecting the origin to an object's stress / strain curve at a specified strain percentage. For example, the "1% secant modulus" is the slope of a line connecting the origin to an object's stress / strain curve at 1% strain. The secant modulus describes the overall stiffness of an object. Lower strain percentages typically approximate elastic behavior more accurately. Measurements for 1% secant modulus can be made by following the procedure of ASTM D790A.

[0049] The term "tensile strength" refers to the stretching force required to inelastically deform a material. The tensile strength of a material can be measured by stretching the material in MD or TD. The "average MD / TD tensile strength" thus refers to the average of the MD tensile strength and the TD tensile strength. Tensile strength can be measured in psi and as set out in the standard test methods of ASTM D638 or ASTM D882.

[0050] Provided herein are films made of secondary polyethylene blends comprising two primary polyethylene blends. Films made of the secondary polyethylene blends have been found to overcome the trade-off paradigm (referred to above) as several observed synergistic effects have resulted in the novel combinations of desirable film properties and features. Generally, the primary polyethylene blends were each targeted to have about 1.0 melt index ("MI") and a density of 0.920 g / cm 3< . More specifically, the primary polyethylene blends have a density between 0.918 g / cm 3< and 0.922 g / cm 3< and an MI (I 2 ) between 0.90 g / 10 min and 1.10 g / 10 min. As described herein, each primary polyethylene blend comprises two polyethylene compositions, each polyethylene composition having a density. The difference in the density of the polyethylene compositions (sometimes referred to as the "density spread") is between 0.050 g / cm 3< and 0.060 g / cm 3< or in an aspect, about 0.055 g / cm 3< .

[0051] As provided in the examples, a series of secondary polyethylene blends were blended for blow film evaluation and compared with the primary polyethylene blend. The secondary polyethylene blends were found in general to show synergistic effects in Puncture, Gloss and MD-Tear over the primary polyethylene blend. At the same time, the secondary polyethylene blends typically maintained stiffness and sealing advantage of the primary polyethylene blend. In short, the trade-off paradigm among various performance attributes has been one of the major hurdles in development of new film product applications and technologies. With the so-called secondary blend approach described herein, such trade-off paradigm was effectively removed, leading to unprecedented combinations of desirable features.

[0052] The present films made from the secondary polyethylene blends described herein have an Elmendorf tear in MD greater than or equal to 14.2 g / µm (360 g / mil) and a puncture peak force greater than or equal to 214 g / µm (12.0 lb / mil) or a puncture break energy greater than or equal to 165 N-m / mm (37.0 in-lb / mil). In addition, the present films can have a heat seal initiation temperature at 5 N less than or equal to 100°C. Furthermore, these films can have a hot tack seal initiation temperature at 1 N less than or equal to 100°C and can have a dart drop greater than or equal to 7.5 g / µm (190 g / mil). The subject films were shown to have an average gloss between 45 GU and 70 GU. The present films also have an average 1% secant modulus greater than or equal to 207 MPa (30,000 psi) and an average yield strength greater than or equal to 9.2 MPa(1340 psi). As described herein, the present films can have an average tensile strength greater than or equal to 52 MPa (7490 psi).

[0053] As described in the examples, the secondary polyethylene blends comprise two primary polyethylene blends, each primary polyethylene blend comprising two polyethylene compositions.

[0054] In an aspect, the primary polyethylene blend comprises the polyethylene composition having a density of about 0.8961 g / cm 3< and an MI (I 2 ) of about 0.28 g / 10 min in an amount between about 55 wt% and about 57 wt%, and another polyethylene composition having a density of about 0.9510 g / cm 3< and an MI (I 2 ) of about 14.2 g / 10 min in an amount between about 43 wt% and about 45 wt%.

[0055] In an aspect, the primary polyethylene blend comprises the polyethylene composition having a density of about 0.8983 g / cm 3< and an MI (I 2 ) of about 7.8 g / 10 min in an amount between about 56 wt% and about 58 wt%, and another polyethylene composition having a density of about 0.9516 g / cm 3< and an MI (I 2 ) of about 0.20 g / 10 min in an amount between about 42 wt% and about 44 wt%.

[0056] In an aspect, the primary polyethylene blend comprises the polyethylene composition having density of about 0.9078 g / cm 3< and an MI (I 2 ) of about 3.1 g / 10 min in an amount between about 52 wt% and about 54 wt%, and another polyethylene composition has a density of about 0.9369 g / cm 3< and an MI (I 2 ) of about 0.44 g / 10 min in an amount between about 46 wt% and about 48 wt%.

[0057] In an aspect, the primary polyethylene blend comprises the polyethylene composition having a density of about 0.9082 g / cm 3< and an MI (I 2 ) of about 0.48 g / 10 min in an amount between about 56 wt% and about 58 wt%, and another polyethylene composition having a density of about 0.9389 g / cm 3< and an MI (I 2 ) of about 3.0 g / 10 min in an amount between about 42 wt% and about 44 wt%.

[0058] In an aspect, the primary polyethylene blend comprises the polyethylene composition having a density of about 0.8961 g / cm 3< and an MI (I 2 ) of about 0.28 g / 10 min in an amount between about 39 wt% and about 41 wt%, and another polyethylene composition having a density of about 0.9389 g / cm 3< and an MI (I 2 ) of about 3.0 g / 10 min in an amount between about 59 wt% and about 61 wt%.

[0059] In an aspect, the primary polyethylene blend comprises the polyethylene composition having a density of about 0.8983 g / cm 3< and an MI (I 2 ) of about 7.8 g / 10 min in an amount between about 38 wt% and about 40 wt%, and another polyethylene composition having a density of about 0.9369 g / cm 3< and an MI (I 2 ) of about 0.44 g / 10 min in an amount between about 60 wt% and about 62 wt%.

[0060] In an aspect, the primary polyethylene blend comprises the polyethylene composition having a density of about 0.9082 g / cm 3< and an MI (I 2 ) of about 0.48 g / 10 min in an amount between about 70 wt% and about 72 wt%, and another polyethylene composition has a density of about 0.9510 g / cm 3< and an MI (I 2 ) of about 14.2 g / 10 min in an amount between about 28 wt% and about 30 wt%.

[0061] In an aspect, in the primary polyethylene blend comprises the polyethylene composition having a density of about 0.9078 g / cm 3< and an MI (I 2 ) of about 3.1 g / 10 min in an amount between about 69 wt% and about 71 wt%, and the other polyethylene composition has a density of about 0.9516 g / cm 3< and an MI (I 2 ) of about 0.20 g / 10 min in an amount between about 29 wt% and about 31 wt%.

[0062] In an aspect, the polyethylene compositions have an M w / M n between about 2.5 and about 3.0 and / or the primary polyethylene blends have an M w / M n between about 2.5 and about 4.0.

[0063] The secondary polyethylene blend can comprise two primary polyethylene blends in the amount of about 50 wt% of each primary polyethylene blend. For example, the secondary polyethylene blend can comprise the primary polyethylene blend comprising the polyethylene composition having a density of about 0.8961 g / cm 3< and an MI (I 2 ) of about 0.28 g / 10 min in an amount between about 55 wt% and about 57 wt%, and another polyethylene composition having a density of about 0.9510 g / cm 3< and an MI (I 2 ) of about 14.2 g / 10 min in an amount between about 43 wt% and about 45 wt%. The other primary polyethylene blend of this secondary polyethylene blend comprises the polyethylene composition having a density of about 0.8983 g / cm 3< and an MI (I 2 ) of about 7.8 g / 10 min in an amount between about 56 wt% and about 58 wt%, and another polyethylene composition having a density of about 0.9516 g / cm 3< and an MI (I 2 ) of about 0.20 g / 10 min in an amount between about 42 wt% and about 44 wt%.

[0064] Likewise, the secondary polyethylene blend can comprise the primary polyethylene comprising the polyethylene composition having density of about 0.9078 g / cm 3< and an MI (I 2 ) of about 3.1 g / 10 min in an amount between about 52 wt% and about 54 wt%, and another polyethylene composition has a density of about 0.9369 g / cm 3< and an MI (I 2 ) of about 0.44 g / 10 min in an amount between about 46 wt% and about 48 wt%. The other primary polyethylene blend of this secondary polyethylene blend comprises the polyethylene composition having a density of about 0.9082 g / cm 3< and an MI (I 2 ) of about 0.48 g / 10 min in an amount between about 56 wt% and about 58 wt%, and another polyethylene composition having a density of about 0.9389 g / cm 3< and an MI (I 2 ) of about 3.0 g / 10 min in an amount between about 42 wt% and about 44 wt%.

[0065] The secondary polyethylene blend can comprise the primary polyethylene blend having the polyethylene composition with a density of about 0.8961 g / cm 3< and an MI (I 2 ) of about 0.28 g / 10 min in an amount between about 39 wt% and about 41 wt%, and another polyethylene composition having a density of about 0.9389 g / cm 3< and an MI (I 2 ) of about 3.0 g / 10 min in an amount between about 59 wt% and about 61 wt%. The other primary polyethylene blend of this secondary polyethylene blend can comprise the polyethylene composition having a density of about 0.8983 g / cm 3< and an MI (I 2 ) of about 7.8 g / 10 min in an amount between about 38 wt% and about 40 wt%, and another polyethylene composition having a density of about 0.9369 g / cm 3< and an MI (I 2 ) of about 0.44 g / 10 min in an amount between about 60 wt% and about 62 wt%.

[0066] In an aspect, the secondary polyethylene blend can comprise the primary polyethylene blend comprising the polyethylene composition having a density of about 0.9082 g / cm 3< and an MI (I 2 ) of about 0.48 g / 10 min in an amount between about 70 wt% and about 72 wt%, and another polyethylene composition has a density of about 0.9510 g / cm 3< and an MI (I 2 ) of about 14.2 g / 10 min in an amount between about 28 wt% and about 30 wt%. The other primary polyethylene blend comprises the polyethylene composition having a density of about 0.9078 g / cm 3< and an MI (I 2 ) of about 3.1 g / 10 min in an amount between about 69 wt% and about 71 wt%, and the other polyethylene composition has a density of about 0.9516 g / cm 3< and an MI (I 2 ) of about 0.20 g / 10 min in an amount between about 29 wt% and about 31 wt%.

[0067] In aspect, the secondary polyethylene blend can comprise two primary polyethylene blends in the amount of about 40 wt% of each primary polyethylene blend. Here, the secondary polyethylene blend can further comprise yet another polyethylene composition having a density of about 0.918 g / cm 3< and an MI (I 2 ) of about 1.0 g / 10 min in an amount about 20 wt%.

[0068] For example, the secondary polyethylene blend can comprise two primary polyethylene blends in the amount of about 40 wt% of each primary polyethylene blend where one of the primary polyethylene blends comprises the polyethylene composition having a density of about 0.8961 g / cm 3< and an MI (I 2 ) of about 0.28 g / 10 min in an amount between about 55 wt% and about 57 wt%, and another polyethylene composition having a density of about 0.9510 g / cm 3< and an MI (I 2 ) of about 14.2 g / 10 min in an amount between about 43 wt% and about 45 wt%. The other primary polyethylene blend of this secondary polyethylene blend comprises the polyethylene composition having a density of about 0.8983 g / cm 3< and an MI (I 2 ) of about 7.8 g / 10 min in an amount between about 56 wt% and about 58 wt%, and another polyethylene composition having a density of about 0.9516 g / cm 3< and an MI (I 2 ) of about 0.20 g / 10 min in an amount between about 42 wt% and about 44 wt%. The secondary polyethylene blend further comprises another polyethylene composition having a density of about 0.918 g / cm 3< and an MI (I 2 ) of about 1.0 g / 10 min in an amount about 20 wt%.

[0069] In aspect, the secondary polyethylene blend comprises two primary polyethylene blends in the amount of about 40 wt% of each primary polyethylene blend and further comprises another polyethylene composition having a density of about 0.918 g / cm 3< and an MI (I 2 ) of about 1.0 g / 10 min in an amount about 20 wt%. Here, one of the primary polyethylene blends comprises the polyethylene composition having a density of about of about 0.9078 g / cm 3< and an MI (I 2 ) of about 3.1 g / 10 min in an amount between about 52 wt% and about 54 wt%, and another polyethylene composition has a density of about 0.9369 g / cm 3< and an MI (I 2 ) of about 0.44 g / 10 min in an amount between about 46 wt% and about 48 wt%. The other primary polyethylene blend of this secondary polyethylene blend comprises the polyethylene composition having a density of about 0.9082 g / cm 3< and an MI (I 2 ) of about 0.48 g / 10 min in an amount between about 56 wt% and about 58 wt%, and another polyethylene composition having a density of about 0.9389 g / cm 3< and an MI (I 2 ) of about 3.0 g / 10 min in an amount between about 42 wt% and about 44 wt%.

[0070] Additional secondary polyethylene compositions used to produce the present films can have various components (primary polyethylene blends and polyethylene compositions) in various amounts (wt%) are described herein and, particularly, in the examples below.Polyethylene Compositions

[0071] As described herein, the present polyethylene compositions comprise from about 50.0 mol% to about 100.0 mol% of units derived from ethylene. The lower limit on the range of ethylene content can be from 50.0 mol%, 75.0 mol%, 80.0 mol%, 85.0 mol%, 90.0 mol%, 92.0 mol%, 94.0 mol%, 95.0 mol%, 96.0 mol%, 97.0 mol%, 98.0 mol%, or 99.0 mol% based on the mol% of polymer units derived from ethylene. The polyethylene composition can have an upper limit on the range of ethylene content of 80.0 mol%, 85.0 mol%, 90.0 mol%, 92.0 mol%, 94.0 mol%, 95.0 mol%, 96.0 mol%, 97.0 mol%, 98.0 mol%, 99.0 mol%, 99.5 mol%, or 100.0 mol%, based on mole % of polymer units derived from ethylene.

[0072] Further described herein are polyethylene compositions produced by polymerization of ethylene and, optionally, an alpha-olefin comonomer having from 3 to 10 carbon atoms. Alpha-olefin comonomers are selected from monomers having 3 to 10 carbon atoms, such as C 3 -C 10 alpha-olefins. Comonomers can be linear or branched or may include two unsaturated carbon-carbon bonds, i.e., dienes. Examples of suitable comonomers include linear C 3 -C 10 alpha-olefins and alpha-olefins having one or more C 1 -C 3 alkyl branches or an aryl group. Comonomer examples include propylene, 1-butene, 3-methyl-1-butene, 3,3-dimethyl-1-butene, 1-pentene, 1-pentene with one or more methyl, ethyl, or propyl substituents, 1-hexene, 1-hexene with one or more methyl, ethyl, or propyl substituents, 1-heptene, 1-heptene with one or more methyl, ethyl, or propyl substituents, 1-octene, 1-octene with one or more methyl, ethyl, or propyl substituents, 1-nonene, 1-nonene with one or more methyl, ethyl, or propyl substituents, ethyl, methyl, or dimethyl-substituted 1-decene, 1-dodecene, and styrene.

[0073] Exemplary combinations of ethylene and comonomers include: ethylene 1-butene, ethylene 1-pentene, ethylene 4-methyl-1-pentene, ethylene 1-hexene, ethylene 1-octene, ethylene decene, ethylene dodecene, ethylene 1-butene 1-hexene, ethylene 1-butene 1-pentene, ethylene 1-butene 4-methyl-1-pentene, ethylene 1-butene 1-octene, ethylene 1-hexene 1-pentene, ethylene 1-hexene 4-methyl-1-pentene, ethylene 1-hexene 1-octene, ethylene 1-hexene decene, ethylene 1-hexene dodecene, ethylene propylene 1-octene, ethylene 1-octene 1-butene, ethylene 1-octene 1-pentene, ethylene 1-octene 4-methyl-1-pentene, ethylene 1-octene 1-hexene, ethylene 1-octene decene, ethylene 1-octene dodecene, and combinations thereof. It should be appreciated that the foregoing list of comonomers and comonomer combinations are merely exemplary and are not intended to be limiting. Often, the comonomer is 1-butene, 1-hexene, or 1-octene.

[0074] During copolymerization, monomer feeds are regulated to provide a ratio of ethylene to comonomer, e.g., alpha-olefin, so as to yield a polyethylene having a comonomer content, as a bulk measurement, of from about 0.1 mol% to about 20 mol% comonomer. In other aspects the comonomer content is from about 0.1 mol% to about 4.0 mol%, or from about 0.1 mol% to about 3.0 mol%, or from about 0.1 mol% to about 2.0 mol%, or from about 0.5 mol% to about 5.0 mol%, or from about 1.0 mol% to about 5.0 mol%. The reaction temperature, monomer residence time, catalyst system component quantities, and molecular weight control agent (such as H 2 ) may be regulated so as to provide the polyethylene compositions. For linear polyethylenes, the amount of comonomers, comonomer distribution along the polymer backbone, and comonomer branch length will generally delineate the density range.

[0075] Comonomer content is based on the total content of all monomers in the polymer. The polyethylene copolymer has minimal long chain branching (i.e., less than 1.0 long-chain branch / 1000 carbon atoms, particularly 0.05 to 0.50 long-chain branch / 1000 carbon atoms). Such values are characteristic of a linear structure that is consistent with a branching index (as defined below) of g' vis ≥ 0.980, 0.985, ≥ 0.99, ≥ 0.995, or 1.0. While such values are indicative of little to no long chain branching, some long chain branches can be present (i.e., less than 1.0 long-chain branch / 1000 carbon atoms, or less than 0.5 long-chain branch / 1000 carbon atoms, particularly 0.05 to 0.50 long-chain branch / 1000 carbon atoms).

[0076] In an aspect, the present polyethylene compositions can include ethylene-based polymers which include LLDPE produced by gas-phase polymerization of ethylene and, optionally, an alpha-olefin with a catalyst having as a transition metal component a bis(n-C 3-4 alkyl cyclopentadienyl) hafnium compound, wherein the transition metal component comprises from about 95 to about 99 mol% of the hafnium compound.

[0077] Generally, polyethylene can be polymerized in any catalytic polymerization process, including solution phase processes, gas phase processes, slurry phase processes, and combinations of such processes. An exemplary process used to polymerize ethylene-based polymers, such as LLDPEs, is as described in U.S. Pat. Nos. 6,936,675 and 6,528,597.

[0078] The above-described processes can be tailored to achieve desired polyethylene compositions. For example, comonomer to ethylene concentration or flow rate ratios are commonly used to control composition density. Similarly, hydrogen to ethylene concentrations or flow rate ratios are commonly used to control composition molecular weight.

[0079] Polyethylene compositions described herein can be blended with LLDPE and other polymers, such as additional polymers prepared from ethylene monomers. Exemplary additional polymers are LLDPE, non-linear LDPE, very low density polyethylene ("VLDPE"), MDPE, high density polyethylene ("HDPE"), differentiated polyethylene ("DPE"), and combinations thereof. DPE copolymers include EVA, EEA, EMA, EBA, and other specialty copolymers. The additional polymers contemplated in certain aspects include ethylene homopolymers and / or ethylene-olefin copolymers. The product of blending one or more polyethylene compositions with other polymers is referred to as a polyethylene blend.

[0080] Polyethylene compositions can be composed of blended polymers include at least 0.1 wt% and up to 99.9 wt% of LLDPE, and at least 0.1 wt% and up to 99.9 wt% of one or more additional polymers, with these wt% based on the total weight of the polyethylene composition. Alternative lower limits of LLDPE can be 5%, 10%, 20%, 30%, 40%, or 50% by weight. Alternative upper limits of LLDPE can be 95%, 90%, 80%, 70%, 60%, and 50% by weight. Ranges from any lower limit to any upper limit are within the scope of the invention. Preferred blends include more than about 90% LLDPE, and preferably more than about 95% LLDPE. In an aspect, the blends include from 5-85%, alternatively from 10-50% or from 10-30% by weight of LLDPE. The balance of the weight percentage is the weight of the additional and / or other type of polymers, e.g., different LLDPE, LDPE, VLDPE, MDPE, HDPE, DPE such as EVA, EEA, EMA, EBA, and combinations thereof.

[0081] The polyethylene compositions can have a density greater than or equal to ("≥") about 0.895 g / cm 3< , ≥ about 0.896 g / cm 3< , ≥ about 0.897 g / cm 3< , ≥ about 0.898 g / cm 3< , ≥ about 0.899 g / cm 3< , ≥ about 0.900 g / cm 3< , ≥ about 0.910 g / cm 3< , ≥ about 0.920 g / cm 3< , 0.930 g / cm 3< , ≥ about 0.935 g / cm 3< , ≥ about 0.940 g / cm 3< , ≥ about 0.945 g / cm 3< , ≥ about 0.950 g / cm 3< , ≥ about 0.955 g / cm 3< , and ≥ about 0.960 g / cm 3< . Alternatively, polyethylene compositions can have a density less than or equal to ("≤") about 0.960 g / cm 3< about 0.950 g / cm 3< , e.g., ≤ about 0.940 g / cm 3< , ≤ about 0.930 g / cm 3< , ≤ about 0.920 g / cm 3< , ≤ about 0.910 g / cm 3< , ≤ about 0.900 g / cm 3< and ≤ about 0.890 g / cm 3< . These ranges include, but are not limited to, ranges formed by combinations any of the above-enumerated values, e.g., from about 0.895 to about 0.960 g / cm 3< , about 0.900 to about 0.950 g / cm 3< , about 0.910 about to 0.940 g / cm 3< , about 0.935 to about 0.950 g / cm 3< , etc. Density is determined using chips cut from plaques compression molded in accordance with ASTM D-1928-C, aged in accordance with ASTM D-618 Procedure A, and measured as specified by ASTM D-1505.

[0082] The polyethylene compositions have an MI according to ASTM D-1238-E (190°C / 2.16 kg) reported in grams per 10 minutes (g / 10 min), of ≥ about 0.10 g / 10 min, e.g., ≥ about 0.15 g / 10 min, ≥ about 0.18 g / 10 min, ≥ about 0.20 g / 10 min, ≥ about 0.22 g / 10 min, ≥ about 0.25 g / 10 min, ≥ about 0.28 g / 10 min, or ≥ about 0.30 g / 10 min.

[0083] Also, the polyethylene compositions can have an MI (I 2.16 ) ≤ about 3.0 g / 10 min, ≤ about 2.0 g / 10 min, ≤ about 1.5 g / 10 min, ≤ about 1.0 g / 10 min, ≤ about 0.75 g / 10 min, ≤ about 0.50 g / 10 min, ≤ about 0.40 g / 10 min, ≤ about 0.30 g / 10 min, ≤ about 0.25 g / 10 min, ≤ about 0.22 g / 10 min, ≤ about 0.20 g / 10 min, ≤ about 0.18 g / 10 min, or ≤ about 0.15 g / 10 min. The ranges, however, include, but are not limited to, ranges formed by combinations any of the above-enumerated values, for example: from about 0.1 to about 5.0; about 0.2 to about 2.0; and about 0.2 to about 0.5 g / 10 min.

[0084] The polyethylene compositions can have a melt index ratio ("MIR") that is a dimensionless number and is the ratio of the high load MI to the MI, or I 21.6 / I 2.16 , as described above. The MIR of the polyethylene compositions described herein is from about 25 to about 80, alternatively, from about 25 to about 70, alternatively, from about 30 to about 55, and alternatively, from about 35 to about 50.

[0085] The polyethylene compositions can have an orthogonal comonomer distribution. The term "orthogonal comonomer distribution" is used herein to mean across the molecular weight range of the ethylene polymer, comonomer contents for the various polymer fractions are not substantially uniform and a higher molecular weight fraction thereof generally has a higher comonomer content than that of a lower molecular weight fraction. Both a substantially uniform and an orthogonal comonomer distribution may be determined using fractionation techniques such as gel permeation chromatography-differential viscometry ("GPC-DV"), temperature rising elution fraction-differential viscometry ("TREF-DV") or cross-fractionation techniques.

[0086] In an aspect, the polyethylene composition can have at least a first peak and a second peak in a comonomer distribution analysis, wherein the first peak has a maximum at a log(M w ) value of 4.0 to 5.4, 4.3 to 5.0, or 4.5 to 4.7; and a TREF elution temperature of 70.0°C to 100.0°C, 80.0°C to 95.0°C, or 85.0°C to 90.0°C. The second peak in the comonomer distribution analysis has a maximum at a log(M w ) value of 5.0 to 6.0, 5.3 to 5.7, or 5.4 to 5.6; and a TREF elution temperature of 5.0°C to 60.0°C or 10.0°C to 60.0°C. A description of the TREF methodology is described in US 8,431,661 B2 and US 6,248,845 Bl.

[0087] The present polyethylene compositions typically have a broad composition distribution as measured by CDBI or solubility distribution breadth index ("SDBI"). For details of determining the CDBI or SDBI of a copolymer, see, for example, PCT Patent Application WO 93 / 03093, published Feb. 18, 1993. Polymers produced using a catalyst system described herein have a CDBI less than 50%, or less than 40%, or less than 30%. In an aspect, the polymers have a CDBI of from 20% to less than 50%. In an aspect, the polymers have a CDBI of from 20% to 35%. In an aspect, the polymers have a CDBI of from 25% to 28%.

[0088] Polyethylene composition are produced using a catalyst system described herein and have a SDBI greater than 15°C, or greater than 16°C, or greater than 17°C, or greater than 18°C, or greater than 20°C. In an aspect, the polymers have a SDBI of from 18°C to 22°C. In an aspect, the polymers have a SDBI of from 18.7°C to 21.4°C. In an aspect, the polymers have a SDBI of from 20°C to 22°C.

[0089] Certain of the present polyethylene compositions are sold under the EXCEED XP ®< trademark, including metallocene polyethylene compositions ("EXCEED XP ®< mPE"), which are available from ExxonMobil Chemical Company. EXCEED XP ™< mPE compositions offer step-out performance with respect to, for example, dart drop impact strength, flex-crack resistance, and machine direction (MD) tear, as well as maintaining stiffness at lower densities. EXCEED XP ™< mPE compositions also offer optimized solutions for a good balance of melt strength, toughness, stiffness, and sealing capabilities which makes this family of polymers well-suited for blown film / sheet solutions.

[0090] For example, EXCEED ™< 1018 polyethylene composition comprises ethylene 1-hexene copolymers and has a density of about 0.918 g / cm 3< and an MI (I 2 ) of about 1.0 g / 10 min.Conventional Catalyst

[0091] Conventional catalysts refer to Ziegler Natta catalysts or Phillips-type chromium catalysts. Examples of conventional-type transition metal catalysts are discussed in U.S. Patent Nos. 4,115,639, 4,077,904 4,482,687, 4,564,605, 4,721,763, 4,879,359 and 4,960,741. The conventional catalyst compounds that may be used in the processes disclosed herein include transition metal compounds from Groups 3 to 10, or Groups 4 to 6 of the Periodic Table of Elements.

[0092] These conventional-type transition metal catalysts may be represented by the formula:         MRx , where M is a metal from Groups 3 to 10, or Group 4, or titanium; R is a halogen or a hydrocarbyloxy group; and x is the valence of the metal M. In an aspect, x is 1, 2, 3 or 4, or x is 4. Non-limiting examples of R include alkoxy, phenoxy, bromide, chloride and fluoride. Non-limiting examples of conventional-type transition metal catalysts where M is titanium include TiCl3, TiCl4, TiBr4, Ti(OC2H5)3Cl, Ti(OC2H5)Cl3, Ti(OC4H9)3Cl, Ti(OC3H7)2Cl2, Ti(OC2H5)2Br2, TiCl3.1 / 3AlCl3 and Ti(OC12H25)Cl3. Conventional chrome catalysts, often referred to as Phillips-type catalysts, may include CrO3, chromocene, silyl chromate, chromyl chloride (CrO2Cl2), chromium-2-ethyl-hexanoate, chromium acetylacetonate (Cr(AcAc)3). Non-limiting examples are disclosed in U.S. Patent Nos. 2,285,721, 3,242,099 and 3,231,550. For optimization, many conventional-type catalysts require at least one cocatalyst. A detailed discussion of cocatalyst may be found in U.S. Patent No. 7,858,719, Col. 6, line 46, to Col. 7, line 45.Metallocene Catalysts

[0093] Metallocene catalysts (also referred to herein sometimes as metallocenes or metallocene compounds) are generally described as containing one or more ligand(s) and one or more leaving group(s) bonded to at least one metal atom, optionally with at least one bridging group. The ligands are generally represented by one or more open, acyclic, or fused ring(s) or ring system(s) or a combination thereof. These ligands, the ring(s) or ring system(s), can comprise one or more atoms selected from Groups 13 to 16 atoms of the Periodic Table of Elements; in an aspect, the atoms are selected from the group consisting of carbon, nitrogen, oxygen, silicon, sulfur, phosphorous, germanium, boron and aluminum or a combination thereof. Further, the ring(s) or ring system(s) comprise carbon atoms such as, but not limited to, those cyclopentadienyl ligands or cyclopentadienyl-type ligand structures or other similar functioning ligand structures such as a pentadiene, a cyclooctatetraendiyl, or an imide ligand. The metal atom can be selected from Groups 3 through 15 and the lanthanide or actinide series of the Periodic Table of Elements. The metal is a transition metal from Groups 4 through 12, Groups 4, 5 and 6, and the transition metal is from Group 4.

[0094] Exemplary metallocene catalysts and catalyst systems are described in, for example, U.S. Patent Nos. 4,530,914, 4,871,705, 4,937,299, 5,017,714, 5,055,438, 5,096,867, 5,120,867, 5,124,418, 5,198,401, 5,210,352, 5,229,478, 5,264,405, 5,278,264, 5,278,119, 5,304,614, 5,324,800, 5,347,025, 5,350,723, 5,384,299, 5,391,790, 5,391,789, 5,399,636, 5,408,017, 5,491,207, 5,455,366, 5,534,473, 5,539,124, 5,554,775, 5,621,126, 5,684,098, 5,693,730, 5,698,634, 5,710,297, 5,712,354, 5,714,427, 5,714,555, 5,728,641, 5,728,839, 5,753,577, 5,767,209, 5,770,753, 5,770,664; EP-A-0 591 756, EP-A-0 520-732, EP-A-0 420 436, EP-B1 0 485 822, EP-B1 0 485 823, EP-A2-0 743 324, EP-B1 0 518 092; WO 91 / 04257, WO 92 / 00333, WO 93 / 08221, WO 93 / 08199, WO 94 / 01471, WO 96 / 20233, WO 97 / 15582, WO 97 / 19959, WO 97 / 46567, WO 98 / 01455, WO 98 / 06759, and WO 98 / 011144.Polymerization Processes

[0095] The catalysts described above are suitable for use in any olefin pre-polymerization or polymerization process or both. Suitable polymerization processes include solution, gas phase, slurry phase, and a high-pressure process, or any combination thereof. A desirable process is a gas phase polymerization of one or more olefin monomers having from 2 to 30 carbon atoms, from 2 to 12 carbon atoms in an aspect, and from 2 to 8 carbon atoms in an aspect. Other monomers useful in the process include ethylenically unsaturated monomers, diolefins having 4 to 18 carbon atoms, conjugated or nonconjugated dienes, polyenes, vinyl monomers and cyclic olefins. Non-limiting monomers may also include norbornene, norbornadiene, isobutylene, isoprene, vinylbenzocyclobutane, styrenes, alkyl substituted styrene, ethylidene norbornene, dicyclopentadiene and cyclopentene.

[0096] In an aspect, a copolymer of ethylene derived units and one or more monomers or comonomers is produced. The one or more comonomers are an α-olefin having from 4 to 15 carbon atoms in an aspect, from 4 to 12 carbon atoms in an aspect, and from 4 to 8 carbon atoms in an aspect. The comonomer can be 1-hexene.

[0097] Hydrogen gas is often used in olefin polymerization to control the final properties of the polyolefin, such as described in Polypropylene Handbook 76-78 (Hanser Publishers, 1996). Increasing concentrations (partial pressures) of hydrogen increase the melt flow rate (MFR) and / or MI of the polyolefin generated. The MFR or MI can thus be influenced by the hydrogen concentration. The amount of hydrogen in the polymerization can be expressed as a mole ratio relative to the total polymerizable monomer, for example, ethylene, or a blend of ethylene and hexane or propene. The amount of hydrogen used in the polymerization process is an amount necessary to achieve the desired MFR or MI of the final polyolefin composition. The mole ratio of hydrogen to total monomer (H 2 :monomer) is in a range of from greater than 0.0001 in an aspect, from greater than 0.0005 in an aspect, from greater than 0.001 in an aspect, to less than 10 in an aspect, less than 5 in an aspect, less than 3 in an aspect, and less than 0.10 in an aspect, wherein a desirable range may comprise any combination of any upper mole ratio limit with any lower mole ratio limit described herein. Expressed another way, the amount of hydrogen in the reactor at any time may range to up to 5000 ppm, up to 4000 ppm in an aspect, up to 3000 ppm in an aspect, between 50 ppm and 5000 ppm in an aspect, and between 100 ppm and 2000 ppm in an aspect.

[0098] In a gas phase polymerization process, a continuous cycle is often employed where one part of the cycle of a reactor system, a cycling gas stream, otherwise known as a recycle stream or fluidizing medium, is heated in the reactor by the heat of polymerization. This heat is removed from the recycle composition in another part of the cycle by a cooling system external to the reactor. Generally, in a gas fluidized bed process for producing polymers, a gaseous stream containing one or more monomers is continuously cycled through a fluidized bed in the presence of a catalyst under reactive conditions. The gaseous stream is withdrawn from the fluidized bed and recycled back into the reactor. Simultaneously, polymer product is withdrawn from the reactor and fresh monomer is added to replace the polymerized monomer.

[0099] The ethylene partial pressure can vary between 80 and 300 psia, or between 100 and 280 psia, or between 120 and 260 psia, or between 140 and 240 psia. More importantly, a ratio of comonomer to ethylene in the gas phase can vary from 0.0 to 0.10, or between 0.005 and 0.05, or between 0.007 and 0.030, or between 0.01 and 0.02.

[0100] Reactor pressure typically varies from 100 psig (690 kPa) to 500 psig (3448 kPa). In an aspect, the reactor pressure is maintained within the range of from 200 psig (1379 kPa) to 500 psig (3448 kPa). In an aspect, the reactor pressure is maintained within the range of from 250 psig (1724 kPa) to 400 psig (2759 kPa).Production of Blown Film

[0101] Blown film extrusion involves the process of extruding the polyethylene blend (also referred to sometimes as a resin) through a die (not shown) followed by a bubble-like expansion. Advantages of manufacturing film in this manner include: (1) a single operation to produce tubing; (2) regulation of film width and thickness by control of the volume of air in the bubble; (3) high extruder output and haul-off speed; (4) elimination of end effects such as edge bead trim and nonuniform temperature that can result from flat die film extrusion; and (5) capability of biaxial orientation (allowing uniformity of mechanical properties).

[0102] As part of the process, a melt comprising the polyethylene blend is mixed with a foaming agent and extruded through an annular slit die (not shown) to form a thin walled tube. Air is introduced via a hole in the center of the die to blow up the tube like a balloon. Mounted on top of the die, a high-speed air ring (not shown) blows onto the hot film to cool it. The foam film is drawn in an upward direction, continually cooling, until it passes through nip rolls (not shown) where the tube is flattened to create what is known as a 'lay-flat' tube of film. This lay-flat or collapsed tube is then taken back down the extrusion tower (not shown) via more rollers. For high output lines, air inside the bubble may also be exchanged. The lay-flat film is either wound or the edges of the film are slit off to produce two flat film sheets and wound up onto reels to produce a tube of film. For lay-flat film, the tube can be made into bags, for example, by sealing across the width of film and cutting or perforating to make each bag. This operation can be performed either in line with the blown film process or at a later time. The blown film extrusion process is typically a continuous process.

[0103] It is to be understood that while the invention has been described in conjunction with the specific embodiments thereof, the foregoing description is intended to illustrate and not limit the scope of the invention. Other aspects, advantages, and modifications will be apparent to those skilled in the art to which the invention pertains.

[0104] In the following examples, films made from secondary polyethylene blends 4CB-15 and 9CB-12345 are according to the claimed invention while all other films are not according to the invention as claimed.EXAMPLE I

[0105] In this example, secondary polyethylene blends were produced by blending two primary polyethylene blends. The primary polyethylene blends were produced by blending two polyethylene compositions. Each primary polyethylene blend comprises one polyethylene composition with lower density and one polyethylene composition with higher density, blended in amounts so that each primary polyethylene blend has a density of approximately 0.920 g / cm 3< . Thus, the secondary polyethylene blends also have densities of approximately 0.920 g / cm 3< . Additionally, each primary polyethylene blend has an MI (I 2 ) of about 1.0 g / 10 min.

[0106] FIG. 1 shows thirteen reactor grades used as blending components (referred to herein as polyethylene compositions) or as a control (reference polyethylene composition). For example, D3 is a control or reference polyethylene composition having a density of 0.9216 g / cm 3< and an MI of 1.08 g / 10 min.

[0107] Tables 1A through 1E provide the characterization of NMWD / NCD components (polyethylene compositions) and the control. Tables 2E through 2E teaches the primary polyethylene blend compositions and characterization. Tables 3A through 3D provide the secondary polyethylene blends formulations. Specifically, Tables 3A through 3D describe the secondary polyethylene blends by wt% of the primary blends. Tables 3E through 3H describe the secondary polyethylene blends by MI and density (DN) of the original components.

[0108] Tables 4A through 4D provide the secondary polyethylene blend characterization on film sample. Note that all of the secondary polyethylene blends in this study exhibits characteristics of broad CD, i.e., T75-T25 greater than 24 (or greater than 30 for those with outstanding stiffness and sealing. Table 1ACharacterization of NMWD / NCD Components and Control in Blend DOEComponentsF1E2Design TargetsComponents for BOCDCatalystOMC-1716OMC-1716MI(dg / min)0.280.48HLMI(dg / min)4.567.74MIR(I 21 / I 2 )16.316.1Density(g / cm 3< )0.89610.9082H-NMR File #hctl201609040412hctl201609040410Vinylene( / 1000C)0.020.01TSO( / 1000C)0.030.02Vinylene( / 1000C)0.010.01Vinylidene( / 1000C)0.010.01Total Unsat( / 1000C)0.070.05methyl w / o CE Correction( / 1000C)29.019.8GPC-4D File #116-2655116-2491Mn GPC4D(g / mol)67,41452,319Mw GPC4D(g / mol)166,205140,928Mz GPC4D(g / mol)283,446245,047Mz+1 GPC4D(g / mol)426,847367,377Mw / Mn GPC4D2.472.69Mz / Mw GPC4D1.711.74Bulk C6(wt %)17.3311.85g'(Vis Ave.)1.001.01Recover(%)103%104%Cryo-TREFIR5 Run #16-112516-1123Mass Recovery(%)95.7498.73SF Weight Fraction(%)0.580.42Tw(°C)58.5870.42Tn(°C)54.1349.73T75-T25(°C)910Pk1 - Tmp(°C)59.072.1Pk1 - Area(%)99.499.6Pk2 - Tmp(°C)Pk2 - Area(%)CFC File #221-16CFC220-16CFC1 st< Half from CFC(%)46.8%51.6%2 nd< Half from CFC(%)53.2%48.4%Mw1198,454189,889Mw-1+2208,746187,274Mw2217,885184,501Tw1(°C)50.463.3Tw1+2(°C)57.470.5Tw2(°C)63.678.1(log(Mw1 / Mw2)) / (Tw1-Tw2)0.0031-0.0008Mw1 / Mw20.911.03Tw1 - Tw2(°C)-13.2-14.8 Table 1B Characterization of NMWD / NCD Components and Control in Blend DOEComponentsC4B5Design TargetsComponents for BOCDCatalystEXP 1201OMC-1716MI(dg / min)3.014.2HLMI(dg / min)51241MIR(I 21 / I 2 )17.017.0Density(g / cm 3< )0.93890.9510H-NMR File #hctl20160904044hctl20160904042Vinylene( / 1000C)0.070.01TSO( / 1000C)0.080.01Vinylene( / 1000C)0.010.01Vinylidene( / 1000C)0.010.00Total Unsat( / 1000C)0.170.03methyl w / o CE Correction( / 1000C)4.43.4GPC-4D File #116-2485116-2651Mn GPC4D(g / mol)31,20817,408Mw GPC4D(g / mol)86,94455,977Mz GPC4D(g / mol)168,938105,252Mz+1 GPC4D(g / mol)289,573164,332Mw / Mn GPC4D2.793.22Mz / Mw GPC4D1.941.88Bulk C6(wt %)2.531.48g'(Vis Ave.)1.001.03Recover(%)100%100%Cryo-TREFIR5 Run #16-111716-1115Mass Recovery(%)101.3399.57SF Weight Fraction(%)0.260.39Tw(°C)91.3992.44Tn(°C)86.5688.85T75-T25(°C)22Pk1 - Tmp(°C)93.394.7Pk1 - Area(%)99.799.6Pk2 - Tmp(°C)Pk2 - Area(%)CFC File #238-16CFC231-16CFC1 st< Half from CFC(%)44.8%44.8%2 nd< Half from CFC(%)55.2%55.2%Mw1115,42860,391Mw-1+2116,08774,146Mw2116,59984,872Tw1(°C)91.493.4Tw1+2(°C)93.895.8Tw2(°C)95.797.7(log(Mwl / Mw2)) / (Twl-Tw2)0.00100.0346Mw1 / Mw20.990.71Tw1 - Tw2(°C)-4.3-4.3 Table 1C Characterization of NMWD / NCD Components and Control in Blend DOEComponentsB1C2Design TargetsComponents for Conventional CDCatalystOMC-1716OMC-1716MI(dg / min)7.83.1HLMI(dg / min)13549MIR(I 21 / I 2 )17.316.0Density(g / cm 3< )0.89830.9078H-NMR File #hctl20160904041hctl20160904043Vinylene( / 1000C)0.020.07TSO( / 1000C)0.040.14Vinylene( / 1000C)0.000.03Vinylidene( / 1000C)0.000.00Total Unsat( / 1000C)0.060.24methyl w / o CE Correction( / 1000C)31.522.7GPC-4D File #116-2482116-2484Mn GPC4D(g / mol)27,95632,985Mw GPC4D(g / mol)67,90585,606Mz GPC4D(g / mol)112,947146,301Mz+1 GPC4D(g / mol)166,117217,119Mw / Mn GPC4D2.432.60Mz / Mw GPC4D1.661.71Bulk C6(wt %)19.313.46g'(Vis Ave.)0.981.01Recover(%)104%100%Cryo-TREFIR5 Run #16-111416-1116Mass Recovery(%)95.9698.91SF Weight Fraction(%)1.520.65Tw(°C)51.9564.85Tn(°C)47.4160.04T75-T25(°C)1312Pk1 - Tmp(°C)54.167.6Pk1 - Area(%)98.599.4Pk2 - Tmp(°C)Pk2 - Area(%)CFC File #215-16CFC216-16CFC1 st< Half from CFC(%)53.1%48.3%2 nd< Half from CFC(%)46.9%51.7%Mw169,10993,584Mw-1+277,30899,707Mw286,796105,294Tw1(°C)42.056.6Tw1+2(°C)50.365.3Tw2(°C)60.073.2(log(Mw1 / Mw2)) / (Tw1-Tw2)0.00550.0031Mw1 / Mw20.800.89Tw1 - Tw2(°C)-18.1-16.5 Table 1D Characterization of NMWD / NCD Components and Control in Blend DOEComponentsE4F5Design TargetsComponents for Conventional CDCatalystEXP 1201EXP 1201MI(dg / min)0.440.20HLMI(dg / min)7.333.67MIR(I 21 / I 2 )16.718.4Density(g / cm 3< )0.93690.9516H-NMR File #hctl201609040411hctl20160904013Vinylene( / 1000C)0.110.06TSO( / 1000C)0.060.01Vinylene( / 1000C)0.000.00Vinylidene( / 1000C)0.010.00Total Unsat( / 1000C)0.180.07methyl w / o CE Correction( / 1000C)2.70.9GPC-4D File #116-2492116-2656Mn GPC4D(g / mol)55,89756,697Mw GPC4D(g / mol)149,248188,670Mz GPC4D(g / mol)294,490426,898Mz+1 GPC4D(g / mol)542,631920,720Mw / Mn GPC4D2.673.33Mz / Mw GPC4D1.972.26Bulk C6(wt %)1.610.37g'(Vis Ave.)1.031.02Recover(%)99%101%Cryo-TREFIR5 Run #16-112416-1126Mass Recovery(%)98.76102.88SF Weight Fraction(%)0.30.42Tw(°C)93.9696.79Tn(°C)85.1985.8T75-T25(°C)11Pk1 - Tmp(°C)94.797.8Pk1 - Area(%)99.799.6Pk2 - Tmp(°C)Pk2 - Area(%)CFC File #236-16CFC237-16CFC1 st< Half from CFC(%)40.2%65.2%2 nd< Half from CFC(%)59.8%34.8%Mw1175,342286,156Mw-1+2196,580267,874Mw2209,475235,794Tw1(°C)78.5103.8Tw1+2(°C)89.9103.0Tw2(°C)96.8101.7(log(Mw1 / Mw2)) / (Tw1-Tw2)0.00420.0401Mw1 / Mw20.841.21Tw1 - Tw2(°C)-18.42.1 Table 1E Characterization of NMWD / NCD Components and Control in Blend DOEComponentsDEExceed 1018Design TargetsNMWD / NCD as ControlCatalystOMC-1716CommercialMI(dg / min)1.080.99HLMI(dg / min)17.415.1MIR(I 21 / I 2 )16.115.2Density(g / cm 3< )0.92160.9187H-NMR File #hctl20160904047Vinylene( / 1000C)0.010.01TSO( / 1000C)0.020.05Vinylene( / 1000C)0.010.06Vinylidene( / 1000C)0.010.02Total Unsat( / 1000C)0.050.13methyl w / o CE Correction( / 1000C)10.411.7GPC-4D File #116-248817-1057Mn GPC4D(g / mol)39,57242,694Mw GPC4D(g / mol)113,015115,629Mz GPC4D(g / mol)200,955207,754Mz+1 GPC4D(g / mol)304,113321,990Mw / Mn GPC4D2.862.71Mz / Mw GPC4D1.781.80Bulk C6(wt %)5.976.3g'(Vis Ave.)0.99Recover(%)101%101%Cryo-TREFIR5 Run #16-112018-0093Mass Recovery(%)100.698.39SF Weight Fraction(%)0.260.23Tw(°C)82.8881.98Tn(°C)67.379.96T75-T25(°C)710Pk1 - Tmp(°C)87.883.6Pk1 - Area(%)99.799.8Pk2 - Tmp(°C)Pk2 - Area(%)CFC File #239-16CFC150-17CFC1 st< Half from CFC(%)47.2%49.4%2 nd< Half from CFC(%)52.8%50.6%Mw1155,572165,078Mw-1+2154,407156,788Mw2153,391148,679Tw1(°C)79.675.5Tw1+2(°C)84.682.0Tw2(°C)89.088.3(log(Mw1 / Mw2)) / (Tw1-Tw2)-0.0007-0.0036Mw1 / Mw21.011.11Tw1 - Tw2(°C)-9.4-12.8 Table 2A Primary Blend Composition and CharacterizationBOCD BlendsF1B5E2B5BCT-206552BCT-206553Blend Composition56% F171% E244% B529% B5MI(dg / min)0.930.96HLMI(dg / min)22.318.2MIR(I 21 / I 2 )24.019.0Density(g / cm 3< )0.9190.918 H-NMR File #hctl201607225713hctl201607225714Vinylene( / 1000C)0.010.01TSO( / 1000C)0.020.01Vinylene( / 1000C)0.000.00Vinylidene( / 1000C)0.000.00Total Unsat( / 1000C)0.030.02methyl w / o CE Correction( / 1000C)18.115.2 GPC-4D Run #16-246816-2469Mn GPC4D(g / mol)30,37033,398Mw GPC4D(g / mol)118,267115,936Mz GPC4D(g / mol)242,682223,565Mz+1 GPC4D(g / mol)385,413348,192Mw / Mn GPC4D3.893.47Mz / Mw GPC4D2.051.93Bulk C6(wt %)10.538.52g'(Vis Ave.)0.9450.989Recover(%)100%100% Cryo-TREFIR5 Run #16-101916-1020SF Weight Fraction(%)0.620.43Tw(°C)73.276.94Tn(°C)64.3671.22T75-T25(°C)3724Pk1 - Tmp(°C)59.071.8Pk1 - Area(%)57.866.9Pk2 - Tmp(°C)94.393.9Pk2 - Area (LD component)(%)41.532.7 CFC File #202-16CFC204-16CFC1 st< Half from CFC(%)56.7%74.0%2 nd< Half from CFC(%)43.3%26.0%Mw1215,714174,915Mw-1+2156,719151,915Mw280,41587,233Tw1(°C)57.670.6Tw1+2(°C)73.577.2Tw2(°C)94.095.6(log(Mw1 / Mw2)) / (Tw1-Tw2)-0.0118-0.0121Mw1 / Mw22.682.01Tw1 - Tw2(°C)-36.4-24.9 Table 2B Primary Blend Composition and CharacterizationBOCD BlendsF1C4E2C4BCT-206554BCT-206555Blend Composition40% F157% E260% C443% C4MI(dg / min)0.960.96HLMI(dg / min)18.716.6MIR(I 21 / I 2 )19.417.3Density(g / cm 3< )0.9200.920 H-NMR File #hctl201607225715hctl201607225716Vinylene( / 1000C)0.050.03TSO( / 1000C)0.060.04Vinylene( / 1000C)0.010.00Vinylidene( / 1000C)0.010.01Total Unsat( / 1000C)0.130.08methyl w / o CE Correction( / 1000C)14.513.4 GPC-4D Run #16-252316-2471Mn GPC4D(g / mol)39,78940,654Mw GPC4D(g / mol)118,092118,003Mz GPC4D(g / mol)229,354221,081Mz+1 GPC4D(g / mol)373,726352,137Mw / Mn GPC4D2.972.90Mz / Mw GPC4D1.941.87Bulk C6(wt %)7.967.76g'(Vis Ave.)0.9801.004Recover(%)100%101% Cryo-TREFIR5 Run #16-102116-1022SF Weight Fraction(%)0.450.49Tw(°C)78.7379.76Tn(°C)70.3143.62T75-T25(°C)3323Pk1 - Tmp(°C)59.071.6Pk1 - Area(%)37.350.8Pk2 - Tmp(°C)93.192.9Pk2 - Area (LD component)(%)62.348.7 CFC File #203-16CFC205-16CFC1 st< Half from CFC(%)40.0%58.8%2 nd< Half from CFC(%)60.0%41.2%Mw1208,027169,953Mw-1+2153,601144,945Mw2117,892109,577Tw1(°C)57.971.0Tw1+2(°C)79.180.3Tw2(°C)93.193.5(log(Mw1 / Mw2)) / (Twl-Tw2)-0.0070-0.0085Mw1 / Mw21.761.55Tw1 - Tw2(°C)-35.2-22.5 Table 2C Primary Blend Composition and CharacterizationConventional CD BlendsB1F5C2F5BCT-206556BCT-206558Blend Composition57% B170% C243% F530% F5MI(dg / min)1.031.09HLMI(dg / min)23.120.6MIR(I 21 / I 2 )22.418.9Density(g / cm 3< )0.9200.919 H-NMR File #hctl201607225717hctl201607225719Vinylene( / 1000C)0.030.02TSO( / 1000C)0.000.02Vinylene( / 1000C)0.010.00Vinylidene( / 1000C)0.000.01Total Unsat( / 1000C)0.040.05methyl w / o CE Correction( / 1000C)19.316.7 GPC-4D Run #16-254916-2474Mn GPC4D(g / mol)34,43937,636Mw GPC4D(g / mol)124,443118,448Mz GPC4D(g / mol)344,355292,905Mz+1 GPC4D(g / mol)781,081671,307Mw / Mn GPC4D3.613.15Mz / Mw GPC4D2.772.47Bulk C6(wt %)10.879.46g'(Vis Ave.)1.0271.012Recover(%)99%100% Cryo-TREFIR5 Run #16-104416-1046SF Weight Fraction(%)0.860.35Tw(°C)72.6775.4Tn(°C)62.1468.78T75-T25(°C)4634Pk1 - Tmp(°C)54.267.2Pk1 - Area(%)53.464.2Pk2 - Tmp(°C)97.496.9Pk2 - Area (LD component)(%)45.835.4 CFC File #201-16CFC207-16CFC1 st< Half from CFC(%)55.3%68.4%2 nd< Half from CFC(%)44.7%31.6%Mw182,070104,587Mw-1+2174,440165,860Mw2292,715305,085Tw1(°C)50.363.7Tw1+2(°C)72.174.8Tw2(°C)100.1100.0(log(Mw1 / Mw2)) / (Tw1-Tw2)0.01110.0128Mw1 / Mw20.280.34Tw1 - Tw2(°C)-49.8-36.3 Table 2D Primary Blend Composition and CharacterizationConventional CD BlendsB1E4C2E4BCT-206557BCT206559Blend Composition39% B153% C261% E447% E4MI(dg / min)1.041.09HLMI(dg / min)19.218.4MIR(I 21 / I 2 )18.416.9Density(g / cm 3< )0.9220.921 H-NMR File #hctl201607225718hctl201607225920Vinylene( / 1000C)0.070.06TSO( / 1000C)0.050.04Vinylene( / 1000C)0.010.00Vinylidene( / 1000C)0.010.00Total Unsat( / 1000C)0.140.10methyl w / o CE Correction( / 1000C)14.414.2 GPC-4D Run #16-247316-2475Mn GPC4D(g / mol)39,19339,901Mw GPC4D(g / mol)120,501116,164Mz GPC4D(g / mol)226,245240,887Mz+1 GPC4D(g / mol)525,790455,451Mw / Mn GPC4D3.072.91Mz / Mw GPC4D1.882.07Bulk C6(wt %)8.298.02g'(Vis Ave.)1.0331.040Recover(%)101%101% Cryo-TREFIR5 Run #16-104516-1047SF Weight Fraction(%)0.470.37Tw(°C)78.0278.65Tn(°C)68.6972.35T75-T25(°C)3930Pk1 - Tmp(°C)54.767.3Pk1 - Area(%)38.049.7Pk2 - Tmp(°C)94.494.4Pk2 - Area (LD component)(%)61.649.9 CFC File #206-16CFC208-16CFC1 st< Half from CFC(%)38.8%53.2%2 nd< Half from CFC(%)61.2%46.8%Mw177,06098,864Mw-1+2160,795147,613Mw2214,922202,198Tw1(°C)53.765.1Tw1+2(°C)80.879.6Tw2(°C)98.495.9(log(Mw1 / Mw2)) / (Tw1-Tw2)0.01000.0101Mw1 / Mw20.360.49Tw1 - Tw2(°C)-44.7-30.9 Table 2E Primary Blend Composition and CharacterizationNMWD / NCD ControlsD3Exceed 1018BCT-206293BCT-236471Blend Composition100% D3100% Exceed 1018MI(dg / min)1.08.99HLMI(dg / min)16.815.1MIR(I 21 / I 2 )15.615.2Density(g / cm 3< )0.9200.919 H-NMR File #hctl201607225725Vinylene( / 1000C)0.010.01TSO( / 1000C)0.020.05Vinylene( / 1000C)0.010.06Vinylidene( / 1000C)0.010.02Total Unsat( / 1000C)0.050.13methyl w / o CE Correction( / 1000C)10.511.7 GPC-4D Run #16-248017-1057Mn GPC4D(g / mol)38,82642,694Mw GPC4D(g / mol)112,293115,629Mz GPC4D(g / mol)199,594207,754Mz+1 GPC4D(g / mol)301,719321,990Mw / Mn GPC4D2.892.71Mz / Mw GPC4D1.781.80Bulk C6(wt %)6.176.30g'(Vis Ave.)1.022-Recover(%)101%101% Cryo-TREFIR5 Run #16-104818-0093SF Weight Fraction(%)0.360.23Tw(°C)82.3581.98Tn(°C)73.379.96T75-T25(°C)710Pk1 - Tmp(°C)87.883.6Pk1 - Area(%)99.699.8Pk2 - Tmp(°C)--Pk2 - Area (LD component)(%)-- CFC File #211-16CFC150-16CFC1 st< Half from CFC(%)48.3%49.4%2 nd< Half from CFC(%)51.7%50.6%Mw1152,348165,078Mw-1+2152,806156,788Mw2153,228148,679Tw1(°C)77.875.5Tw1+2(°C)83.282.0Tw2(°C)88.188.3(log(Mw1 / Mw2)) / (Tw1-Tw2)0.0002-0.0036Mw1 / Mw20.991.11Tw1 - Tw2(°C)-10.3-12.8 Table 3A Secondary Blend FormulationPrimary BlendsSecondary BlendCompositionwt%-1wt%-24CB-154CB-24F1B556%44%50.0%E2B571%29%F1C440%60%E2C457%43%50%Exceed 1018100%B1F557%43%50.0%B1E439%61%C2F570%30%C2E453%47%50.0% Table 3B Secondary Blend FormulationPrimary BlendsSecondary BlendCompositionwt%-1wt%-24CB-144CB-25F1B556%44%E2B571%29%50.0%F1C440%60%50.0%E2C457%43%Exceed 1018100%B1F557%43%B1E439%61%50.0%C2F570%30%50.0%C2E453%47% Table 3C Secondary Blend FormulationPrimary BlendsSecondary BlendCompositionwt%-1wt%-25CB-1355CB-234F1B556%44%40.0%E2B571%29%F1C440%60%E2C457%43%40.0%Exceed 1018100%20.0%20.0%B1F557%43%40.0%B1E439%61%C2F570%30%C2E453%47%40.0% Table 3D Secondary Blend FormulationPrimary BlendsSecondary Blend Compositionwt%-1wt%-29CB-12345F1B556%44%22.0%E2B571%29%F1C440%60%E2C457%43%22.0%Exceed 1018100%12.0%B1F557%43%22.0%B1E439%61%C2F570%30%C2E453%47%22.0% Table 3E Secondary Blend FormulationOriginal ComponentsSecondary BlendCompositionMIDN4CB-154CB-24F10.280.89628.0%B17.830.89828.5%E20.480.90828.5%C23.070.90826.5%Exceed 10181.000.919E40.440.93723.5%C43.000.93921.5%F50.200.95221.5%B514.190.95122.0% Table 3F Secondary Blend FormulationOriginal ComponentsSecondary BlendCompositionMIDN4CB-144CB-25F10.280.89620.0%B17.830.89819.5%E20.480.90835.5%C23.070.90835.0%Exceed 10181.000.919E40.440.93730.5%C43.000.93930.0%F50.200.95215.0%B514.190.95114.5% Table 3G Secondary Blend FormulationOriginal ComponentsSecondary BlendCompositionMIDN5CB-1355CB-234F10.280.89622.4%B17.830.89822.8%E20.480.90822.8%C23.070.90821.2%Exceed 10181.000.91920.0%20.0%E40.440.93718.8%C43.000.93917.2%F50.200.95217.2%B514.190.95117.6% Table 3H Secondary Blend FormulationOriginal ComponentsSecondary BlendMIDN9CB-1234F10.280.89612.3%B17.830.89812.5%E20.480.90812.5%C23.070.90811.7%Exceed 10181.000.91912.0%E40.440.93710.3%C43.000.9399.5%F50.200.9529.5%B514.190.9519.7% Table 4A Secondary Blend Characterization on Film Sample4CB-154CB-24H-NMR File #201711034381201711034382vinylene( / 1000C)0.120.05TSO( / 1000C)0.270.02vinylene( / 1000C)0.040.00vinylidene( / 1000C)0.000.00Total Unsat( / 1000C)0.430.07methyl w / o CE Correction( / 1000C)18.713.5GPC-4D Run #18-074818-0749Mn GPC4D(g / mol)33,62141,096Mw GPC4D(g / mol)118,029113,145Mz GPC4D(g / mol)316,691228,752Mz+1 GPC4D(g / mol)955,888414,216Mw / Mn GPC4D3.512.75Mz / Mw GPC4D2.682.02Bulk C6(wt %)10.317.46g'(Vis Ave.)1.0091.014Recover(%)104%102%Cryo-TREFIR5 Run ID18-032118-0322Mass Recovery101.05102.15SF Weight Fraction(%)0.380.27Tw(°C)74.3479.75Tn(°C)66.7573.69T75-T25(°C)40.426.6Pk1 - Tmp(°C)57.969.9Pk1 - Area (LD component)(%)56.151.5Pk2 - Tmp(°C)96.394.1Pk2 - Area (HD component)(%)43.648.3Pk3 -TmpPk3 - Area (additional)CFC File #35-18CFC.rdf36-18CFC.rdf1 st< Half from CFC(%)50.5%49.2%2 nd< Half from CFC(%)49.5%50.8%Mw1152,088140,538Mw-1+2164,823146,548Mw2177,562152,309Tw1(°C)52.665.9Tw1+2(°C)74.079.8Tw2(°C)95.493.1(log(Mw1 / Mw2)) / (Tw1-Tw2)0.00160.0013Mw1 / Mw20.860.92Tw1 - Tw2(°C)-42.8-27.2 Table 4B Secondary Blend Characterization on Film Sample4CB-144CB-25H-NMR File #201711034383201711034384vinylene( / 1000C)0.260.10TSO( / 1000C)0.140.05vinylene( / 1000C)0.000.00vinylidene( / 1000C)0.000.00Total Unsat( / 1000C)0.400.15methyl w / o CE Correction( / 1000C)15.116.1 GPC-4D Run #18-075018-0751Mn GPC4D(g / mol)40,24336,384Mw GPC4D(g / mol)114,379113,168Mz GPC4D(g / mol)243,631257,290Mz+1 GPC4D(g / mol)456,888546,285Mw / Mn GPC4D2.843.11Mz / Mw GPC4D2.132.27Bulk C6(wt %)7.888.79g'(Vis Ave.)1.0161.013Recover(%)101%102% Cryo-TREFIR5 Run ID18-032318-0324Mass Recovery102.13101.47SF Weight Fraction(%)0.280.22Tw(°C)79.3276.87Tn(°C)71.1972.23T75-T25(°C)35.130.0Pk1 - Tmp(°C)58.070.2Pk1 - Area (LD component)(%)39.866.6Pk2 - Tmp(°C)94.296.0Pk2 - Area (HD component)(%)60.033.2Pk3 -TmpPk3 - Area (additional) CFC File #37-18CFC.rdf38-18CFC.rdf1 st< Half from CFC(%)50.1%50.2%2 nd< Half from CFC(%)49.9%49.8%Mw1138,665140,660Mw-1+2157,716149,808Mw2176,429158,859Tw1(°C)63.463.3Tw1+2(°C)79.876.8Tw2(°C)95.890.2(log(Mw1 / Mw2)) / (Tw1-Tw2)0.00320.0020Mw1 / Mw20.790.89Tw1 - Tw2(°C)-32.4-26.9 Table 4C Secondary Blend Characterization on Film Sample5CB-1355CB-234H-NMR File #201711034385201711034386Vinylene( / 1000C)0.070.09TSO( / 1000C)0.040.05Vinylene( / 1000C)0.010.01Vinylidene( / 1000C)0.000.00Total Unsat( / 1000C)0.120.15methyl w / o CE Correction( / 1000C)18.613.2 GPC-4D Run #18-075218-0753Mn GPC4D(g / mol)35,36841,608Mw GPC4D(g / mol)117,224112,134Mz GPC4D(g / mol)278,602221,738Mz+1 GPC4D(g / mol)608,732396,620Mw / Mn GPC4D3.312.70Mz / Mw GPC4D2.381.98Bulk C6(wt %)9.487.18g'(Vis Ave.)1.0091.021Recover(%)102%102% Cryo-TREFIR5 Run ID18-032518-0327Mass Recovery102.29101.63SF Weight Fraction(%)0.260.16Tw(°C)76.180.31Tn(°C)67.4772.4T75-T25(°C)38.424.5Pk1 - Tmp(°C)57.570.1Pk1 - Area (LD component)(%)43.752.9Pk2 - Tmp(°C)79.293.9Pk2 - Area (HD component)(%)13.647.0Pk3 -Tmp95.9Pk3 - Area (additional)42.5 CFC File #40-18CFC.rdf41-18CFC.rdf1 st< Half from CFC(%)50.3%49.0%2 nd< Half from CFC(%)49.7%51.0%Mw1151,291147,777Mw-1+2166,949153,678Mw2182,454159,257Tw1(°C)56.968.4Tw1+2(°C)75.980.6Tw2(°C)94.692.2(log(Mw1 / Mw2)) / (Tw1-Tw2)0.00220.0014Mw1 / Mw20.830.93Tw1 - Tw2(°C)-37.7-23.8 Table 4D Secondary Blend Characterization on Film Sample9CB-12345Exceed1018H-NMR File #201711034387201711034388Vinylene( / 1000C)0.040.17TSO( / 1000C)0.020.12Vinylene( / 1000C)0.010.04Vinylidene( / 1000C)0.000.00Total Unsat( / 1000C)0.070.33methyl w / o CE Correction( / 1000C)15.411.6 GPC-4D Run #18-075418-0755Mn GPC4D(g / mol)37,33242,465Mw GPC4D(g / mol)114,966109,263Mz GPC4D(g / mol)255,878195,604Mz+1 GPC4D(g / mol)556,170306,038Mw / Mn GPC4D3.082.57Mz / Mw GPC4D2.231.79Bulk C6(wt %)8.456.31g'(Vis Ave.)1.0101.015Recover(%)103%102% Cryo-TREFIR5 Run ID18-032818-0329Mass Recovery101.92102.53SF Weight Fraction(%)0.240.14Tw(°C)77.9481.93Tn(°C)64.4867.61T75-T25(°C)32.19.7Pk1 - Tmp(°C)60.883.8Pk1 - Area (LD component)(%)54.999.9Pk2 - Tmp(°C)95.0Pk2 - Area (HD component)(%)44.8Pk3 -TmpPk3 - Area (additional) CFC File #42-18CFC.rdf43-18CFC.rdf1 st< Half from CFC(%)48.9%51.4%2 nd< Half from CFC(%)51.1%48.6%Mw1154,653153,250Mw-1+2163,278143,882Mw2171,407134,158Tw1(°C)61.477.3Tw1+2(°C)77.982.5Tw2(°C)93.687.9(log(Mw1 / Mw2)) / (Tw1-Tw2)0.0014-0.0054Mw1 / Mw20.901.14Tw1 - Tw2(°C)-32.2-10.6

[0109] The various polyethylene compositions in Tables 1A through 1G were lettered and numbered according to their approximate densities and MIs. Numbers increased as density increased, while lettering progressed as MI decreased. For example, B1, D1, and F1 all have densities below 0.900 g / cm 3< , while B5, D5, and F5 all have densities greater than 0.950 g / cm 3< . As a further example, B1 and B5 both have MIs greater than 7.0 g / 10 min, while F1 and F5 both have MIs less than 0.30 g / 10 min.

[0110] The primary polyethylene blends described in Tables 2A through 2E were made by blending one low-density polyethylene composition with one high-density polyethylene composition in an amount such that the primary polyethylene blend has a density of approximately 0.920 g / cm 3< . D3 and Exceed 1018 are included as comparative references.

[0111] The secondary polyethylene blends shown in Tables 3A through 3H and Tables 4A through 4D were made by blending two primary polyethylene compositions. Some secondary polyethylene blends also include yet another polyethylene blend, Exceed 1018. Tables 3A through 3H show the compositions of the secondary polyethylene blends as percentages of the primary polyethylene blends and as percentages of the polyethylene compositions. Tables 3A through 3H also list the densities and MIs of the polyethylene compositions, as well as the polyethylene compositions (by wt%) of the primary polyethylene blends. Tables 4A through 4D provide additional detailed properties of the secondary polyethylene blends.

[0112] Tables 5A through 5D and 6A through 6D provide processing data for the extrusion process used to create blown films from the primary polyethylene blends and secondary polyethylene blends. All the blown films were extruded with a screw speed of 30 rpm, a blow-up ratio of 2.5, a die gap of 60 mil, and a film thickness of 1.0 mil. Table 5APrimary Blends Film Blowing Data at 25.4 µm (1.0 mil) GaugeF1B5E2B5F1C4E2C4@ 1mil@ 1mil@ 1mil@ 1milBOCDBOCDBOCDBOCDScrew Speed (rpm):30303030Specific Output (lb / hr-rpm)*1.471.471.471.47Die Sp. Output (lb / hr-in-die)*7.07.07.07.0Motor Load %50525152Melt Temperature (°C; °F)177; 350177; 350177; 350177; 351Heat Pressure (MPa; psi)27.2; 3,95029.4; 4,26028.1; 4,08530.0; 4,355Die Gap (mm; mil)1.5; 601.5; 601.5; 601.5; 60Blower %:63636363Take-up (m / min; ft / min)29.9; 9829.3; 9629.3; 9629.3; 96Frost Line Height (cm; in)28.7; 11.328.7; 11.328.7; 11.328.7; 11.3Blow up Ratio2.52.52.52.5*Estimated from screw rpm based on pre-established correlation Table 5B Primary Blends Film Blowing Data at 25.4 µm (1.0 mil) GaugeB1F5C2F5@ 1mil@ 1milConv. CDConv. CDScrew Speed (rpm):3030Specific Output (lb / hr-rpm)*1.471.47Die Sp. Output (lb / hr-in-die)*7.07.0Motor Load %4951Melt Temperature (°C;°F)176; 349177; 350Heat Pressure (MPa; psi)26.0; 3,77028.0; 4,065Die Gap (mm; mil)1.5; 601.5; 60Blower %:6060Take-up (m / min; ft / min)29.9; 9829.9; 98Frost Line Height (cm; in)28.7; 11.328.7; 11.3Blow up Ratio2.52.5 *Estimated from screw rpm based on pre-established correlation Table 5C Primary Blends Film Blowing Data at 25.4 µm (1.0 mil) GaugeB1E4C2E4@ 1mil@ 1milConv. CDConv. CDScrew Speed (rpm):3030Specific Output (lb / hr-rpm)*1.471.47Die Sp. Output (lb / hr-in-die)*7.07.0Motor Load %5051Melt Temperature (°C;°F)177; 351177; 351Heat Pressure (MPa; psi)28.0; 4,06528.8; 4,175Die Gap (mm; mil)1.5; 601.5; 60Blower %:6060Take-up (m / min; ft / min)29.9; 9829.9; 98Frost Line Height (cm; in)28.7; 11.328.7; 11.3Blow up Ratio2.52.5 *Estimated from screw rpm based on pre-established correlation Table 5D Primary Blends Film Blowing Data at 25.4 µm (1.0 mil) GaugeD3Exceed 1018@ 1mil@ 1milNMWD / NCD ControlNMWD / NCD ControlScrew Speed (rpm):3030Specific Output (lb / hr-rpm)*1.471.47Die Sp. Output (lb / hr-in-die)*7.07.0Motor Load %5253Melt Temperature (°C;°F)177; 350177; 351Heat Pressure (MPa; psi)29.0; 4,20529.6; 4,290Die Gap (mm; mil)1.5; 651.5; 60Blower %:6366Take-up (m / min; ft / min)29.9; 9829.6; 97Frost Line Height (cm; in)28.7; 11.328.7; 11.3Blow up Ratio2.52.5 *Estimated from screw rpm based on pre-established correlation Table 6A Secondary Blends Film Blowing Data at 25.4 µm (1.0 mil) GaugeExceed 1018 (2)4CB-15@ 1mil@ 1milNMWD / NCD50% F1B5Control50%B1F5Screw Speed (rpm):3030Specific Output (lb / hr-rpm)*1.471.47Die Sp. Output (lb / hr-in-die)*7.07.0Motor Load %5350Melt Temperature (°C;°F)177; 351176; 348Heat Pressure (MPa; psi)29.1; 4,22026.3; 3,820Die Gap (mm; mil)1.5; 601.5; 60Blower %:6565Take-up (m / min; ft / min)29.6; 9729.6; 97Frost Line Height (cm; in)28.7; 11.326.2; 10.3Blow up Ratio2.52.5 *Estimated from screw rpm based on pre-established correlation Table 6B Secondary Blends Film Blowing Data at 25.4 µm (1.0 mil) Gauge4CB-244CB-14@ 1mil@ 1mil50% E2C450% F1C450% C2E450% B1E4Screw Speed (rpm):3030Specific Output (lb / hr-rpm)*1.471.47Die Sp. Output (lb / hr-in-die)*7.07.0Motor Load %5251Melt Temperature (°C;°F)177; 350176; 349Heat Pressure (MPa; psi)29.0; 4,20528.0; 4,065Die Gap (mm; mil)1.5; 601.5; 60Blower %:6565Take-up (m / min; ft / min)29.6; 9729.6; 97Frost Line Height (cm; in)27.4; 10.827.4; 10.8Blow up Ratio2.52.5 *Estimated from screw rpm based on pre-established correlation Table 6C Secondary Blends Film Blowing Data at 25.4 µm (1.0 mil) Gauge4CB-255CB-135@ 1mil@ 1mil40% F1B550% E2B520% Exceed50% C2F540% B1F5Screw Speed (rpm):3030Specific Output (lb / hr-rpm)*1.471.47Die Sp. Output (lb / hr-in-die)*7.07.0Motor Load %5150Melt Temperature (°C; °F)177; 350177; 350Heat Pressure (MPa; psi)27.9; 4,05027.2; 3,950Die Gap (mm; mil)1.5; 601.5; 60Blower %:6565Take-up (m / min; ft / min)29.6; 9729.6; 97Frost Line Height (cm; in)27.9; 11.026.1; 10.3Blow up Ratio2.52.5 *Estimated from screw rpm based on pre-established correlation Table 6D Secondary Blends Film Blowing Data at 25.4 um (1.0 mil) Gauge5CB-2349CB-12345@ 1mil@ 1mil22% F1B540% E2C422% E2C420% Exceed12% Exceed40% C2E422% B1F522% C2E4Screw Speed (rpm):3030Specific Output (lb / hr-rpm)*1.471.47Die Sp. Output (lb / hr-in-die)*7.07.0Motor Load %5250Melt Temperature (°C; °F)177; 350177; 350Heat Pressure (MPa; psi)29.5; 4,28027.9; 4,050Die Gap (mm; mil)1.5; 601.5; 60Blower %:6565Take-up (m / min; ft / min)29.6; 9729.6; 97Frost Line Height (cm; in)27.4; 10.827.4; 10.8Blow up Ratio2.52.5 *Estimated from screw rpm based on pre-established correlation EXAMPLE II

[0113] Mechanical properties are important film characteristics, as polyethylene films typically face a multitude of forces throughout their lifetime. Therefore, these properties were investigated in blown films made from the secondary polyethylene blends and primary polyethylene blends of Example I. FIG. 2A and FIG. 2B provide a comparison of properties of blown films made from secondary polyethylene blends, blown films made only of the primary polyethylene blends (sometimes referred to as a parents or parental blend), and a blown film made from the polyethylene composition referred to as reference D3.

[0114] Both of the blown films made from secondary polyethylene blends in FIG. 2A and FIG. 2B show improved, or nearly equivalent, mechanical properties as compared to the reference D3. The secondary polyethylene blends also show notably improved puncture peak force and puncture break energy over both parents. The secondary polyethylene blends have Elmendorf tear in MD similar to their parent with higher Elmendorf tear in MD, all of which have greatly improved tear over the reference D3.

[0115] Tables 7A through 7D and Tables 8A through 8C show mechanical properties of 1.0 mil-thick blown films produced from the primary polyethylene blends (Tables 7A through 7D) and secondary polyethylene blends (Tables 8A through 8C). Table 7APrimary Blends Film Property at 25.4 µm (1.0 mil)F1B5E2B5F1C4@ 1 mil@ 1 mil@ 1 milMethod UsedGauge Mic (µm; mils)ASTM D6988Average28.7; 1.1328.7; 1.1329.5; 1.161% Secant (MPa; psi)ExxonMobilMD207; 30,051193; 27,929228; 33,045TD300; 43,568226; 32,842262; 38,065Avg254; 36,810210; 30,386245; 35,555TensileExxonMobilYield Strength (MPa; psi)MD9.3; 1,3508.6; 1,24410.1; 1,463TD11.5; 1,6669.7; 1,40311.5; 1,666Elongation @ Yield (%)MD5.75.46.0TD7.05.65.9Tensile Strength (MPa; psi)MD53; 7,64256; 8,05857; 8,297TD57; 8,27562; 9,00457; 8,214Elongation @ Break (%)MD396417439TD590602650Elmendorf TearASTM D1922MD (g / µm; g / mil)8.9; 2259.7; 24714.4; 365TD (g / µm; g / mil)16.2; 41117.3; 44021.1; 537Haze (%)ASTM D100315.510.810.5Internal (%)ExxonMobil3.922.713.08Gloss (GU)ASTM D2457MD374647TD445558Dart DropExxonMobilPhenolicMethod A(g / µm; g / mil)38.5; 97935.2; 89423.5; 597PunctureExxonMobilBTEC Probe B1Peak Force (g / µm; lbs / mil)176; 9.84191; 10.68176; 9.86Break Energy (N-m / mm; in-lbs / mil)125; 28.14141; 31.74124; 27.92Heat SealExxonMobilHeat seal temp @ 1 N (°C)86.0<9590.6Heat seal temp @ 5 N (°C)90.197.296.9Max. Heat Seal (N)14.213.014.8Hot TackExxonMobilHot tack temp @ 1 N (°C)84.492.793.0Hot tack temp @ 5 N (°C)89.7100.2100.4Max. Hot Tack (N)14.613.011.8 Table 7B Primary Blends Film Property at 25.4 um (1.0 mil)E2C4B1F5C2F5@ 1 mil@ 1 mil@ 1 milMethod UsedGauge Mic (µm; mils)ASTM D6988Average28.7; 1.1327.4; 1.0829.5; 1.161% Secant (MPa; psi)ExxonMobilMD200; 29,039244; 35,359211; 30,553TD228; 33,097294; 42,595238; 34,492Avg214; 31,068269; 38,977224; 32,523TensileExxonMobilYield Strength (MPa; psi)MD9.8; 1,41810.2; 1,4839.5; 1,380TD10.6; 1,54011.7; 1,70310.1; 1,459Elongation @ Yield (%)MD6.16.56.6TD6.15.85.8Tensile Strength (MPa; psi)MD62; 9,04052; 7,54455; 8,015TD58; 8,36049; 7,03750; 7,204Elongation @ Break (%)MD452728630TD623774680Elmendorf TearASTM D1922MD (g / µm; g / mil)10.8; 27517.4; 44216.6; 422TD (g / µm; g / mil)17.9; 45524.5; 62225.2; 641Haze (%)ASTM D10037.715.512.3Internal (%)ExxonMobil3.024.455.07Gloss (GU)ASTM D2457MD483744TD594642Dart DropExxonMobilPhenolicMethod A(g / µm; g / mil)28.9; 7355.4; 13810.4; 263PunctureExxonMobilBTEC Probe B1Peak Force (g / µm; lbs / mil)188; 10.51161; 9.00162; 9.06Break Energy (N-m / mm; in-lbs / mil)130; 29.27121; 27.10121; 27.21Heat SealExxonMobilHeat seal temp @ 1 N (°C)95.075.585.6Heat seal temp @ 5 N (°C)100.882.191.9Max. Heat Seal (N)13.415.414.8Hot TackExxonMobilHot tack temp @ 1 N (°C)96.382.488.6Hot tack temp @ 5 N (°C)101.2116.794.4Max. Hot Tack (N)12.15.86.9 Table 7C Primary Blends Film Property at 25.4 um (1.0 mil)B1E4C2E4D3@ 1 mil@ 1 mil@ 1 milMethod UsedGauge Mic ((µm; mils)ASTM D6988Average28.7; 1.1329.2; 1.1529.0; 1.141% Secant (MPa; psi)ExxonMobilMD256; 37,078224; 32,511195; 28,251TD307; 44,490252; 36,527210; 30,499Avg281; 40,784238; 34,519203; 29,375TensileExxonMobilYield Strength (MPa; psi)MD11.2; 1,62710.3; 1,4949.4; 1,366TD12.8; 1,85211.0; 1,60010.1; 1,472Elongation @ Yield (%)MD7.45.96.0TD5.95.85.8Tensile Strength (MPa; psi)MD53; 7,63058; 8,42658; 8,483TD50; 7,29753; 7,74360; 8,660Elongation @ Break (%)MD603583488TD765717661Elmendorf TearASTM D1922MD (g / µm; g / mil)11.7; 29815.4; 39111.1; 283TD (g / µm; g / mil)25.0; 63522.0; 55917.3; 440Haze (%)ASTM D100310.98.75.9Internal (%)ExxonMobil3.16.142.24Gloss (GU)ASTM D2457MD486566TD535763Dart DropExxonMobilPhenolicMethod A(g / µm; g / mil)4.8; 1216.7; 17115.2; 386PunctureExxonMobilBTEC Probe B1Peak Force (g / µm; lbs / mil)171; 9.58177; 9.92199; 11.12Break Energy (N-m / mm; in-lbs / mil)122; 27.38129; 29.03154; 34.62Heat SealExxonMobilHeat seal temp @ 1 N (°C)<9091.4<105Heat seal temp @ 5 N (°C)97.197.2107.1Max. Heat Seal (N)15.114.213.1Hot TackExxonMobilHot tack temp @ 1 N (°C)100.597.9103.5Hot tack temp @ 5 N (°C)114.5103.7110.6Max. Hot Tack (N)5.46.89.7 Table 7D Primary Blends Film Property at 25.4 um (1.0 mil)Exceed 1018 (1)@ 1 milMethod UsedGauge Mic (µm; mils)ASTM D6988Average29.2; 1.151% Secant (MPa; psi)ExxonMobilMD183; 26,516TD203; 29,456Avg193; 27,986TensileExxonMobilYield Strength (MPa; psi)MD9.4; 1,364TD9.7; 1,400Elongation @ Yield (%)MD6.4TD5.6Tensile Strength (MPa; psi)MD71; 10,252TD64; 9,263Elongation @ Break (%)MD479TD624Elmendorf TearASTM D1922MD (g / µm; g / mil)10.2; 257TD (g / µm; g / mil)16.6; 422Haze (%)ASTM D10038.9Internal (%)ExxonMobil2.12Gloss (GU)ASTM D2457MD58TD57Dart DropExxonMobilPhenolicMethod A(g / µm; g / mil)23.5; 597PunctureExxonMobilBTEC Probe B1Peak Force (g / µm; lbs / mil)199; 11.16Break Energy (N-m / mm; in-lbs / mil)154; 34.63Heat SealExxonMobilHeat seal temp @ 1 N (°C)100.2Heat seal temp @ 5 N (°C)102.5Max. Heat Seal (N)13.4Hot TackExxonMobilHot tack temp @ 1 N (°C)100.4Hot tack temp @ 5 N (°C)104.9Max. Hot Tack (N)11.0 Table 8A Secondary Blends Film Property at 25.4 µm (1.0 mil)Exceed-24CB-154CB-24Method UsedGauge Mic (µm;_mils)ASTM D6988Average30.5; 1.227.9; 1.130.5; 1.21% Secant (MPa; psi)ExxonMobilMD175; 25,346223; 32,433214; 31,097TD186; 27,047266; 38,595249; 36,182Avg181; 26,197245; 35,514232; 33,640TensileExxonMobilYield Strength (MPa; psi)MD8.6; 1,24692; 1,3379.3; 1,356TD9.1; 1,31610.7; 1,55410.1; 1,465Elongation @ Yield (%)MD6.76.15.9TD6.06.45.8Tensile Strength (MPa; psi)MD60; 8,64455; 7,99658; 8,358TD55; 8,02450; 7,24656; 8,137Elongation @ Break (%)MD500559526TD635703707Elmendorf TearASTM D1922MD (g / µm; g / mil)9.7; 24716.8; 42715.6; 397TD (g / µm; g / mil)15.6; 39622.4; 56821.0; 534Haze (%)ASTM D100311.39.58.2Internal (%)ExxonMobil3.04.02.9Gloss (GU)ASTM D2457MD385563TD405666Dart DropExxonMobilPhenolicMethod A(g / µm; g / mil)282; 71614.2; 36013.3; 338PunctureExxonMobilBTEC Probe B1Peak Force (g / µm; lbs / mil)223; 12.51218; 12.19228; 12.76Break Energy (N-m / mm; in-lbs / mil)159; 35.72174; 39.17194; 43.52Heat SealExxonMobilHeat seal temp @ 1 N (°C)1029197Heat seal temp @ 5 N (°C)1029297Max. Heat Seal (N)13.815.214.1Hot TackExxonMobilHot tack temp @ 1 N (°C)1018996Hot tack temp @ 5 N (°C)111102103Max. Hot Tack (N)15.29.88.6 Table 8B Secondary Blends Film Property at 25.4 um (1.0 mil)4CB-144CB-255CB-135Method UsedGauge Mic (µm; mils)ASTM D6988Average30.5; 1.230.5; 1.230.5; 1.21% Secant (MPa; psi)ExxonMobilMD224; 32,549198; 28,758212; 30,753TD270; 39,151226; 32,756240; 34,839Avg247; 35,850212; 30,757226; 32,796TensileExxonMobilYield Strength (MPa; psi)MD10.5; 1,5208.9; 1,2939.2; 1,341TD11.2; 1,6279.6; 1,39810.0; 1,453Elongation @ Yield (%)MD6.96.46.6TD6.06.26.0Tensile Strength (MPa; psi)MD527; 7,64357.8; 8,39054.3; 7,884TD54.4; 7,88555.7; 8,076537; 7,785Elongation @ Break (%)MD535531538TD752681715Elmendorf TearASTM D1922MD (g / µm; g / mil)17.0; 43216.5; 42017.3; 439TD (g / µm; g / mil)20.7; 52721.1; 53521.5; 547Haze (%)ASTM D10039.511.39.2Internal (%)ExxonMobil3.73.54.0Gloss (GU)ASTM D2457MD645143TD645647Dart DropExxonMobilPhenolicMethod A(g / µm; g / mil)7.5; 19020.3; 51514.8; 377PunctureExxonMobilBTEC Probe B1Peak Force (g / µm; lbs / mil)228; 12.74229; 12.83172; 9.62Break Energy (N-m / mm; in-lbs / mil)177; 39.77190; 42.72120; 27.01Heat SealExxonMobilHeat seal temp @ 1 N (°C)959187Heat seal temp @ 5 N (°C)959288Max. Heat Seal (N)14.814.914.9Hot TackExxonMobilHot tack temp @ 1 N (°C)989193Hot tack temp @ 5 N (°C)10698103Max. Hot Tack (N)9.98.98.1 Table 8C Secondary Blends Film Property at 25.4 um (1.0 mil)5CB-2349CB-12345Method UsedGauge Mic (µm; mils)ASTM D6988Average27.9; 1.130.5; 1.21% Secant (MPa; psi)ExxonMobilMD200; 29,025208; 30,194TD231; 33,495239; 34,715Avg218; 31,260224; 32,455TensileExxonMobilYield Strength (MPa; psi)MD9.4; 1,3639.4; 1,367TD10.0; 1,44599; 1,432Elongation @ Yield (%)MD6.46.1TD6.05.5Tensile Strength (MPa; psi)MD56; 8,12854; 7,857TD52; 7,61249; 7,133Elongation @ Break (%)MD518520TD666664Elmendorf TearASTM D1922MD (g / µm; g / mil)14.3; 36315.6; 395TD (g / µm; g / mil)20.6; 52222.2; 563Haze (%)ASTM D10039.57.5Internal (%)ExxonMobil4.14.0Gloss (GU)ASTM D2457MD6958TD7159Dart DropExxonMobilPhenolicMethod A(g / µm; g / mil)11.5; 29113.9; 353PunctureExxonMobilBTEC Probe B1Peak Force (g / µm; lbs / mil)218; 12.18218; 12.20Break Energy (N-m / mm; in-lbs / mil)170; 38.12169; 38.02Heat SealExxonMobilHeat seal temp @ 1 N (°C)9993Heat seal temp @ 5 N (°C)10094Max. Heat Seal (N)14.715.2Hot TackExxonMobilHot tack temp @ 1 N (°C)10097Hot tack temp @ 5 N (°C)106103Max. Hot Tack (N)11.010.6

[0116] Tables 7A through 7D and Tables 8A through 8C show that blown films made from the secondary polyethylene blends generally have improved puncture peak force, puncture break energy, Elmendorf Tear in MD and glossiness (in both MD and TD) when compared to blown films made only from either of the primary polyethylene blends. With these improved properties, blown films made from the secondary polyethylene blends can maintain a similar heat seal initiation temperature at 5 N, hot tack seal initiation temperature at 1 N, and average MD / TD 1% secant modulus as the primary polyethylene blends. Generally, blown films made from the secondary polyethylene blends had dart drop (dart drop impact or dart impact) values that fall between the values of the primary polyethylene blends, suggesting that this property could be adjusted through the wt% of primary polyethylene blends.

[0117] Puncture properties were investigated (FIG. 3). With one exception, the secondary polyethylene blends demonstrated significantly improved puncture peak force and puncture break energy over the primary polyethylene blends.

[0118] FIG. 4 shows a plot of the resultant elution peaks from a TREF experiment on a secondary polyethylene blend and the primary polyethylene blends. The secondary polyethylene blend yields peaks in between the primary polyethylene blends, suggesting that some co-crystallization occurs between the polyethylene compositions. This co-crystallization could account for the synergistically improved mechanical properties of the secondary polyethylene blends over the primary polyethylene blends.

[0119] Heat seal and hot tack curves are shown FIG. 5A and FIG. 5B, respectively, for 1 mil blown films made from one secondary polyethylene blend, the primary polyethylene blends and the reference D3. The secondary polyethylene blend and the primary polyethylene blends had better sealing properties than the reference D3. That is, each generally had a lower heat seal initiation temperature at 5 N, a lower hot tack seal initiation temperature at 1 N, a higher max heat seal strength, and a higher max hot tack strength when compared to the reference D3.

[0120] [Deleted]

[0121] [Deleted]

Claims

1. A film having an Elmendorf tear in MD greater than or equal to 14.2 g / µm (360 g / mil), and a puncture peak force greater than or equal to 214 g / µm (12.0 lb / mil), or a puncture break energy greater than or equal to 165 N-m / mm (37.0 in-lb / mil), the film comprising a secondary polyethylene blend, the secondary polyethylene blend comprising two primary polyethylene blends, each primary polyethylene blend comprising two polyethylene compositions, each polyethylene composition having a density, wherein the density of each of the polyethylene compositions differs from the other in an amount between 0.050 g / cm3 and 0.060 g / cm3, and each primary polyethylene blend having a density between 0.918 g / cm3 and 0.922 g / cm3 and an MI (I2) between 0.90 g / 10 min and 1.10 g / 10 min.

2. The film of claim 1, wherein the secondary polyethylene blend comprises 50 wt% of each primary polyethylene blend.

3. The film of claim 1, wherein the primary polyethylene blend comprises a polyethylene composition having a density of 0.8961 g / cm3 and an MI (I2) of 0.28 g / 10 min in an amount between 55 wt% and 57 wt%, and another polyethylene composition having a density of 0.9510 g / cm3 and an MI (I2) of 4.2 g / 10 min in an amount between 43 wt% and 45 wt%.

4. The film of claim 1, wherein one of the primary polyethylene blends comprises a polyethylene composition having a density of 0.8983 g / cm3 and an MI (I2) of 7.8 g / 10 min in an amount between 56 wt% and 58 wt%, and another polyethylene composition having a density of 0.9516 g / cm3 and an MI (I2) of 0.20 g / 10 min in an amount between 42 wt% and 44 wt%.

5. The film of any of the preceding claims, wherein the secondary polyethylene blend further comprises a polyethylene composition having a density of 0.918 g / cm3 and an MI (I2) of 1.0 g / 10 min in an amount between 10 wt% and 25 wt%.

6. The film of any of the preceding claims, wherein the film has a dart drop greater than or equal to 7.5 g / µm (190 g / mil).

7. The film of any of the preceding claims, wherein the film has an average gloss between 45 GU and 70 GU.

8. The film of any of the preceding claims, wherein the secondary polyethylene blend comprises two primary polyethylene blends, each primary polyethylene blend having a density between 0.919 g / cm3 and 0.922 g / cm3, and an MI (I2) between 0.93 g / 10 min and 1.09 g / 10 min.