Adhesive-free thermal laminated barrier heat seal film containing polyethylene

Abstract

Heat-sealable barrier laminates comprising polyethylene are provided. The laminates are adhesive-free and can be fully compatible with polyethylene recycle streams. They can exhibit improved, maintained, or desirable properties compared to existing laminate structures that are not fully compatible with polyethylene recycle streams. The laminates include a multilayer film and an oriented film. The oriented film is heat-laminated to an outer layer of the multilayer film to provide the laminate.

Description

[Technical Field]

[0001] FIELD OF THE DISCLOSURE Embodiments of the present disclosure relate generally to laminates, and more particularly to laminates comprising polyethylene.

[0002] Introduction Laminates incorporating polypropylene, polyamide, and polyethylene terephthalate contain multiple layers and are widely used in flexible packaging for consumer products. For example, a typical laminate for flexible packaging may include an outer printed substrate of biaxially oriented polypropylene (BOPP), a barrier layer of metallized film, an adhesive layer of solvent-based adhesive, and a sealant layer of polyethylene. The combination of layers and materials may enable a wide seal window, good printability, high barrier performance, and heat resistance for sealing without shrinkage. However, such laminates may be difficult, if not impossible, to recycle together due to different types of materials that are not compatible with each other for recycling. As the demand for sustainable and recyclable materials continues to rise, there remains a strong need for laminates that can be more easily recycled and exhibit equivalent or improved performance characteristics to existing structures. Summary of the Invention

[0003]

[0003] Embodiments of the present disclosure fulfill the aforementioned needs by providing laminates that are thermally bonded without laminating adhesives and are fully compatible with recycling in polyethylene recycle streams. The performance of the laminates of the present invention may be better than, or at least comparable to, other laminates, such as those containing BOPP, and may allow for, for example, the use of faster packaging speeds during manufacturing. In aspects, the recyclable laminates may exhibit improved or maintained properties, such as bond strength, oxygen transmission rate (OTR), water vapor transmission rate (WVTR), heat seal initiation temperature (HSIT), heat seal strength, hot tack strength, hot tack initiation temperature, and / or shrinkage, compared to existing laminates.

[0004] Disclosed herein is a laminate. In embodiments, the laminate includes: (a) an outer layer comprising: (1) at least one of an anhydride-modified ethylene acrylate copolymer, an anhydride-modified polyethylene, an anhydride-modified ethylene vinyl acetate, an ethylene-vinyl acetate copolymer, a polyethylene / vinyl acetate copolymer, a polyethylene / acrylic acid ethylene copolymer, a polyethylene / acrylate copolymer, or a polyethylene elastomer / plastomer; (2) a barrier layer comprising an ethylene-vinyl alcohol copolymer; and (3) a sealant layer, wherein the sealant layer comprises at least 70% by weight of a polymer having a maximum peak melting temperature (T m (b) a sealant layer comprising a polymer having a viscosity of 0.900 to 0.970 g / cm; (c) a sealant layer comprising a polymer having a viscosity of 0.900 to 0.970 g / cm; and (d) a tie layer between the barrier layer and the sealant layer. 3 and an oriented film comprising an ethylene-based polymer having a density of

[0005] These and other embodiments are described in more detail in the detailed description. [Brief explanation of the drawings]

[0006] [Figure 1] 1 is a heat seal strength graph of the comparative examples and inventive examples discussed below. [Figure 2] 1 is a hot tack strength graph of the comparative examples and inventive examples discussed below. DETAILED DESCRIPTION OF THE INVENTION

[0007] Aspects of the disclosed laminates are described in more detail below. The laminates may have a wide variety of uses, including, for example, pouches, stand-up pouches, pillow pouches, bulk bags, prefabricated packaging, sachets, etc. However, the present disclosure should not be construed as limiting the embodiments described below, as the present disclosure is an exemplary implementation of the embodiments described herein.

[0008] As used herein, the term "polymer" refers to a polymeric compound prepared by polymerizing monomers, whether of the same or different types. Thus, the generic term "polymer" encompasses the term homopolymer (used to refer to a polymer prepared from only one type of monomer), as well as the terms copolymer or interpolymer. Minor impurities (e.g., catalyst residues) may be incorporated into and / or within the polymer. The polymer may be a single polymer, a polymer blend, or a polymer mixture, including a mixture of polymers formed in situ during polymerization.

[0009] As used herein, the term "polyethylene" or "ethylene-based polymer" refers to a polymer containing a majority (>50 mol%) of units derived from ethylene monomers. This includes polyethylene homopolymers and copolymers (meaning units derived from two or more comonomers). Common forms of polyethylene known in the art include low-density polyethylene (LDPE), linear low-density polyethylene (LLDPE), ultra-low-density polyethylene (ULDPE), very low-density polyethylene (VLDPE), single-site catalyzed linear low-density polyethylene (m-LLDPE), including both linear and substantially linear low-density resins, ethylene-based plastomers (POP) and ethylene-based elastomers (POE), medium-density polyethylene (MDPE), and high-density polyethylene (HDPE). These polyethylene materials are generally known in the art. However, the following description may be helpful in understanding the differences between some of these different polyethylene resins.

[0010] The term "LDPE" may also be referred to as "high pressure ethylene polymer" or "highly branched polyethylene" and is defined to mean that the polymer is partially or fully homopolymerized or copolymerized in an autoclave or tubular reactor at pressures above 14,500 psi (100 MPa) using a free radical initiator, such as peroxide (see, for example, U.S. Pat. No. 4,599,392, incorporated by reference). LDPE resins typically have a density of 0.916 to 0.935 g / cm. 3 The density is in the range of

[0011] The term "LLDPE" includes both resins made using single-site catalysts, including, but not limited to, traditional Ziegler-Natta catalyst systems and chromium-based catalysts, as well as mono- or bis-cyclopentadienyl catalysts (typically referred to as metallocenes) and constrained geometry catalysts, phosphinimine catalysts, and polyaryloxy ether catalysts (typically referred to as bisphenylphenoxy), and includes linear, substantially linear, or heterogeneous polyethylene copolymers or homopolymers. LLDPE contains less long chain branching than LDPE and includes substantially linear ethylene polymers as further defined in U.S. Patent Nos. 5,272,236, 5,278,272, 5,582,923, and 5,733,155, homogeneously branched linear ethylene polymer compositions such as those in U.S. Patent No. 3,645,992, heterogeneously branched ethylene polymers such as those prepared according to the process disclosed in U.S. Patent No. 4,076,698, and / or blends thereof (such as those disclosed in U.S. Patent No. 3,914,342 or 5,854,045). LLDPE may be made via gas phase, solution phase, or slurry polymerization, or any combination thereof, using any type of reactor or reactor configuration known in the art.

[0012] The term "MDPE" refers to 0.926-0.935 g / cm 3 "MDPE" refers to polyethylene having a density of 1000 MPa or less. "MDPE" is typically produced using chromium or Ziegler-Natta catalysts, or using single-site catalysts including, but not limited to, substituted mono- or bis-cyclopentadienyl catalysts (typically referred to as metallocenes), constrained geometry catalysts, phosphinimine catalysts, and polyaryloxy ether catalysts (typically referred to as bisphenylphenoxy), and typically has a molecular weight distribution ("MWD") greater than 2.5.

[0013] The term "HDPE" refers to a polymer having a density of about 0.935 g / cm, typically prepared using a single-site catalyst, including, but not limited to, Ziegler-Natta, chromium, or substituted mono- or bis-cyclopentadienyl catalysts (typically referred to as metallocenes), constrained geometry catalysts, phosphinimine catalysts, and polyaryloxy ether catalysts (typically referred to as bisphenylphenoxy). 3 Super ~ maximum approx. 0.980g / cm 3 It refers to polyethylene having a density of

[0014] The term "ULDPE" refers to polymers with a yield of 0.855 to 0.912 g / cm, typically prepared using single-site catalysts, including, but not limited to, Ziegler-Natta catalysts, chromium catalysts, or substituted mono- or bis-cyclopentadienyl catalysts (typically referred to as metallocenes), constrained geometry catalysts, phosphinimine catalysts, and polyaryloxy ether catalysts (typically referred to as bisphenylphenoxy). 3 ULDPE refers to polyethylene having a density of 1000 MPa (1000 MPa). ULDPE includes, but is not limited to, polyethylene (ethylene-based) plastomers and polyethylene (ethylene-based) elastomers.

[0015] As used herein, the term "polyethylene elastomer / plastomer" refers to a polymer that contains units derived from ethylene and at least one C3-C6 10 "polyethylene elastomers" refers to substantially linear or linear ethylene / α-olefin copolymers containing a homogeneous distribution of short chain branches comprising units derived from an α-olefin comonomer, or at least one C4-C8 α-olefin comonomer, or at least one C6-C8 α-olefin comonomer. Polyethylene elastomers / plastomers have a molecular weight of 0.865 g / cm. 3 , or 0.870 g / cm 3 , or 0.880 g / cm 3 , or 0.890 g / cm 3 ~0.900g / cm 3 , or 0.902 g / cm 3 , or 0.904 g / cm3 , or 0.909 g / cm 3 , or 0.910 g / cm 3 Non-limiting examples of polyethylene elastomers / plastomers include AFFINITY™ plastomers and elastomers (available from The Dow Chemical Company), EXACT™ plastomers (available from ExxonMobil Chemical), Tafmer (available from Mitsui), Nexlene™ (available from SK Chemicals Co.), and Lucene™ (available from LG Chem Ltd.).

[0016] The terms "comprising," "including," "having," and their derivatives are not intended to exclude the presence of any additional component, step, or procedure, whether specifically disclosed or not. For the avoidance of doubt, all compositions claimed through the use of the term "comprising" may include any additional additive, adjuvant, or compound, whether polymeric or otherwise, unless otherwise stated to the contrary. In contrast, the term "consisting essentially of" excludes from the scope of any subsequent description any other component, step, or procedure, except those that are not essential to operability. The term "consisting of" excludes any component, step, or procedure not specifically delineated or listed.

[0017] Laminated multilayer film The laminates disclosed herein include multilayer films. The multilayer films according to embodiments disclosed herein include an outer layer, a barrier layer, a sealant layer, and a tie layer. In further embodiments, the multilayer films include a second tie layer in addition to the outer layer, barrier layer, sealant layer, and tie layer.

[0018] Outer layer of multilayer film The multilayer film of the laminate includes an outer layer.

[0019] In embodiments, the outer layer of the multilayer film may be laminated to an oriented film as described below and positioned next to or adjacent to a barrier layer comprising an ethylene vinyl alcohol copolymer. In other embodiments, a second tie layer is disposed between the outer layer and the barrier layer. In still further embodiments, additional layers may be disposed between the outer layer and the barrier layer.

[0020] According to embodiments disclosed herein, the outer layer of the multilayer film comprises at least one of an anhydride-modified ethylene acrylate copolymer, an anhydride-modified polyethylene, an anhydride-modified ethylene vinyl acetate, a polyethylene / acrylic acid ethylene copolymer, an ethylene-vinyl acetate copolymer, a polyethylene / vinyl acetate copolymer, a polyethylene / acrylate copolymer, or a polyethylene elastomer / plastomer.

[0021] In embodiments where the outer layer comprises an ethylene-vinyl acetate copolymer, the ethylene-vinyl acetate copolymer has a viscosity of 0.930 to 0.980 g / cm 3 It may have a density in the range of 0.930 to 0.980 g / cm 3 All individual values ​​and subranges of density are disclosed and included herein, for example, ethylene-vinyl acetate copolymers have a density of 0.930 to 0.980 g / cm 3 , 0.935~0.970g / cm 3 , 0.935~0.950g / cm 3 , 0.935~0.945g / cm 3 , or 0.940 to 0.945 g / cm 3 The density may range from 0.01 to 0.01.

[0022] In embodiments where the outer layer comprises an ethylene-vinyl acetate copolymer, the ethylene-vinyl acetate copolymer may have a melt index (I2) from 0.1 g / 10 min to 500 g / 10 min, or from 0.2 g / 10 min to 400 g / 10 min, or from 0.5 g / 10 min to 100 g / 10 min, or from 0.1 to 30 g / 10 min, or from 0.1 to 10 g / 10 min.

[0023] In embodiments in which the outer layer comprises an ethylene-vinyl acetate copolymer, the ethylene-vinyl acetate copolymer may have a vinyl acetate content of 5 to 50 wt %, based on the total weight of the ethylene-vinyl acetate copolymer. All individual values ​​and subranges between 5 wt % and 50 wt % vinyl acetate content are disclosed and included herein. For example, in some embodiments, the ethylene-vinyl acetate copolymer may have a vinyl acetate content of 5 to 10 wt %, 10 to 30 wt %, or 30 to 50 wt %, based on the total weight of the ethylene-vinyl acetate copolymer.

[0024] An example of a commercially available ethylene-vinyl acetate copolymer that may be used in some embodiments includes ELVAX™ 470 (18% by weight vinyl acetate content) available from The Dow Chemical Company, Midland, MI.

[0025] In embodiments where the outer layer comprises a polyethylene / acrylate copolymer, the polyethylene / acrylate copolymer has a density of 0.925 to 0.955 g / cm 3 It may have a density in the range of 0.925 to 0.955 g / cm 3 All individual values ​​and subranges of density are disclosed and included herein, for example, polyethylene / acrylate copolymers have a density of 0.925 to 0.955 g / cm 3 , 0.925~0.945g / cm 3 , 0.930~0.955g / cm 3 , 0.930~0.945g / cm 3 , 0.935~0.955g / cm 3 , or 0.935 to 0.945 g / cm 3 The density may range from 0.01 to 0.01.

[0026] In embodiments where the outer layer comprises a polyethylene / acrylate copolymer, the polyethylene / acrylate copolymer may have a melt index (I2) of from 0.1 g / 10 min to 50 g / 10 min, or from 0.5 g / 10 min to 20 g / 10 min, or from 1.0 g / 10 min to 10 g / 10 min.

[0027] Commercially available examples of polyethylene / acrylate copolymers that can be used in the outer layer include those sold under the BYNEL™ name by The Dow Chemical Company (Midland, MI), including, for example, BYNEL™ 22E780 adhesive resin and BYNEL™ 22E757 adhesive resin.

[0028] In embodiments where the outer layer comprises a polyethylene elastomer / plastomer, the polyethylene elastomer / plastomer has a modulus of 0.865 to 0.910 g / cm 3 It may have a density in the range of 0.865 to 0.910 g / cm 3 All individual values ​​and subranges of density are disclosed and included herein, for example, polyethylene elastomer / plastomers have a density of 0.865 to 0.910 g / cm 3 , 0.865~0.900g / cm 3 , 0.865~0.890g / cm 3 , 0.865~0.880g / cm 3 , 0.870~0.910g / cm 3 , 0.870~0.900g / cm 3 , 0.870~0.890g / cm 3 , 0.870~0.880g / cm 3 , 0.880~0.910g / cm 3 , 0.880~0.900g / cm 3 , 0.880~0.890g / cm 3 , 0.890~0.910g / cm 3 , 0.890~0.900g / cm 3 , or 0.900 to 0.910 g / cm 3 The density may range from 0.01 to 0.01.

[0029] In embodiments in which the outer layer comprises a polyethylene elastomer / plastomer, the polyethylene elastomer / plastomer may have a melt index (I2) in the range of 0.50 to 20 g / 10 minutes (g / 10 min). All individual values ​​and subranges of melt index from 0.50 to 20 g / 10 min are disclosed and included herein, for example, the polyethylene elastomer / plastomer may have a melt index from a lower limit of 0.50, 1.0, 2.0, 5.0, 10.0, 15, or 18 g / 10 min to an upper limit of 1.0, 2.0, 5.0, 10.0, 15, 18, 19, or 20 g / 10 min.

[0030] Commercially available examples of polyethylene plastomers / elastomers that may be used in the outer layer include those sold under the AFFINITY™ name by The Dow Chemical Company (Midland, MI), including, for example, AFFINITY™ VP 8770G1, AFFINITY™ PF7266, AFFINITY™ PL 1881G, and AFFINITY™ PF1140G.

[0031] In embodiments, the outer layer further comprises at least one of linear low density polyethylene, low density polyethylene, medium density polyethylene, or high density polyethylene. In such embodiments, the outer layer may comprise up to 50% by weight of at least one of linear low density polyethylene, low density polyethylene, medium density polyethylene, or high density polyethylene.

[0032] Barrier layer of multilayer film The multilayer film of the laminate includes a barrier layer.

[0033] In embodiments, the barrier layer of the multilayer film may be positioned adjacent to or near the tie layer described below and the outer layer described above. The barrier layer according to embodiments disclosed herein comprises an ethylene vinyl alcohol copolymer (EVOH).

[0034] In embodiments, the EVOH of the barrier layer has an ethylene content of 20-50 mol%. All subranges and individual values ​​between 20-50 mol% ethylene content are disclosed and included herein. For example, in embodiments, the EVOH of the barrier layer has an ethylene content of 20-50 mol%, or 22-45 mol%, or 25-40 mol%. Those skilled in the art will understand that the ethylene content of the EVOH can contribute to a lower or higher OTR of the laminates disclosed herein (i.e., generally, the lower the ethylene content, the lower the achievable OTR value). Those skilled in the art will also understand that barrier layers comprising EVOH with lower ethylene content may be suitable for flexible bottle and tube applications, while barrier layers comprising EVOH with higher ethylene content may enable easier processing, long-term running stability, and packaging types requiring flexibility (flex crack resistance), such as thermoformability.

[0035] Commercially available examples of EVOH that can be used in the barrier layer include those sold under the name EVAL™ by Kuraray Co., Ltd. (Tokyo, Japan), including, for example, EVAL™ H171B (ethylene content of 38 mol%) and EVAL™ F171B (ethylene content of 32 mol%).

[0036] Various thicknesses are contemplated for the multilayer film. In embodiments, the barrier layer is 5-25% of the total thickness of the multilayer film.

[0037] Sealant layer of multilayer film The multilayer film of the laminate includes a sealant layer.

[0038] The sealant layer of the multilayer film comprises at least 70% by weight of a polymer having a maximum peak melting temperature (T m) The sealant layer can act as an inner surface of the laminate, for example, to provide a method for sealing the packaging around a packaged product. The composition of the sealant layer can affect the ability of the laminate and sealant layers to achieve high seal bond strength at lower sealing temperatures. In embodiments, the sealant layer is at least 10 microns thick. In further embodiments, the sealant layer is 25-60% of the total thickness of the multilayer film.

[0039] The sealant layer of the multilayer film comprises at least 70 wt. % polymer, based on the total weight of the sealant layer. All individual values ​​and subranges of at least 70 wt. % are disclosed and included herein. For example, in embodiments, the sealant layer can comprise at least 70 wt. %, at least 80 wt. %, at least 90 wt. %, at least 95 wt. %, at least 99 wt. %, at least 99.5 wt. %, or 70 wt. % to 100 wt. %, 75 wt. % to 99 wt. %, 80 wt. % to 95 wt. %, or 90 wt. % to 95 wt. % polymer, based on the total weight of the sealant layer.

[0040] The sealant layer of the multilayer film comprises at least 70% by weight of a polymer having a maximum peak melting temperature (T m All individual values ​​and subranges of 108°C or less are disclosed and included herein. For example, in embodiments, the polymer of the sealant layer has a maximum peak melting temperature (T ) of 108°C or less, 106°C or less, 104°C or less, 102°C or less, 100°C or less, 98°C or less, 96°C or less, 94°C or less, or 92°C or less, or in the range of 70°C to 108°C, 70°C to 100°C, 70°C to 95°C, 75°C to 108°C, 75°C to 100°C, or 75°C to 95°C. m ) and has the highest peak melting temperature (T m ) can be measured according to the DSC test method described below.

[0041] In embodiments, the polymer of the sealant layer has a maximum peak melting temperature (T mIn such an embodiment, the polyethylene elastomer / plastomer of the sealant layer comprises or consists of a polyethylene elastomer / plastomer having a modulus of elasticity of 0.865 to 0.910 g / cm 3 It may have a density in the range of 0.865 to 0.910 g / cm 3 All individual values ​​and subranges of density are disclosed and included herein, for example, polyethylene elastomer / plastomers have a density of 0.865 to 0.910 g / cm 3 , 0.865~0.900g / cm 3 , 0.865~0.890g / cm 3 , 0.865~0.880g / cm 3 , 0.865~0.870g / cm 3 , 0.870~0.910g / cm 3 , 0.870~0.900g / cm 3 , 0.870~0.890g / cm 3 , 0.870~0.880g / cm 3 , 0.880~0.910g / cm 3 , 0.880~0.900g / cm 3 , 0.880~0.890g / cm 3 , 0.890~0.910g / cm 3 , 0.890~0.900g / cm 3 , or 0.900 to 0.910 g / cm 3 The density may range from 0.01 to 0.01.

[0042] In embodiments in which the sealant layer polymer comprises or consists of a polyethylene elastomer / plastomer, the polyethylene elastomer / plastomer may have a melt index (I2) in the range of 0.50 to 20 g / 10 minutes (g / 10 min). All individual values ​​and subranges of melt index from 0.50 to 20 g / 10 min are disclosed and included herein, for example, the polyethylene elastomer / plastomer may have a melt index from a lower limit of 0.50, 1.0, 2.0, 5.0, 10.0, 15, or 18 g / 10 min to an upper limit of 1.0, 2.0, 5.0, 10.0, 15, 18, 19, or 20 g / 10 min.

[0043] Commercially available examples of polyethylene elastomers / plastomers that can be used in the sealant layer include those sold under the AFFINITY™ name by The Dow Chemical Company (Midland, MI), including, for example, AFFINITY™ VP 8770G1, AFFINITY™ PF7266, AFFINITY™ PL 1881G, and AFFINITY™ PF1140G.

[0044] In embodiments, the polymer of the sealant layer has a maximum peak melting temperature (T m The ionomer of ethylene (meth)acrylic acid copolymer having a cation source (also referred to herein as "ionomer of ethylene acid copolymer") may comprise or consist of a cation source of ethylene (meth)acrylic acid copolymer having a cation source source of ethylene acid copolymer. The cation source of the ionomer of ethylene acid copolymer may be a monovalent or divalent cation source, including formate, acetate, hydroxide, nitrate, carbonate, and dicarbonate. In embodiments, the ionomer of ethylene acid copolymer may be treated with one or more cations or cation sources, which may include magnesium, sodium, zinc, or a combination thereof.

[0045] In embodiments, the ethylene content of the ionomer of the ethylene acid copolymer is greater than 50% by weight, or greater than 60% by weight, based on the total weight of the ionomer of the ethylene acid copolymer. For example, the ethylene content of the ionomer of the ethylene acid copolymer can be 50% to 95%, 50% to 90%, 50% to 85%, or 60% to 80% by weight, based on the total weight of the ionomer of the ethylene acid copolymer.

[0046] In embodiments, the ionomer of ethylene acid copolymer has a melt index (I2) of 0.1 g / 10 min to 16 g / 10 min, 0.5 g / 10 min to 15 g / 10 min, 3 g / 10 min to 13 g / 10 min, 3.5 g / 10 min to 10 g / 10 min, or 5 g / 10 min to 8 g / 10 min. Commercially available ionomers of ethylene acid copolymer include those available under the SURLYN™ from The Dow Chemical Company (Midland, MI).

[0047] In embodiments, the polymer of the sealant layer has a maximum peak melting temperature (T m For example, in embodiments, the polymer of the sealant layer may comprise or consist of linear low density polyethylene (LLDPE). Linear low density polyethylene has a viscosity of 0.930 g / cm 3 It may have a density of 0.930 g / cm 3 All individual values ​​and subranges below are included and disclosed herein, for example, the density of linear low density polyethylene is 0.870 g / cm 3 Lower limit: 0.928, 0.925, 0.920, or 0.915 g / cm 3 The upper limit of the saturation temperature is 0.870 to 0.930 g / cm 3 All individual values ​​and subranges are included and disclosed herein.

[0048] Commercially available examples of polyethylenes that can be used in the sealant layer include those sold under the name ELITE™ AT by The Dow Chemical Company, including, for example, ELITE™ AT6202 and ELITE™ AT6410.

[0049] Maximum peak melting temperature (T mIn addition to at least 70% by weight of the polymer having a saturation constant (SCL), the sealant layer may, in embodiments, further comprise at least one additional polymer and / or at least one additive. For example, the at least one additional polymer may be selected from the group of polyethylene, ethylene vinyl acetate, ethylene acrylic acid, or a combination thereof, in an amount less than 30% by weight of the sealant layer. For example, the at least one additive may be selected from the group of antioxidants, UV stabilizers, heat stabilizers, slip agents, antiblock agents, antistatic agents, pigments or colorants, processing aids, crosslinking catalysts, flame retardants, fillers, blowing agents, or a combination thereof, in an amount less than 30% by weight of the sealant layer.

[0050] Multilayer film bonding layer The multilayer film may include a tie layer between the barrier layer and the sealant layer, the tie layer adhering the barrier layer to the sealant layer.

[0051] In embodiments, the tie layer comprises an adhesive resin selected from the group consisting of anhydride-grafted ethylene-based polymers, ethylene acid copolymers, and ethylene vinyl acetate. Examples of anhydride-grafted moieties include maleic anhydride, citraconic anhydride, 2-methylmaleic anhydride, 2-chloromaleic anhydride, 2,3-dimethylmaleic anhydride, bicyclo[2,2,1]-5-heptane-2,3-dicarboxylic anhydride, 4-methyl-4-cyclohexene-1,2-dicarboxylic anhydride, bicyclo(2.2.2)oct-5-ene-2,3-dicarboxylic anhydride, and 10-octahydronaphthalene-2,3-dicarboxylic anhydride. Examples of suitable anhydrides include, but are not limited to, 2-oxa-1,3-diketospiro(4.4)non-7-ene, bicyclo(2.2.1)hept-5-ene-2,3-dicarboxylic anhydride, tetrahydrophthalic anhydride, norborn-5-ene-2,3-dicarboxylic anhydride, nadic anhydride, methylnadic anhydride, himic anhydride, methylhimic anhydride, and x-methyl-bi-cyclo(2.2.1)hept-5-ene-2,3-dicarboxylic anhydride. In one embodiment, the anhydride grafted moiety comprises maleic anhydride.

[0052] In an embodiment, the tie layer comprises an anhydride-modified linear low density polyethylene. In an embodiment, the anhydride-modified linear low density polyethylene has a viscosity of 0.860 g / cm 3 ~0.935g / cm 3 It has a density in the range of 0.860 g / cm 3 ~0.935g / cm 3 All individual values ​​and subranges are disclosed and included herein, for example, an anhydride-modified linear low density polyethylene has a viscosity of 0.875 g / cm 3 ~0.935g / cm 3 , 0.900g / cm 3 ~0.925g / cm 3 , 0.910g / cm 3 ~0.935g / cm 3 , 0.910g / cm 3 ~0.925g / cm 3 , 0.915g / cm 3 ~0.935g / cm 3 , or 0.920 g / cm 3 ~0.930g / cm 3 In embodiments, the anhydride-modified linear low density polyethylene has a melt index (I2) of from 0.1 g / 10 min to 50 g / 10 min, or from 0.5 g / 10 min to 20 g / 10 min, or from 1.0 g / 10 min to 10 g / 10 min.

[0053] In embodiments, the tie layer comprises 0 to 100 weight percent anhydride-modified linear low density polyethylene, based on the total weight of the tie layer. All individual values ​​and subranges between 0 and 100 weight percent are disclosed and included herein. For example, in embodiments, the tie layer may comprise 10 to 90 weight percent, 20 to 80 weight percent, 30 to 70 weight percent, or 40 to 60 weight percent anhydride-modified linear low density polyethylene, based on the total weight of the tie layer.

[0054] Examples of commercially available anhydride-modified linear low density polyethylenes that may be used in embodiments include BYNEL™ series 4100 resins, such as BYNEL™ 41E710 and BYNEL™ 41E687, available from The Dow Chemical Company (Midland, MI).

[0055] In embodiments, the tie layer further comprises at least one of linear low density polyethylene, low density polyethylene, medium density polyethylene, or high density polyethylene. For example, in embodiments, the tie layer may comprise a polyethylene having a viscosity of 0.945 g / cm 3 ~0.970g / cm 3 0.945 g / cm 3 ~0.970g / cm 3 All individual values ​​and subranges of 0.945 g / cm are disclosed and included herein, for example, high density polyethylene has a viscosity of 0.945 g / cm 3 ~0.965g / cm 3 , 0.950g / cm 3 ~0.970g / cm 3 , 0.950g / cm 3 ~0.965g / cm 3 , 0.955g / cm 3 ~0.970g / cm 3 , 0.955g / cm 3 ~0.965g / cm 3 , or 0.955 g / cm 3 ~0.965g / cm 3 The density may range from 0.01 to 0.01.

[0056] In embodiments where high density polyethylene is present, the high density polyethylene of the tie layer is a mixture of ethylene and C3-C 12It may be a copolymer with a comonomer. In embodiments, the tie layer further comprises 0 to 90 wt. % high-density polyethylene, based on the total weight of the tie layer. All individual values ​​and subranges between 0 and 90 wt. % are disclosed and included herein. For example, in embodiments, the tie layer may comprise 10 to 90 wt. %, 20 to 80 wt. %, 30 to 70 wt. %, or 40 to 60 wt. % high-density polyethylene, based on the total weight of the tie layer. In embodiments, the melt index (I2) of the high-density polyethylene may be 0.3 to 10.0 g / 10 min, 0.3 to 7.0 g / 10 min, 0.3 to 5.0 g / 10 min, 0.3 to 4.0 g / 10 min, 0.3 to 3.0 g / 10 min, 0.3 to 2.0 g / 10 min, 0.3 to 1.5 g / 10 min, or 0.5 to 1.0 g / 10 min.

[0057] Commercially available examples of high density polyethylene that can be used in the tie layer include those sold under the names ELITE™ 5960G1 and DOWLEX™ 2006G by The Dow Chemical Company (Midland, MI).

[0058] Second tie layer of multilayer film In embodiments, the multilayer film further comprises a second tie layer between the outer layer and the barrier layer. The second tie layer may adhere the outer layer to the barrier layer.

[0059] In embodiments, the second tie layer comprises an adhesive resin selected from the group consisting of anhydride-grafted ethylene-based polymers, ethylene acid copolymers, and ethylene vinyl acetate. Examples of anhydride-grafted moieties include maleic anhydride, citraconic anhydride, 2-methylmaleic anhydride, 2-chloromaleic anhydride, 2,3-dimethylmaleic anhydride, bicyclo[2,2,1]-5-heptane-2,3-dicarboxylic anhydride, 4-methyl-4-cyclohexene-1,2-dicarboxylic anhydride, bicyclo(2.2.2)oct-5-ene-2,3-dicarboxylic anhydride, and 10-octahydronaphthalene-2,3-dicarboxylic anhydride. Examples of suitable anhydrides include, but are not limited to, 2-oxa-1,3-diketospiro(4.4)non-7-ene, bicyclo(2.2.1)hept-5-ene-2,3-dicarboxylic anhydride, tetrahydrophthalic anhydride, norborn-5-ene-2,3-dicarboxylic anhydride, nadic anhydride, methylnadic anhydride, himic anhydride, methylhimic anhydride, and x-methyl-bi-cyclo(2.2.1)hept-5-ene-2,3-dicarboxylic anhydride. In one embodiment, the anhydride grafted moiety comprises maleic anhydride.

[0060] In an embodiment, the second tie layer comprises an anhydride-modified linear low density polyethylene. In an embodiment, the anhydride-modified linear low density polyethylene has a viscosity of 0.860 g / cm 3 ~0.935g / cm 3 It has a density in the range of 0.860 g / cm 3 ~0.935g / cm 3 All individual values ​​and subranges are disclosed and included herein, for example, an anhydride-modified linear low density polyethylene has a viscosity of 0.875 g / cm 3 ~0.935g / cm 3 , 0.900g / cm 3 ~0.925g / cm 3 , 0.910g / cm 3 ~0.935g / cm 3 , 0.910g / cm 3 ~0.925g / cm 3 , 0.915g / cm 3 ~0.935g / cm3 , or 0.920 g / cm 3 ~0.930g / cm 3 In embodiments, the anhydride-modified linear low density polyethylene has a melt index (I2) of from 0.1 g / 10 min to 50 g / 10 min, or from 0.5 g / 10 min to 20 g / 10 min, or from 1.0 g / 10 min to 10 g / 10 min.

[0061] In embodiments, the second tie layer comprises 0 to 100 weight percent anhydride-modified linear low density polyethylene, based on the total weight of the second tie layer. All individual values ​​and subranges between 0 and 100 weight percent are disclosed and included herein. For example, in embodiments, the second tie layer may comprise 10 to 90 weight percent, 20 to 80 weight percent, 30 to 70 weight percent, or 40 to 60 weight percent anhydride-modified linear low density polyethylene, based on the total weight of the second tie layer.

[0062] Examples of commercially available anhydride-modified linear low density polyethylenes that may be used in embodiments include BYNEL™ series 4100 resins, such as BYNEL™ 41E710 and BYNEL™ 41E687, available from The Dow Chemical Company (Midland, MI).

[0063] In embodiments, the second tie layer further comprises at least one of linear low density polyethylene, low density polyethylene, medium density polyethylene, or high density polyethylene. For example, in embodiments, the second tie layer has a density of 0.945 g / cm 3 ~0.970g / cm 3 0.945 g / cm 3 ~0.970g / cm 3 All individual values ​​and subranges of 0.945 g / cm are disclosed and included herein, for example, the high density polyethylene of the second tie layer is 0.945 g / cm 3 ~0.965g / cm 3 , 0.950g / cm 3 ~0.970g / cm 3 , 0.950g / cm 3~0.965g / cm 3 , 0.955g / cm 3 ~0.970g / cm 3 , 0.955g / cm 3 ~0.965g / cm 3 , or 0.955 g / cm 3 ~0.965g / cm 3 The density may range from 0.01 to 0.01.

[0064] In embodiments where high density polyethylene is present, the high density polyethylene of the second tie layer is a mixture of ethylene and C3-C 12 It may be a copolymer with a comonomer. In embodiments, the second tie layer comprises 0 to 90 weight percent high density polyethylene, based on the total weight of the second tie layer. All individual values ​​and subranges between 0 and 90 weight percent are disclosed and included herein. For example, in embodiments, the second tie layer may comprise 10 to 90 weight percent, 20 to 80 weight percent, 30 to 70 weight percent, or 40 to 60 weight percent high density polyethylene, based on the total weight of the second tie layer. In embodiments, the high density polyethylene of the second tie layer may have a melt index (I2) of 0.3 to 10.0 g / 10 min, 0.3 to 7.0 g / 10 min, 0.3 to 5.0 g / 10 min, 0.3 to 4.0 g / 10 min, 0.3 to 3.0 g / 10 min, 0.3 to 2.0 g / 10 min, or 0.3 to 1.5 g / 10 min, or 0.5 to 1.0 g / 10 min.

[0065] Commercially available examples of high density polyethylene that can be used for the second tie layer include those available under the names ELITE™ 5960G1 and DOWLEX™ 2006G from The Dow Chemical Company (Midland, MI).

[0066] Laminated oriented film The laminate disclosed herein includes an oriented film. The oriented film according to the embodiments disclosed herein is heat laminated to an outer layer of a multilayer film and has a viscosity of 0.900 to 0.970 g / cm. 3 The ethylene-based polymer has a density.

[0067] In an embodiment, the ethylene-based polymer of the oriented film has a viscosity of 0.900 to 0.970 g / cm 3 It has a density of 0.900 to 0.970 g / cm 3 All individual values ​​and subranges are disclosed and included herein. For example, ethylene-based polymers may have a modulus of elasticity of 0.900 to 0.970 g / cm. 3 , 0.910~0.957g / cm 3 , 0.920~0.947g / cm 3 , 0.920~0.937g / cm 3 , 0.920~0.930g / cm 3 , or 0.920 to 0.927 g / cm 3 The density may be

[0068] In embodiments, the ethylene-based polymer has a melt index (I2) from 0.1 g / 10 min to 10 g / 10 min, or from 0.5 g / 10 min to 8 g / 10 min, or from 0.5 g / 10 min to 5 g / 10 min.

[0069] In embodiments, the ethylene-based polymer comprises at least 50 wt% of the oriented film, based on the total weight of the oriented film. All individual values ​​and subranges of at least 50 wt% are disclosed and included herein. For example, the ethylene-based polymer may comprise at least 50 wt%, at least 75 wt%, at least 90 wt%, at least 99 wt%, or at least 99.9 wt% of the oriented film, based on the total weight of the oriented film.

[0070] In addition to the ethylene-based polymer, in embodiments, the oriented film may further comprise at least one additional polymer, which may be selected from the group of ultra-low density polyethylene, low density polyethylene, polyethylene elastomer / plastomer, ethylene vinyl alcohol copolymer (EVOH), ethylene vinyl acetate, ethylene acrylic acid, or combinations thereof, in an amount of less than 50% by weight of the oriented film.

[0071] In embodiments, the oriented film is a machine direction oriented film. In such embodiments, the oriented film may be a machine direction oriented (MDO) polyethylene film. In other embodiments, the oriented film is biaxially oriented. In such embodiments, the oriented film may be a biaxially oriented polyethylene (BOPE) film. In embodiments where the oriented film is BOPE, the BOPE may be biaxially oriented using a tenter frame sequential biaxial orientation process and may be referred to as tenter frame biaxially oriented polyethylene (TF-BOPE). Such techniques are generally known to those skilled in the art. In other embodiments, the oriented film may be biaxially oriented using other techniques known to those skilled in the art, such as a double bubble orientation process, based on the teachings herein. Generally, with a tenter frame sequential biaxial orientation process, the tenter frame is incorporated as part of the extrusion line. After extrusion from the flat die, the film is cooled on a chill roll and immersed in a water bath filled with room temperature water. The cast film is then passed over a series of rollers with different rotational speeds to achieve stretching in the machine direction. The MD stretching segment of the production line has several pairs of rollers, all of which are oil heated. The pairs of rollers operate sequentially as preheating rollers, stretching rollers, and relaxation and annealing rollers. The temperature of each pair of rollers is controlled separately. After stretching in the machine direction, the film web is passed through a tenter frame hot air oven with heating zones to achieve stretching in the transverse direction. The first several zones are for preheating, followed by a stretching zone and then a final zone for annealing.

[0072] The oriented film can be a multilayer film or a monolayer film. For example, in embodiments, the oriented film can be a monolayer TF-BOPE film comprising an ethylene-based polymer. In other embodiments, the oriented film is a multilayer film and comprises at least two layers. For example, in embodiments, the oriented film can be a multilayer TF-BOPE film comprising three layers (e.g., an A / B / C structure TF-BOPE film made by coextrusion of three layers using a single ethylene-based polymer resin). Embodiments of the oriented film can include, for example, a tie layer, a sealant layer, or a barrier layer. In embodiments, the oriented film includes a barrier layer comprising an ethylene-vinyl alcohol copolymer.

[0073] In embodiments, an oriented film has a transverse direction stretch ratio that is greater than its machine direction stretch ratio, and the oriented film has a ratio of machine direction elongation to transverse direction elongation to break of at least 2: 1. In embodiments, the oriented film may exhibit a machine direction elongation to break that is at least 2 times greater, or alternatively at least 5 times greater, or alternatively at least 8 times greater, or alternatively at least 10 times greater than the transverse direction elongation to break, as measured according to ASTM D882.

[0074] In embodiments, the oriented film is oriented in the machine direction and / or the cross direction. In embodiments, the oriented film may be oriented in the machine direction with a stretch ratio of 2:1 to 6:1, or alternatively with a stretch ratio of 3:1 to 5:1. In embodiments, the oriented film may be oriented in the cross direction with a stretch ratio of 2:1 to 9:1, or alternatively with a stretch ratio of 3:1 to 8:1.

[0075] In embodiments, for example, depending on the end use application, the oriented film may be corona treated or printed using techniques known to those skilled in the art, either before or after lamination to the multilayer film.

[0076] The multilayer and oriented films disclosed herein can have a variety of thicknesses, depending, for example, on the number of layers. For example, in embodiments, the multilayer or oriented film can have a thickness of 10 to 200 microns, or alternatively, 15 to 100 microns.

[0077] additives It should be understood that any of the foregoing layers of the multilayer film or oriented film may further comprise one or more additives known to those skilled in the art, such as, for example, antioxidants, UV stabilizers, heat stabilizers, slip agents, antiblock agents, antistatic agents, pigments or colorants, processing aids, crosslinking catalysts, flame retardants, fillers, and blowing agents. For example, in embodiments, the sealant layer of the multilayer film comprises at least one of a slip agent or an antiblock agent.

[0078] Laminate As described above, the oriented film is heat laminated to the outer layer of the multilayer film, the combination of the multilayer film and the oriented film providing a laminate.

[0079] The laminates of the present invention may have several desirable properties. For example, the laminates of the present invention may have one or more of the following properties: a bond strength of at least 2.00 N / 25 mm; 3 / day / m 2 OTR less than 5.75 g / day / m 2 a WVTR of less than 1.20 N, a heat seal initiation temperature at 5 N less than 115°C, a seal strength at 120°C of at least 4.0 N / 25 mm, a hot tack initiation at 1 N less than 95°C, a hot tack strength at 110°C of at least 1.20 N, and zero percent (0%) shrinkage at temperatures ranging from 70°C to 110°C.

[0080] In embodiments, laminates of the present invention may exhibit a bond strength of at least at least 2.00 N / 25 mm, or alternatively at least 3.50 N / 25 mm, or alternatively at least 5.00 N / 25 mm, or alternatively at least 5.50 N / 25 mm, or alternatively at least 6.50 N / 25 mm, or alternatively at least 7.00 N / 25 mm, or alternatively at least 7.50 N / 25 mm, which bond strength may be measured according to the test methods described below.

[0081] In an embodiment, the laminate of the present invention is 5.25 cm 3 / day / m 2 Less than, or alternatively 4.00 cm 3 / day / m 2 Less than, or alternatively 3.00 cm 3 / day / m 2 Less than, or alternatively 2.50 cm 3 / day / m 2 The OTR may be less than 100%, which may be measured according to the test method described below.

[0082] In an embodiment, the laminate of the present invention has a saturation of 5.75 g / day / m 2 Less than, or alternatively 5.00 g / day / m 2 Less than, or alternatively 4.75 g / day / m 2 The WVTR may be less than 100%, which may be measured according to the test method described below.

[0083] In embodiments, laminates of the present invention may exhibit a heat seal initiation temperature at 5N of less than 115°C, or alternatively less than 110°C, or alternatively less than 105°C, or alternatively less than 95°C, or alternatively less than 85°C, or alternatively less than 75°C, where heat seal initiation at 5N may be measured according to the test method described below.

[0084] In embodiments, laminates of the present invention may exhibit a seal strength at 120°C of at least 4.0 N / 25mm, or alternatively at least 10.0 N / 25mm, or alternatively at least 30.0 N / 25mm, or alternatively at least 50.0 N / 25mm, or alternatively at least 55.0 N / 25mm, which seal strength at 120°C may be measured according to the test method described below.

[0085] In embodiments, laminates of the present invention may exhibit a hot tack initiation at 1 Newton of less than 95°C, or alternatively less than 80°C, or alternatively less than 78°C, or alternatively less than 76°C, or alternatively less than 72°C, which hot tack initiation at 1 Newton may be measured according to the test method described below.

[0086] In embodiments, laminates of the present invention may exhibit a hot tack strength at 110°C of at least 1.20 N, or alternatively at least 1.60 N, or alternatively at least 1.80 N, or alternatively at least 4.00 N, or alternatively at least 5.00 N, which may be measured according to the test method described below.

[0087] In embodiments, the laminates of the present invention may exhibit zero percent (0%) shrinkage at 70°C, 80°C, 90°C, 100°C, and 110°C, where shrinkage is measured according to the test method described below, and may provide a seal window of 45°C or less, or alternatively, 40°C or less, or alternatively, 35°C or less.

[0088] In embodiments, the laminate of the present invention comprises at least 90% by weight polyethylene, or at least 95% by weight polyethylene, or at least 99% by weight polyethylene, or at least 99.5% by weight polyethylene, or at least 99.9% by weight polyethylene, based on the total weight of the laminate.

[0089] In embodiments, the laminate of the present invention does not include an adhesive (eg, a solvent-based or water-based adhesive).

[0090] Goods Embodiments of the present invention also provide articles formed from the laminates described herein. Examples of such articles may include packaging, flexible packaging, pouches, and sachets. In embodiments, the packaging of the present invention may contain liquids, powders, food, or other items. Articles and packaging of the present invention may be formed from the laminates disclosed herein using techniques known to those skilled in the art in view of the teachings herein.

[0091] Test Method density Density was measured according to ASTM D792 and is in grams / cm 3 (g / cm 3 )

[0092] Melt Index (I2) Melt index (I2) is measured according to ASTM D-1238 at 2.16 kg at 190° C. Values ​​are reported in g / 10 min, which corresponds to grams dissolved per 10 minutes.

[0093] Oxygen transmission rate (OTR) Oxygen transmission rate (OTR) is measured according to ASTM D3985 using a Mocon Ox-Tran 2 / 21. Samples are dried at 23°C with 100% O2 gas, 0% RH, and 50 cm 2 Test with a sample size of 1000. Values ​​are expressed in cm 3 / day / m 2 Report at.

[0094] Water Vapor Transmission Rate (WVTR) Water vapor transmission rate (WVTR) is measured according to ASTM F1249 using Mocon Permatran-W3 / 34 and 3 / 60. Samples are heated at 37.8°C, 100% RH, 50 cm 2 Test with a sample size of g / day / m 2 Report at.

[0095] Hot tack initiation and hot tack strength Hot tack test was performed with a seal width of 25 mm, a dwell seal time of 0.5 seconds, and a 0.275 N / mm 2(40 psi) seal pressure, and a hot tack pull speed of 200 mm / sec using a J&B Hot Tack Tester 4000. Hot tack initiation is reported as the minimum temperature in degrees Celsius to reach 1 Newton force. Hot tack strength is measured in units of Newtons per 25 mm (N / 25 mm).

[0096] Heat seal initiation temperature and seal strength To determine the heat seal initiation temperature (HSIT) and seal strength, the samples are sealed by a J&B Hot Tack 4000 tester. The sample width is 25 mm, the dwell seal time is 0.5 seconds, and the seal pressure is 0.275 N / mm. 2 The heat-sealed samples are conditioned for 24 hours and then measured using a Zwick tensile machine equipped with a 200 N load cell and a pull rate of 500 mm / min. The HSIT is reported as the minimum temperature in degrees Celsius to reach 5 Newton force. Seal strength values ​​are reported in N / 25 mm.

[0097] Contraction Shrinkage (%) is obtained by measuring the length and width of the sealed area in both the machine direction (MD) and the transverse or transverse direction (TD) after the films have been heat sealed together, and calculating the percentage change compared to the width of the sealing bar, which can be 1 mm to 15 mm. Standard heat sealing machines, including PULSA impulse sealers or J&B hot tack testers, can be used, provided the machine has an accurate and adjustable temperature controller. Sealing conditions are jaw pressure (40-80 psi or 0.275-0.552 N / mm). 2 ), dwell time (0.1-1.5 seconds), and seal temperature (60-150°C) window, depending on the packaging speed; typical conditions for high speed packaging machines are 40 psi (0.275 N / mm 2 ) jaw pressure and a dwell time of 0.5 seconds.

[0098] Bonding strength Bond strength is measured using a Zwick tensile tester with a pulling speed of 250 mm / min and a 25 mm wide strip. The tensile tester is equipped with a gripper fixture (which holds the sample in a T-shape) to hold both ends of a partially delaminated or partially peeled sample and then pull it apart. The upper gripper, which is connected to a crosshead, is driven in the pulling direction to measure the force or bond strength required between two adjacent layers of a multilayer sample. Maximum and average force results are calculated from five measurements and are reported in Newtons (N / 25 mm strip).

[0099] Maximum peak melting temperature (Tm) Differential scanning calorimetry (DSC) is used to measure the melting and crystallization behavior of polymers over a wide temperature range. For example, a TA Instruments Q1000 DSC equipped with a refrigerated cooling system (RCS) and an autosampler is used to perform this analysis. The instrument is first calibrated using the software calibration wizard. A baseline is obtained by heating the cell from -80°C to 280°C without any sample in the aluminum DSC pan. A sapphire standard is then used, as instructed by the calibration wizard. Next, 1-2 milligrams (mg) of fresh indium sample is analyzed by heating the standard sample to 180°C, cooling it to 120°C at a cooling rate of 10°C / min, and then holding the standard sample isothermal at 120°C for 1 minute. The standard sample is then heated from 120°C to 180°C at a heating rate of 10°C / min. The indium standard sample is then measured to determine its heat of fusion (H). f )=28.71±0.50 Joules per gram (J / g), and onset of melting=156.6° C.±0.5° C. The test sample is then analyzed on a DSC instrument.

[0100] A nitrogen purge gas flow rate of 50 ml / min is used during testing. Each sample is melt-pressed into a thin film at approximately 175°C, after which the molten sample is air-cooled to room temperature (approximately 25°C). Film samples are formed by pressing a 0.1-0.2 gram sample at 175°C, 1,500 psi, and 30 seconds to form a 0.1-0.2 mil thick film. A 3-10 mg, 6 mm diameter specimen is extracted from the cooled polymer, weighed, placed in a light (approximately 50 mg) aluminum pan, and crimped shut. Analysis is then performed to determine its thermal properties.

[0101] The thermal behavior of the sample is determined by raising and lowering the sample temperature to generate a heat flow versus temperature profile. First, the sample is rapidly heated to 180°C and held isothermal for 5 minutes to remove the thermal history. Next, the sample is cooled to -40°C at a cooling rate of 10°C / min and held isothermal at -40°C for 5 minutes. The sample is then heated to 150°C at a heating rate of 10°C / min (this is the "second heating" ramp). A cooling curve and a second heating curve are recorded. The cooling curve is analyzed by setting a baseline endpoint from the onset of crystallization to -20°C. The heating curve is analyzed by setting a baseline endpoint from -20°C to the end of melting. The determined value is the maximum peak melting temperature (T m ), maximum peak crystallization temperature (T c ), onset crystallization temperature (Tc onset), heat of fusion (H f ) (Joules / gram), and the % crystallinity of the polyethylene sample calculated using % crystallinity of PE = ((Hf) / (292 J / g)) x 100, and the % crystallinity of the polypropylene sample calculated using % crystallinity of PP = ((Hf) / 165 J / g)) x 100. f ) and maximum peak melting temperature are reported from the second heat curve. Maximum peak crystallization temperature and onset crystallization temperature are determined from the cooling curve. [Example]

[0102] The following examples illustrate features of the present disclosure and are not intended to limit the scope of the disclosure.

[0103] Polymers / films used The example laminates discussed below contained the following materials:

[0104] ELITE(TM) 5960G1, 0.962g / cm 3 and a melt index (I2) of 0.85 g / 10 min, commercially available from The Dow Chemical Company (Midland, MI).

[0105] DOW (trademark) LDPE450E, 0.923g / cm 3 and a melt index (I2) of 2.0 g / 10 min, commercially available from The Dow Chemical Company (Midland, MI).

[0106] BYNEL(trademark)22E780, 0.94g / cm 3 and a melt index (I2) of 2 g / 10 min, commercially available from The Dow Chemical Company (Midland, MI).

[0107] ELVAX™ 470, 18% by weight vinyl acetate comonomer content, 0.941 g / cm 3 and a melt index (I2) of 0.7 g / 10 min, commercially available from The Dow Chemical Company (Midland, MI).

[0108] BYNEL(TM)41E710, 0.922g / cm 3 and a melt index (I2) of 2.7 g / 10 min, and is commercially available from The Dow Chemical Company (Midland, MI).

[0109] EVAL(trademark) H171B, 1.17g / cm 3 and a melt index (I2) of 1.7 g / 10 min, and is commercially available from Kuraray Co., Ltd. (Tokyo, Japan).

[0110] SURLYN™ 1707, with a maximum peak melting temperature (T m ), 0.95g / cm 3 and a melt index (I2) of 0.9 g / 10 min, and is commercially available from The Dow Chemical Company (Midland, MI).

[0111] AFFINITY™ PF7266, with a maximum peak melting temperature (T m ), 0.885g / cm 3 and a melt index (I2) of 2.5 g / 10 min, commercially available from The Dow Chemical Company (Midland, MI).

[0112] ADCOTE™ 545S / Co-reactant F, a solvent-based two-component polyurethane adhesive commercially available from The Dow Chemical Company (Midland, MI).

[0113] POLYBATCH® CE505, a slip masterbatch commercially available from Lyondell Basell (Houston, TX).

[0114] POLYBATCH® AB5, an anti-blocking masterbatch commercially available from Lyondell Basell (Houston, TX).

[0115] CONPOL™ 13B, an anti-blocking masterbatch commercially available from The Dow Chemical Company (Midland, MI).

[0116] CONPOL™ 20S1, a slip masterbatch commercially available from The Dow Chemical Company (Midland, MI).

[0117] TF-BOPE film, a linear low density polyethylene, biaxially oriented film stretched to a thickness of 20 microns in a tenter frame at a stretch ratio of 3 to 5X in the machine direction and 7 to 9X in the transverse direction. The linear low density polyethylene has a density of 0.926 g / cm. 3 and a melt index (I2) of 1.7 g / 10 min and is commercially available from The Dow Chemical Company, Midland, MI under the name INNATE™ XUS 59910.08.

[0118] BOPP film, a printed biaxially oriented propylene film processed at 36 dynes and having a gauge of 18 microns.

[0119] Laminates designated as Inventive Examples 1-5 and Comparative Examples 1-2 were formed using a print-ABCBD construction, where "print" corresponds to the TF-BOPE film of the inventive examples and the BOPP film of the comparative examples (oriented film), and "ABCBD" corresponds to the five-layer coextruded film (multilayer film). For each of the inventive examples, the TF-BOPE film was heat-laminated to the five-layer multilayer film using a hot roll lamination process on a ChemInstruments #007416 at a temperature of 160°C, a pressure of 60 psi, and a speed of 0.75 m / min. The examples were conditioned and cured for 24 hours. For each of the comparative examples, the BOPP film was laminated to the five-layer multilayer film using ADCOTE™ 545S / Co-Reactant F applied at a coating weight of 3-3.5 gsm. The examples are cured at room temperature (25°C) for 2 days and the hot roll lamination process is carried out on a ChemInstruments #007416 at a temperature of 75°C, a pressure of 60 psi, and a speed of 1.66 m / min.

[0120] Each of the five-layer, multilayer coextruded films of the inventive and comparative examples was formed on a Collin five-layer blown coextrusion line with the following parameters: target film thickness: 55 μm; extruders: 4 extruders; layer configuration: A / B / C / B / D; layer ratio (%): 18.2% / 13.6% / 18.2% / 13.6% / 36.4% (or 2 / 1.5 / 2 / 1.5 / 4); layer thickness (μm): 10 / 7.5 / 10 / 7.5 / 20; die diameter (mm): 50; blow-up ratio (BUR): 3.0; layflat width: 235 mm; total throughput of 8 kg / hr; line speed of 5.4 m / min; melt temperatures (°C) of 163-174°C, 191°C, 195°C, and 175-185°C for extruders A, B, C, and D, respectively.

[0121] Table 1 below provides the structures and compositions of laminate examples, inventive examples 1-5, and comparative examples 1-2.

[0122] [Table 1] * In addition to 80% AFFINITY™ PF7266, Layer D contains 10% POLYBATCH® CE505 and 10% POLYBATCH® AB5. ** In addition to 93.5% SURLYN™ 1707, Layer D contains 4% CONPOL™ 13B and 2.5% CONPOL™ 20S1.

[0123] The thickness, oxygen transmission rate (OTR), water vapor transmission rate (WVTR), and bond strength of the examples were measured. Table 2 provides the results. As shown in Table 2, the bond strength of the inventive examples is surprisingly high compared to that of the comparative examples. The inventive examples do not have delamination between the multilayer film and the oriented film, despite the absence of a laminating adhesive in the laminate. The comparative examples in some aspects exhibit lower OTR and WVTR values, but the comparative examples are not compatible with polyethylene recycle streams. Those skilled in the art will also understand that the OTR of the laminate can be adjusted depending on the thickness of the barrier layer and the ethylene content of the EVOH in the barrier layer (i.e., generally, the thicker the barrier layer or the lower the ethylene content, the lower the achievable OTR value). As noted above, the inventive examples are non-limiting examples not intended to limit the scope of the present disclosure, and multilayer films according to embodiments of the present invention may include a barrier layer containing EVOH having an ethylene content of 20 to 50 mol%.

[0124] [Table 2] * The comparative BOPP film is a printed BOPP that is printed ink side laminated to a five layer film using a solvent based laminating adhesive, so the bond strength is measured along the printed ink side of the BOPP to the five layer film.

[0125] The heat seal initiation temperature (HSIT), heat seal strength, hot tack initiation temperature at 1 Newton, and hot tack strength were measured. Figure 1 shows the heat seal strength curves for Comparative Example 1 and Inventive Examples 1-3. Figure 2 shows the hot tack strength curves for Comparative Example 2 and Inventive Examples 4-5. Table 3 provides the results for Comparative Example 1 and Inventive Examples 1-3, in which AFFINITY™ PF7266 is part of sealant layer / layer D. From the data in Table 3, the inventive examples have lower HSIT and higher seal strength in some embodiments. Table 4 provides the results for Comparative Example 2 and Inventive Examples 4-5, in which SURLYN™ 1707 is part of sealant layer / layer D. From the data in Table 4, the inventive examples demonstrate higher or desirable hot tack strength. From Tables 3 and 4, the inventive examples demonstrate desirable or maintained low hot tack initiation temperatures and low HSIT. The inventive examples also achieve desirable, maintained, or improved seal strength performance in some embodiments.

[0126] [Table 3]

[0127] [Table 4]

[0128] The shrinkage (%) of the examples is measured at 70°C, 80°C, 90°C, 100°C, 110°C, and 120°C. None of the examples show shrinkage in the machine direction (MD) or the transverse or transverse direction (TD) at 70°C, 80°C, 90°C, 100°C, or 110°C. The shrinkage (%) results for the examples are reported in Table 5. While the inventive examples show some shrinkage at 120°C compared to the comparative examples, the inventive examples can perform equal or similar to the comparative examples in the lower temperature range of about 70°C to 110°C, which provides a wider sealing window of at least 40°C.

[0129] [Table 5] * Seal bar dimensions: 0.5cm (MD direction) x 2.5cm (TD direction).

[0130] All documents cited herein, including any cross-referenced or related patents or applications, if any, and any patent application or patent to which this application claims priority or benefit, are incorporated herein by reference in their entirety, unless expressly excluded or otherwise limited. The citation of any document is not an admission that it is prior art with respect to any invention disclosed or claimed herein, or that it teaches, suggests, or discloses such invention, either alone or in any combination with any other reference. Furthermore, to the extent that the meaning or definition of any term in this document conflicts with any meaning or definition of the same term in a document incorporated by reference, the meaning or definition assigned to that term in this document shall govern.

[0131] While particular embodiments of the present invention have been illustrated and described, it would be obvious to those skilled in the art that various other changes and modifications can be made without departing from the spirit and scope of the invention. Therefore, it is intended in the appended claims to cover all such changes and modifications that are within the scope of this invention. The present application also relates to the following aspects: [Claim 1] A laminate, (a) (1) an outer layer comprising at least one of an anhydride-modified ethylene acrylate copolymer, an anhydride-modified polyethylene, an anhydride-modified ethylene vinyl acetate, an ethylene-vinyl acetate copolymer, a polyethylene / vinyl acetate copolymer, a polyethylene / acrylic acid ethylene copolymer, a polyethylene / acrylate copolymer, or a polyethylene elastomer / plastomer; (2) a barrier layer comprising an ethylene vinyl alcohol copolymer; (3) a sealant layer, the sealant layer comprising at least 70% by weight of a polymer having a maximum peak melting temperature (Tm) of 108°C or less; (4) a tie layer between the barrier layer and the sealant layer; and (b) an oriented film heat-laminated to the outer layer of the multilayer film, the oriented film comprising an ethylene-based polymer having a density of 0.900 to 0.970 g / cm3. [Claim 2] The laminate of claim 1 , wherein the multilayer film further comprises a second tie layer between the outer layer and the barrier layer. [Claim 3] 3. The laminate according to claim 1, wherein the barrier layer has a thickness of 5 to 25% of the total thickness of the multilayer film. [Claim 4] 4. The laminate of claim 1, wherein the sealant layer is at least 10 microns thick. [Claim 5] 5. The laminate according to claim 1, wherein the sealant layer occupies 25 to 60% of the total thickness of the multilayer film. [Claim 6] 6. The laminate according to claim 1, wherein the oriented film comprises a barrier layer comprising an ethylene vinyl alcohol copolymer. [Claim 7] 7. The laminate according to claim 1, wherein the oriented film is a machine direction oriented film. [Claim 8] 7. The laminate according to claim 1, wherein the oriented film is a biaxially oriented film. [Claim 9] 9. The laminate according to claim 1, wherein the sealant layer comprises a polyethylene elastomer / plastomer. [Claim 10] 10. The laminate of claim 1, wherein the sealant layer comprises an ionomer of an ethylene acid copolymer. [Claim 11] 11. The laminate according to claim 1, wherein the outer layer further comprises at least one of linear low-density polyethylene, low-density polyethylene, medium-density polyethylene, or high-density polyethylene. [Claim 12] 12. The laminate of claim 1, wherein the tie layer comprises an anhydride-modified linear low-density polyethylene and at least one of linear low-density polyethylene, low-density polyethylene, medium-density polyethylene, or high-density polyethylene.

Claims

1. A laminate, (a) (1) an outer layer comprising at least one of an anhydride-modified ethylene acrylate copolymer, an anhydride-modified polyethylene, an anhydride-modified ethylene vinyl acetate, an ethylene-vinyl acetate copolymer, a polyethylene / vinyl acetate copolymer, a polyethylene / acrylic acid ethylene copolymer, a polyethylene / acrylate copolymer, or a polyethylene elastomer / plastomer; (2) a barrier layer comprising an ethylene vinyl alcohol copolymer; and (3) A sealant layer, wherein the sealant layer comprises at least 70% by weight of a polymer having a maximum peak melting temperature (T ｍ a sealant layer comprising a polymer having (4) a tie layer between the barrier layer and the sealant layer; and (b) heat-laminated to the outer layer of the multilayer film, ３ and an oriented film comprising an ethylene-based polymer having a density of the laminate exhibits zero percent (0%) shrinkage at temperatures ranging from 70°C to 110°C; Laminate.

2. The laminate of claim 1 , wherein the multilayer film further comprises a second tie layer between the outer layer and the barrier layer.

3. 3. The laminate of claim 1, wherein the barrier layer is 5 to 25% of the total thickness of the multilayer film.

4. The laminate of any one of claims 1 to 3, wherein the sealant layer is at least 10 microns thick.

5. The laminate of any one of claims 1 to 4, wherein the sealant layer is 25 to 60% of the total thickness of the multilayer film.

6. The laminate of any one of claims 1 to 5, wherein the oriented film comprises a barrier layer comprising an ethylene vinyl alcohol copolymer.

7. The laminate of any one of claims 1 to 6, wherein the oriented film is a machine direction oriented film.

8. The laminate according to any one of claims 1 to 6, wherein the oriented film is a biaxially oriented film.

9. The laminate of any one of claims 1 to 8, wherein the sealant layer comprises a polyethylene elastomer / plastomer.

10. The laminate of any one of claims 1 to 9, wherein the sealant layer comprises an ionomer of an ethylene acid copolymer.

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