WO2022105198A1 - 改性聚烯烃复合膜组合物和改性聚烯烃复合膜及其制备方法和应用 - Google Patents

改性聚烯烃复合膜组合物和改性聚烯烃复合膜及其制备方法和应用 Download PDF

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Publication number
WO2022105198A1
WO2022105198A1 PCT/CN2021/098847 CN2021098847W WO2022105198A1 WO 2022105198 A1 WO2022105198 A1 WO 2022105198A1 CN 2021098847 W CN2021098847 W CN 2021098847W WO 2022105198 A1 WO2022105198 A1 WO 2022105198A1
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Prior art keywords
layer
film
polyethylene
composite film
glue
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PCT/CN2021/098847
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English (en)
French (fr)
Inventor
韦丽明
黎倬辰
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上海若祎新材料科技有限公司
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Publication of WO2022105198A1 publication Critical patent/WO2022105198A1/zh

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00—Layered products comprising a layer of synthetic resin
    • B32B27/32—Layered products comprising a layer of synthetic resin comprising polyolefins
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00—Layered products comprising a layer of synthetic resin
    • B32B27/06—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B27/08—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00—Layered products comprising a layer of synthetic resin
    • B32B27/30—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers
    • B32B27/306—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers comprising vinyl acetate or vinyl alcohol (co)polymers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B33/00—Layered products characterised by particular properties or particular surface features, e.g. particular surface coatings; Layered products designed for particular purposes not covered by another single class
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B37/00—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding
    • B32B37/12—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by using adhesives
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B7/00—Layered products characterised by the relation between layers; Layered products characterised by the relative orientation of features between layers, or by the relative values of a measurable parameter between layers, i.e. products comprising layers having different physical, chemical or physicochemical properties; Layered products characterised by the interconnection of layers
    • B32B7/04—Interconnection of layers
    • B32B7/12—Interconnection of layers using interposed adhesives or interposed materials with bonding properties
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
    • B65D65/00—Wrappers or flexible covers; Packaging materials of special type or form
    • B65D65/38—Packaging materials of special type or form
    • B65D65/40—Applications of laminates for particular packaging purposes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
    • B65D85/00—Containers, packaging elements or packages, specially adapted for particular articles or materials
    • B65D85/70—Containers, packaging elements or packages, specially adapted for particular articles or materials for materials not otherwise provided for
    • B65D85/72—Containers, packaging elements or packages, specially adapted for particular articles or materials for materials not otherwise provided for for edible or potable liquids, semiliquids, or plastic or pasty materials
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2307/00—Properties of the layers or laminate
    • B32B2307/70—Other properties
    • B32B2307/724—Permeability to gases, adsorption
    • B32B2307/7242—Non-permeable
    • B32B2307/7244—Oxygen barrier
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2307/00—Properties of the layers or laminate
    • B32B2307/70—Other properties
    • B32B2307/724—Permeability to gases, adsorption
    • B32B2307/7242—Non-permeable
    • B32B2307/7246—Water vapor barrier
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2307/00—Properties of the layers or laminate
    • B32B2307/70—Other properties
    • B32B2307/726—Permeability to liquids, absorption
    • B32B2307/7265—Non-permeable
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2439/00—Containers; Receptacles
    • B32B2439/70—Food packaging
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2439/00—Containers; Receptacles
    • B32B2439/80—Medical packaging
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2535/00—Medical equipment, e.g. bandage, prostheses or catheter
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/50—Reuse, recycling or recovery technologies
    • Y02W30/80—Packaging reuse or recycling, e.g. of multilayer packaging

Definitions

  • the invention relates to the technical field of composite packaging processing, in particular to a modified polyolefin composite film composition and a modified polyolefin composite film and a preparation method and application thereof.
  • the single-product composite packaging structure of liquid milk is: BOPA film//glue//PET aluminized film//glue//blown PE film; nuts composite packaging structure: BOPP film//glue//paper//glue/ /BOPET Aluminized Film//Glue//Blown PE Film.
  • Packaging is an indispensable material for product protection.
  • the demand and output of packaging are increasing.
  • Land burial of waste packaging materials will cause soil barrenness and deterioration, and crop yields will be reduced or eliminated; incineration of waste plastics will produce a large amount of toxic gases such as CO 2 , CO and residual heavy metals in ash, aggravating environmental pollution and the greenhouse effect; a large number of studies have found that marine organisms Life is being endangered by discarded packaging materials. Recycling has a long way to go.
  • modified polyolefin composite film composition and modified polyolefin composite film that have high barrier properties, are easy to recycle and can be recycled for thermoplastic processing after the packaging is discarded.
  • the purpose of the present invention is to overcome the problem that the composite packaging materials in the prior art are not easy to be recycled and reused, the problems of poor puncture resistance, moisture resistance, air resistance and oxygen resistance of the composite packaging materials, and the composite packaging materials.
  • a modified polyolefin composite film composition and a modified polyolefin composite film and a preparation method and application thereof are provided.
  • the composite film has excellent barrier properties, excellent puncture resistance, excellent pressure resistance and excellent drop resistance, and the composite film is mainly made of polyolefin, which has the advantage of being fully recycled.
  • the first aspect of the present invention provides a modified polyolefin composite film composition, wherein the composition includes a first layer of film material, an intermediate layer of film material and a third layer of film material, and the third layer of film material.
  • Layer film materials include PE corona layer material, barrier layer film material and PE heat sealing layer material;
  • the first layer of film material and the intermediate layer of film material each include one or more of C4-C8 polyethylene, one-component homopolypropylene, two-component copolymerized polypropylene and terpolymerized polypropylene ; and the barrier layer film material contains ethylene-vinyl alcohol copolymer and/or thermoplastic polyvinyl alcohol.
  • the second aspect of the present invention provides a barrier polyolefin composite film prepared from the aforementioned composition, wherein the composite film comprises a first layer film 810, an intermediate layer film 830 and a third layer film that are stacked in sequence 850, and the first layer film 810 is obtained by extruding the first material containing the first layer film material; the intermediate layer film 830 is obtained by extruding the second material containing the intermediate layer film material;
  • the third layer film 850 includes a PE corona layer 610, a thermoplastic barrier layer 950 and a PE heat sealing layer 611 stacked in sequence; and the PE corona layer 610 is extruded from a third material containing a PE corona layer material
  • the thermoplastic barrier layer 950 is obtained by extruding the fourth material containing thermoplastic ethylene-vinyl alcohol copolymer and/or thermoplastic polyvinyl alcohol;
  • the PE heat-sealing layer 611 is obtained by extruding the fifth material containing the PE heat-sealing layer material. The material is extruded.
  • a third aspect of the present invention provides a preparation method of the aforementioned composite membrane, wherein the preparation method comprises:
  • the third material is used to prepare the PE corona layer 610
  • the fourth material is used to prepare the thermoplastic barrier layer 950
  • the fifth material is used to prepare the PE heat sealing layer 611
  • the PE corona layer 610, the thermoplastic barrier layer 950 and the The PE heat-sealing layer 611 is sequentially bonded by the first polymer adhesive layer 210 and the second polymer adhesive layer 220 to prepare a third film 850;
  • the first layer film 810, the intermediate layer film 830 and the third layer film 850 are sequentially bonded through the first glue layer 821 and the second glue layer 822 to prepare a modified polyolefin composite film.
  • a fourth aspect of the present invention provides an application of the aforementioned composite film in one or more of food packaging, industrial products, packaging of daily chemical products, and medicines and medical devices.
  • the modified polyolefin composite film of the present invention has excellent barrier properties, excellent puncture resistance, excellent pressure resistance and excellent drop resistance; in addition, it conforms to the trend of environmental protection, and its function and appearance meet the market demand, and it has significant Social Significance.
  • Fig. 1 is the structural representation of the modified polyolefin composite membrane of the present invention
  • Fig. 2 is the structural representation of the third layer film 850 in the modified polyolefin composite film of the present invention.
  • FIG. 3 is a schematic flow chart of a finished product prepared by using the modified polyolefin composite film of the present invention.
  • the present invention provides a modified polyolefin composite film composition, wherein the composition includes a first layer of film material, an intermediate layer of film material and a third layer of film material, and the The third layer of film material includes PE corona layer material, barrier layer film material and PE heat sealing layer material;
  • the first layer of film material and the intermediate layer of film material each comprise one or more of C4-C8 polyethylene, one-component homopolypropylene, two-component copolymerized polypropylene and terpolymerized polypropylene ; and the barrier layer film material contains ethylene-vinyl alcohol copolymer and/or thermoplastic polyvinyl alcohol.
  • the inventors of the present invention have found through a large number of scientific experiments that the use of the barrier layer film material containing ethylene-vinyl alcohol copolymer and/or thermoplastic polyvinyl alcohol in the production process of the multi-layer co-extruded polyolefin composite film has high Barrier and degradable properties, under suitable ratio and extrusion process conditions, the formed high-barrier layer has excellent gas and oxygen barrier properties, and the polyolefin composite film can maintain good transparency and moisture resistance. Waterborne.
  • the monobasic homopolymeric polypropylene is generally also referred to as homopolymeric polypropylene.
  • the monobasic homopolymeric polypropylene is a homopolymeric polypropylene with an isotacticity greater than 95%.
  • the binary copolymer polypropylene is ethylene propylene copolymer polypropylene and/or ethylene butene copolymer polypropylene.
  • Terpolymer polypropylene is ethylene propylene butene copolymer polypropylene and/or ethylene propylene hexene copolymer polypropylene.
  • the film material for the barrier layer contains thermoplastic polyvinyl alcohol (TPVA), wherein the melt flow rate of the thermoplastic polyvinyl alcohol at 210° C. under a load of 2.16 kg is 2.0-5.0 g/ 10min, the density is 0.92-1.30g/cm 3 ; preferably, the melt flow rate of the thermoplastic polyvinyl alcohol at 210°C under a load of 2.16kg is 2.5-4.0g/10min, and the density is 1.0-1.28g/cm 3 ; More preferably, the thermoplastic polyvinyl alcohol has a melt flow rate of 2.7-2.9 g/10min and a density of 1.05-1.15 g/cm 3 at 210° C. under a load of 2.16 kg.
  • TPVA thermoplastic polyvinyl alcohol
  • thermoplastic polyvinyl alcohol and the ethylene-vinyl alcohol copolymer can be obtained commercially, for example, they can be purchased from Sinopec, the models are TPVA-1 and EVOH-1, respectively.
  • the PE corona layer material contains a first medium density linear polyethylene (MLDPE) and a first anti-blocking masterbatch; preferably, based on the total weight of the PE corona layer material, the first The content of a medium density linear polyethylene is 80.0-99.5% by weight, and the content of the first anti-blocking masterbatch is 0.5-20% by weight; more preferably, based on the total weight of the PE corona layer material, The content of the first medium density linear polyethylene is 90-98% by weight, and the content of the first anti-blocking masterbatch is 2-10% by weight; more preferably, the total content of the PE corona layer material is 90-98% by weight. On a weight basis, the content of the first medium density linear polyethylene is 95-97% by weight, and the content of the first anti-blocking masterbatch is 3-5% by weight.
  • MLDPE medium density linear polyethylene
  • the PE heat-sealing layer material contains a second medium density linear polyethylene (MLDPE), a metallocene catalyzed polyethylene (m-LLDPE), a high pressure polyethylene (LDPE), a second anti-blocking masterbatch and a macromolecule
  • MLDPE medium density linear polyethylene
  • m-LLDPE metallocene catalyzed polyethylene
  • LDPE high pressure polyethylene
  • a second anti-blocking masterbatch a macromolecule
  • One or more of the slippery masterbatches preferably, based on the total weight of the PE heat-sealing layer material, the content of the second medium density linear polyethylene is 10.0-58.5% by weight, and the The content of metal-catalyzed polyethylene is 20-30% by weight, the content of the high-pressure polyethylene is 20-40% by weight, the content of the second anti-blocking masterbatch is 0.5-10% by weight, and the polymer is smooth The content of the masterbatch is 1.0-10% by weight.
  • the content of the second medium density linear polyethylene is 25-40% by weight, and the content of the metallocene-catalyzed polyethylene is 25-29% by weight.
  • the content of the high pressure polyethylene is 25-30% by weight
  • the content of the second anti-blocking masterbatch is 5-8% by weight
  • the content of the polymer slippery masterbatch is 5-8% by weight.
  • the metallocene-catalyzed polyethylene is C6-C8 metallocene-catalyzed polyethylene.
  • the melt flow rate of the metallocene-catalyzed polyethylene at 190°C under a load of 2.16kg is 0.5-4.0g/ 10min, the density is 0.86-0.930g/cm 3 ; preferably, the melt flow rate of the metallocene-catalyzed polyethylene at 190°C under a load of 2.16kg is 0.5-3.0g/10min, and the density is 0.86-0.89g/ cm 3 .
  • the melt flow rate of the high pressure polyethylene at 190°C under a load of 2.16 kg is 1.5-4.0 g/10min, and the density is 0.89-0.935 g/cm 3 ; preferably, the high pressure polyethylene is 2.16 g/cm 3 .
  • the melt flow rate at 190°C under kg load was 1.5-3.0 g/10min and the density was 0.89-0.92 g/cm 3 .
  • the polymer slippery masterbatch is prepared by blending and modifying the blend E, wherein the blend E contains optional siloxane, erucamide and a third medium density linear polyethylene.
  • the content of the silicon dioxide is 0-20% by weight; the content of the erucamide is 0.5-10% by weight, and the third medium density linear polymer
  • the ethylene content is 70-99.5% by weight.
  • the first medium density linear polyethylene, the second medium density linear polyethylene and the third medium density linear polyethylene are the same or different, each having a melt flow at 190°C under a load of 2.16 kg
  • the rate is 1.5-4.5g/10min
  • the density is 0.87-0.940g/cm 3 ; preferably, the melt flow rate at 190°C under a load of 2.16kg is 1.5-3.5g/10min, and the density is 0.89-0.92g /cm 3 .
  • the first anti-blocking masterbatch and the second anti-blocking masterbatch are the same or different, and each consists of silica and medium density polyethylene, wherein the first anti-blocking masterbatch or the second anti-blocking masterbatch is composed of silicon dioxide and medium density polyethylene.
  • the content of the silicon dioxide (SiO 2 ) is 0.5-1 wt %
  • the content of the medium density polyethylene is 99-99.5 wt %.
  • the present invention provides a barrier polyolefin composite film prepared from the aforementioned composition, wherein the composite film comprises a first layer film 810 and an intermediate layer film 830 stacked in sequence and the third layer film 850, and the first layer film 810 is obtained by extruding the first material containing the first layer film material; the intermediate layer film 830 is obtained by extruding the second material containing the intermediate layer film material;
  • the third layer film 850 includes a PE corona layer 610, a thermoplastic barrier layer 950 and a PE heat sealing layer 611 stacked in sequence; and the PE corona layer 610 is extruded from a third material containing a PE corona layer material
  • the thermoplastic barrier layer 950 is obtained by extruding the fourth material containing thermoplastic ethylene-vinyl alcohol copolymer and/or thermoplastic polyvinyl alcohol;
  • the PE heat-sealing layer 611 is obtained by extruding the fifth material containing the PE heat-sealing layer material. The material is extruded.
  • an aluminum film is also plated on the surface of the intermediate layer film 830 .
  • the aluminum film includes a vaporized aluminum film and/or an aluminum oxide film.
  • the inventors of the present invention have found through a large number of scientific experiments that: the surface of the interlayer film 830 is also plated with an aluminum film, which can form a dense barrier layer on the surface of the interlayer film 830, and can obtain Excellent moisture barrier, water barrier, gas barrier and oxygen barrier; in addition, the inventor of the present invention also found that the aluminum film has high brittleness, if used alone, it is easy to have cracks in the film winding or subsequent processing, The barrier property is reduced, and in the present invention, the aluminum film is vapor-deposited on the surface of the intermediate layer film 830, which can overcome the above-mentioned defects; at the same time, the transparency of the polyolefin composite film can be ensured.
  • the thickness of the first layer of film 810 is 5-80 ⁇ m; the thickness of the second layer of film 830 is 5-150 ⁇ m; the thickness of the third layer of film 850 is 5-200 ⁇ m; The thickness of the first layer film 810 is 9-60 ⁇ m; the thickness of the second layer film 830 is 10-50 ⁇ m; the thickness of the third layer film 850 is 40-100 ⁇ m; more preferably, the first layer The thickness of the film 810 is 20-30 ⁇ m; the thickness of the second film 830 is 20-30 ⁇ m; the thickness of the third film 850 is 70-90 ⁇ m.
  • the total thickness of the composite film is 15-430 ⁇ m, preferably 59-150 ⁇ m, more preferably 110-130 ⁇ m.
  • the composite film further includes a first film 810 , a first glue layer 821 , an intermediate film 830 , a second glue layer 822 and a third film 850 that are stacked in sequence.
  • the first glue layer 821 and the second glue layer 822 are the same or different, and each is one or more of polyvinyl alcohol compound glue, polyurethane two-component glue and modified polyolefin adhesive , preferably polyvinyl alcohol compound glue.
  • the polyvinyl alcohol compound glue includes a polyvinyl alcohol main agent and a curing agent, and based on the total weight of the polyvinyl alcohol compound glue, the solid content of the polyvinyl alcohol main agent is 15-32 % by weight, the solid content of the curing agent is 10-25% by weight.
  • the ratio of the polyvinyl alcohol main agent to the curing agent is 10:(0.5-1.5).
  • the respective gluing amounts of the first glue layer 821 and the second glue layer 822 are 1.0-10.0 g/m 2 , preferably 2.5-5.0 g/m 2 .
  • the third film 850 further comprises a PE corona layer 610 , a first polymer adhesive layer 210 , a thermoplastic barrier layer 950 , a second polymer adhesive layer 220 and a PE heat seal layer 611 stacked in sequence .
  • the first polymer adhesive layer 210 and the second polymer adhesive layer 220 are the same or different, and each is a maleic anhydride graft copolymer, the melting temperature is 119-125° C., and the load is 2.16kg.
  • the melt flow rate at 190°C was 2.8-3.5 g/10min, and the density was 0.935-0.942 g/cm 3 .
  • the content of the PE corona layer 610 , the first polymer adhesive layer 210 , the thermoplastic barrier layer 950 , the second polymer adhesive layer 220 and the PE heat seal layer 611 The weight ratio is 1:(0.02-0.95):(0.02-0.95):(0.02-0.95):(0.5-2); preferably 1:(0.1-0.6):(0.1-0.6):(0.1-0.6 ): (1.0-1.8).
  • the present invention provides a preparation method of the aforementioned composite membrane, wherein the preparation method comprises:
  • the third material is used to prepare the PE corona layer 610
  • the fourth material is used to prepare the thermoplastic barrier layer 950
  • the fifth material is used to prepare the PE heat sealing layer 611
  • the PE corona layer 610, the thermoplastic barrier layer 950 and the The PE heat-sealing layer 611 is sequentially bonded by the first polymer adhesive layer 210 and the second polymer adhesive layer 220 to prepare a third film 850;
  • the first layer film 810, the intermediate layer film 830 and the third layer film 850 are sequentially bonded through the first glue layer 821 and the second glue layer 822 to prepare a modified polyolefin composite film.
  • the preparation method further includes: the first layer film 810, the intermediate layer film 830 and the third layer film 850 are co-extruded and stretched, blown tube bubble method or flow Made by extension method.
  • the first layer film 810 is selected from one or more of multi-layer co-extruded stretched polyolefin films, multi-layer co-extruded cast polyolefin films and multi-layer co-extruded blown polyolefin films.
  • the multi-layer co-extruded stretched film is selected from multi-layer co-extruded uniaxially oriented polypropylene (MOPP) film, multi-layer co-extruded biaxially oriented polypropylene (BOPP) film, multi-layer co-extruded uniaxially stretched film Any of polyethylene (MOPE) film and multilayer co-extruded biaxially oriented polyethylene (BOPE) film.
  • the multi-layer co-extrusion cast polyolefin film is a multi-layer co-extrusion cast polypropylene (CPP) film and/or a multi-layer co-extrusion cast polyethylene (CPE) film.
  • CPP multi-layer co-extrusion cast polypropylene
  • CPE multi-layer co-extrusion cast polyethylene
  • the multi-layer co-extrusion blown polyolefin film is a multi-layer co-extrusion blown polypropylene (IPP) film and/or a multi-layer co-extrusion blown polyethylene (IPE) film.
  • IPP multi-layer co-extrusion blown polypropylene
  • IPE multi-layer co-extrusion blown polyethylene
  • the functional polyethylene film 810 is a multi-layer co-extruded biaxially oriented polyethylene (BOPE) film.
  • BOPE biaxially oriented polyethylene
  • an aluminum film is deposited on the surface of the interlayer film 830 by means of vapor deposition.
  • the intermediate layer film 830 is prepared by co-extrusion and uniaxial stretching method, biaxial stretching method or casting method, preferably, the intermediate layer film 830 is selected from multi-layer co-extrusion stretched polyolefin Vapor-deposited aluminum film, multilayer co-extrusion stretched polyolefin vapor-deposited aluminum film, multilayer co-extrusion cast polyolefin vapor-deposited aluminum film, multilayer co-extrusion cast polyolefin vapor-deposited aluminum oxide film a kind of;
  • the multi-layer co-extruded stretched polyolefin film is a multi-layer co-extruded uniaxially oriented polypropylene (MOPP) film, a multi-layer co-extruded biaxially oriented polypropylene (BOPP) film, a multi-layer co-extruded uniaxially stretched Any one of stretched polyethylene (MOPE) film and multi-layer co-extruded biaxially oriented polyethylene (BOPE) film;
  • the multi-layer co-extrusion cast polyolefin is any one of the multi-layer co-extrusion cast polypropylene (CPP) film and the multi-layer co-extrusion cast polyethylene (CPE) film;
  • the functional polyethylene film 830 is a multilayer co-extruded biaxially oriented polyethylene vapor-deposited alumina film.
  • the third layer film 850 is produced by co-extrusion and stretching, blowing or casting.
  • the third layer film 850 is a multi-layer co-extrusion cast barrier film; preferably, it is a five-layer co-extrusion cast barrier film; preferably, the layer structure of the five-layer co-extrusion cast barrier film is PE corona in sequence
  • the layer 610 , the first polymer adhesive layer 210 , the thermoplastic barrier layer 950 , the second polymer adhesive layer 220 , and the PE heat-sealing layer 611 are melted and co-extruded by an extruder to form a film.
  • the present invention provides an application of the aforementioned composite film in one or more of food packaging, industrial products, packaging of daily chemical products, and medicines and medical devices.
  • using the modified polyolefin composite film composition of the present invention and the preparation method of the present invention to prepare the modified polyolefin composite film includes:
  • the modified polyolefin composite film composition includes:
  • the first layer of film material multi-layer co-extruded biaxially oriented polyethylene (BOPE) film.
  • BOPE biaxially oriented polyethylene
  • Intermediate film material multilayer co-extruded biaxially oriented polyethylene vapor-deposited alumina film.
  • the third layer of film material is the third layer of film material.
  • PE corona layer material the first medium density linear polyethylene (MLDPE) and the first anti-blocking masterbatch; based on the total weight of the PE corona layer material, the content of the first medium density linear polyethylene is 95.5-96.5% by weight, and the content of the first anti-blocking masterbatch is 3.5-4.5% by weight.
  • MLDPE medium density linear polyethylene
  • Barrier layer film material thermoplastic polyvinyl alcohol, with a melt flow rate of 2.7-2.8 g/10min at 210°C under a load of 2.16 kg, and a density of 1.05-1.15 g/cm 3 .
  • PE heat sealing layer material second medium density linear polyethylene (MLDPE), metallocene catalyzed polyethylene (m-LLDPE), high pressure polyethylene (LDPE), second anti-blocking masterbatch and polymer slippery masterbatch; Based on the total weight of the PE heat-sealing layer material, the content of the second medium density linear polyethylene is 29-40% by weight, the content of the metallocene-catalyzed polyethylene is 25-27% by weight, and the high pressure The content of polyethylene is 25-30% by weight, the content of the second anti-blocking masterbatch is 5-7% by weight, and the content of the polymer slippery masterbatch is 5-7% by weight.
  • MLDPE second medium density linear polyethylene
  • m-LLDPE metallocene catalyzed polyethylene
  • LDPE high pressure polyethylene
  • second anti-blocking masterbatch second anti-blocking masterbatch and polymer slippery masterbatch
  • the melt flow rate of the metallocene-catalyzed polyethylene is 0.5-3.0g/10min, the density is 0.86-0.89g/cm 3 , and the melt flow rate of the high-pressure polyethylene is 1.5-3.0g/10min, the density is 0.89-0.92g/cm 3 , the first medium density linear polyethylene is the same as the second medium density linear polyethylene, and the melt flow rate is 1.5-3.0g/10min, The density is 0.89-0.92 g/cm 3 .
  • the component of the first polymer adhesive layer 210 is a maleic anhydride graft copolymer
  • the component of the second polymer adhesive layer 220 is a maleic anhydride graft copolymer
  • the component of the first glue layer 821 is polyvinyl alcohol
  • the composition of the second glue layer 822 is polyvinyl alcohol.
  • the first layer of film 810 is prepared from the first material of the first layer of film material by extrusion and biaxial stretching;
  • the interlayer film 830 is prepared by an aluminum oxide evaporation method
  • the PE corona layer 610 is prepared from the PE corona layer material by extrusion casting method
  • the barrier layer 950 is prepared from thermoplastic polyvinyl alcohol by extrusion casting method
  • the PE heat-sealing layer 611 is prepared from the PE heat-sealing layer material by extrusion casting method
  • the first layer film 810, the intermediate layer film 830 and the third layer film 850 are sequentially bonded through the first glue layer 821 and the second glue layer 822;
  • the PE corona layer 610, the polymer adhesive layer 210, the thermoplastic barrier layer 950, the polymer adhesive layer 210, and the PE heat sealing layer 611 have an extrusion ratio of 1:(0.1-0.6):(0.1-0.6 ): (0.1-0.6): (1.0-1.8);
  • the modified polyolefin composite film was prepared, marked as S1; the thickness of the first film 810 was 20-30 ⁇ m; the thickness of the intermediate film 830 was 20-30 ⁇ m; the thickness of the third film 850 was 70-90 ⁇ m , and the total thickness of the modified polyolefin composite film is 110-130 ⁇ m.
  • Test of puncture resistance The standard environment for sample state adjustment and test is carried out according to GB/T 2918.
  • the test environment conditions are temperature 23°C ⁇ 2°C, relative humidity 50% ⁇ 1%, according to GB/T 37841-2019 "Test Method for Puncture Resistance of Plastic Films and Sheets".
  • Oxygen transmission rate test The standard environment for sample state adjustment and test is carried out according to GB/T 2918.
  • the test environment conditions are temperature 23°C ⁇ 2°C, relative humidity 50% ⁇ 1%, according to GB/T 1038-2000 "Plastic film and sheet gas permeability test method pressure difference method" to test.
  • Drop performance of the bag The standard environment for sample state adjustment and test is carried out according to GB/T 2918, the test environment conditions are temperature 23°C ⁇ 2°C, relative humidity 50% ⁇ 1%, according to GB/T 10004-2008 "Packaging plastic composite film, bag dry composite, extrusion composite" to test.
  • the weight of the bag and inner package is 1000g, and the drop height is 500mm.
  • This example is to illustrate the preparation of the modified polyolefin composite film by using the modified polyolefin composite film composition of the present invention and the preparation method of the present invention.
  • the modified polyolefin composite film composition includes:
  • the first layer of film material multi-layer co-extruded biaxially oriented polyethylene (BOPE) film.
  • BOPE biaxially oriented polyethylene
  • Intermediate film material multilayer co-extruded biaxially oriented polyethylene vapor-deposited alumina film.
  • the third layer of film material is the third layer of film material.
  • PE corona layer material the first medium density linear polyethylene (MLDPE) and the first anti-blocking masterbatch; based on the total weight of the PE corona layer material, the content of the first medium density linear polyethylene is 96.5% by weight, and the content of the first anti-blocking masterbatch is 3.5% by weight.
  • MLDPE medium density linear polyethylene
  • Barrier layer film material thermoplastic polyvinyl alcohol, with a melt flow rate of 2.8 g/10 min at 210° C. under a load of 2.16 kg, and a density of 1.05 g/cm 3 .
  • PE heat sealing layer material second medium density linear polyethylene (MLDPE), metallocene catalyzed polyethylene (m-LLDPE), high pressure polyethylene (LDPE), second anti-blocking masterbatch and polymer slippery masterbatch; Based on the total weight of the PE heat-sealing layer material, the content of the second medium density linear polyethylene is 35% by weight, the content of the metallocene catalyzed polyethylene is 25% by weight, and the content of the high pressure polyethylene is 25% by weight. is 30% by weight, the content of the second anti-blocking masterbatch is 5% by weight, and the content of the polymer slippery masterbatch is 5% by weight.
  • MLDPE second medium density linear polyethylene
  • m-LLDPE metallocene catalyzed polyethylene
  • LDPE high pressure polyethylene
  • the melt flow rate of the metallocene-catalyzed polyethylene is 3.0g/10min
  • the density is 0.89g/cm 3
  • the melt flow rate of the high pressure polyethylene is 3.0g/10min
  • the density is 0.92g/cm 3
  • the first medium density linear polyethylene is the same as the second medium density linear polyethylene
  • the melt flow rate is 3.0g/10min
  • the density is 0.92g/cm 3 .
  • the component of the first polymer adhesive layer 210 is a maleic anhydride graft copolymer
  • the component of the second polymer adhesive layer 220 is a maleic anhydride graft copolymer
  • the component of the first glue layer 821 is polyvinyl alcohol
  • the composition of the second glue layer 822 is polyvinyl alcohol.
  • the first layer of film 810 is prepared from the first material of the first layer of film material by extrusion and biaxial stretching;
  • the interlayer film 830 is prepared by an aluminum oxide evaporation method
  • the PE corona layer 610 is prepared from the PE corona layer material by extrusion casting method
  • the barrier layer film 950 is prepared from polyvinyl alcohol by extrusion casting method
  • the PE heat-sealing layer 611 is prepared from the PE heat-sealing layer material by extrusion casting method
  • the first layer film 810, the intermediate layer film 830 and the third layer film 850 are successively bonded by the first glue layer 821 and the second glue layer 822;
  • the extrusion ratio is 1:0.6:0.6:0.6:1.8;
  • a modified polyolefin composite film was prepared, marked as S1; wherein, the thickness of the first layer film 810 was 20 ⁇ m; the thickness of the intermediate layer film 830 was 20 ⁇ m; the thickness of the third layer film 850 was 80 ⁇ m, and the modified The total thickness of the polyolefin composite film was 122 ⁇ m.
  • modified polyolefin composite film was tested for maximum puncture force, oxygen permeability and water vapor permeability, and the results are shown in Table 1;
  • This example is to illustrate the preparation of the modified polyolefin composite film by using the modified polyolefin composite film composition of the present invention and the preparation method of the present invention.
  • the modified polyolefin composite film composition includes:
  • the first layer of film material multi-layer co-extruded biaxially oriented polyethylene (BOPE) film.
  • BOPE biaxially oriented polyethylene
  • Intermediate film material multilayer co-extruded biaxially oriented polyethylene vapor-deposited alumina film.
  • the third layer of film material is the third layer of film material.
  • PE corona layer material the first medium density linear polyethylene (MLDPE) and the first anti-blocking masterbatch; based on the total weight of the PE corona layer material, the content of the first medium density linear polyethylene is 80% by weight, and the content of the first anti-blocking masterbatch is 20% by weight.
  • MLDPE medium density linear polyethylene
  • Barrier layer film material thermoplastic polyvinyl alcohol, with a melt flow rate of 2.0 g/10 min at 210° C. under a load of 2.16 kg, and a density of 0.92 g/cm 3 .
  • PE heat sealing layer material second medium density linear polyethylene (MLDPE), metallocene catalyzed polyethylene (m-LLDPE), high pressure polyethylene (LDPE), second anti-blocking masterbatch and polymer slippery masterbatch; Based on the total weight of the PE heat-sealing layer material, the content of the second medium density linear polyethylene is 10% by weight, the content of the metallocene catalyzed polyethylene is 30% by weight, and the content of the high pressure polyethylene is 30% by weight. is 40% by weight, the content of the second anti-blocking masterbatch is 10% by weight, and the content of the polymer slippery masterbatch is 10% by weight.
  • MLDPE second medium density linear polyethylene
  • m-LLDPE metallocene catalyzed polyethylene
  • LDPE high pressure polyethylene
  • second anti-blocking masterbatch second anti-blocking masterbatch and polymer slippery masterbatch
  • the melt flow rate of the metallocene-catalyzed polyethylene is 0.5g/10min, the density is 0.86g/cm 3 , and the melt flow rate of the high pressure polyethylene is 1.5g/10min , the density is 0.89g/cm 3 , the first medium density linear polyethylene is the same as the second medium density linear polyethylene, the melt flow rate is 1.5g/10min, and the density is 0.89g/cm 3 .
  • the component of the first polymer adhesive layer 210 is a maleic anhydride graft copolymer
  • the component of the second polymer adhesive layer 220 is a maleic anhydride graft copolymer
  • the component of the first glue layer 821 is polyvinyl alcohol
  • the composition of the second glue layer 822 is polyvinyl alcohol.
  • the first layer of film 810 is prepared from the first material of the first layer of film material by extrusion and biaxial stretching;
  • the interlayer film 830 is prepared by an aluminum oxide evaporation method
  • the PE corona layer 610 is prepared from the PE corona layer material by extrusion casting method
  • the barrier layer film 950 is prepared from polyvinyl alcohol by extrusion casting method
  • the PE heat-sealing layer 611 is prepared from the PE heat-sealing layer material by extrusion casting method
  • the first layer film 810, the intermediate layer film 830 and the third layer film 850 are sequentially bonded through the first glue layer 821 and the second glue layer 822;
  • the extrusion ratio is 1:0.6:0.6:0.6:1.8;
  • the compound gluing amount is 10g/ m2 glues 821 and 822, and the compound structure is 810/glue/830/glue/850, After compounding, it is dried in a drying oven, and then cured for 2 days at a temperature of 48 °C ⁇ 5 °C and a humidity below 50% RH; after taking it out, it is cut and bagged; among them, the virtual box can be selected not to carry out process.
  • a modified polyolefin composite film was prepared, marked as S2; wherein, the thickness of the first layer film 810 was 20 ⁇ m; the thickness of the intermediate layer film 830 was 20 ⁇ m; the thickness of the third layer film 850 was 80 ⁇ m, and the modified The total thickness of the polyolefin composite film was 128 ⁇ m.
  • modified polyolefin composite film was tested for maximum puncture force, oxygen permeability and water vapor permeability, and the results are shown in Table 1;
  • This example is to illustrate the preparation of the modified polyolefin composite film by using the modified polyolefin composite film composition of the present invention and the preparation method of the present invention.
  • the modified polyolefin composite film composition includes:
  • the first layer of film material multi-layer co-extruded biaxially oriented polyethylene (BOPE) film.
  • BOPE biaxially oriented polyethylene
  • Intermediate film material multilayer co-extruded biaxially oriented polyethylene vapor-deposited alumina film.
  • the third layer of film material is the third layer of film material.
  • PE corona layer material the first medium density linear polyethylene (MLDPE) and the first anti-blocking masterbatch; based on the total weight of the PE corona layer material, the content of the first medium density linear polyethylene is 99.5% by weight, and the content of the first anti-blocking masterbatch is 0.5% by weight.
  • MLDPE medium density linear polyethylene
  • Barrier layer film material thermoplastic polyvinyl alcohol, with a melt flow rate of 5 g/10 min at 210° C. under a load of 2.16 kg, and a density of 1.3 g/cm 3 .
  • PE heat sealing layer material second medium density linear polyethylene (MLDPE), metallocene catalyzed polyethylene (m-LLDPE), high pressure polyethylene (LDPE), second anti-blocking masterbatch and polymer slippery masterbatch; Based on the total weight of the PE heat-sealing layer material, the content of the second medium density linear polyethylene is 58.5% by weight, the content of the metallocene catalyzed polyethylene is 20% by weight, and the content of the high pressure polyethylene is 20% by weight. The content of the second anti-blocking masterbatch is 0.5% by weight, and the content of the polymer slippery masterbatch is 1% by weight.
  • MLDPE second medium density linear polyethylene
  • m-LLDPE metallocene catalyzed polyethylene
  • LDPE high pressure polyethylene
  • second anti-blocking masterbatch polymer slippery masterbatch
  • the melt flow rate of the metallocene-catalyzed polyethylene is 4.0g/10min
  • the density is 0.93g/cm 3
  • the melt flow rate of the high pressure polyethylene is 4.0g/10min
  • the density is 0.935g/cm 3
  • the first medium density linear polyethylene is the same as the second medium density linear polyethylene
  • the melt flow rate is 4.5g/10min
  • the density is 0.94g/cm 3 .
  • the component of the first polymer adhesive layer 210 is a maleic anhydride graft copolymer
  • the component of the second polymer adhesive layer 220 is a maleic anhydride graft copolymer
  • the component of the first glue layer 821 is polyvinyl alcohol
  • the composition of the second glue layer 822 is polyvinyl alcohol.
  • the first layer of film 810 is prepared from the first material of the first layer of film material by extrusion and biaxial stretching;
  • the interlayer film 830 is prepared by an aluminum oxide evaporation method
  • the PE corona layer 610 is prepared from the PE corona layer material by extrusion casting method
  • the barrier layer film 950 is prepared from polyvinyl alcohol by extrusion casting method
  • the PE heat-sealing layer 611 is prepared from the PE heat-sealing layer material by extrusion casting method
  • the first layer film 810, the intermediate layer film 830 and the third layer film 850 are sequentially bonded through the first glue layer 821 and the second glue layer 822;
  • the extrusion ratio is 1:0.02:0.02:0.02:1.8;
  • a modified polyolefin composite film was prepared, marked as S3; wherein, the thickness of the first layer film 810 was 20 ⁇ m; the thickness of the intermediate layer film 830 was 20 ⁇ m; the thickness of the third layer film 850 was 80 ⁇ m, and the modified The total thickness of the polyolefin composite film was 120 ⁇ m.
  • modified polyolefin composite film was tested for maximum puncture force, oxygen permeability and water vapor permeability, and the results are shown in Table 1;
  • This example is to illustrate the preparation of the modified polyolefin composite film by using the modified polyolefin composite film composition of the present invention and the preparation method of the present invention.
  • the modified polyolefin composite membrane was prepared in the same manner as in Example 1, except that:
  • the interlayer film 830 is prepared;
  • a modified polyolefin composite film was prepared, marked as S4; wherein, the thickness of the first layer film 810 was 20 ⁇ m; the thickness of the intermediate layer film 830 was 20 ⁇ m; the thickness of the third layer film 850 was 80 ⁇ m, and the modified The total thickness of the polyolefin composite film was 122 ⁇ m.
  • modified polyolefin composite film was tested for maximum puncture force, oxygen permeability and water vapor permeability, and the results are shown in Table 1;
  • This example is to illustrate the preparation of the modified polyolefin composite film by using the modified polyolefin composite film composition of the present invention and the preparation method of the present invention.
  • the modified polyolefin composite membrane was prepared in the same manner as in Example 1, except that:
  • a modified polyolefin composite film was prepared, marked as S5; wherein, the thickness of the first layer film 810 was 60 ⁇ m; the thickness of the intermediate layer film 830 was 50 ⁇ m; the thickness of the third layer film 850 was 100 ⁇ m, and the modified The total thickness of the polyolefin composite film was 212 ⁇ m.
  • modified polyolefin composite film was tested for maximum puncture force, oxygen permeability and water vapor permeability, and the results are shown in Table 1;
  • This example is to illustrate the preparation of the modified polyolefin composite film by using the modified polyolefin composite film composition of the present invention and the preparation method of the present invention.
  • the modified polyolefin composite membrane was prepared in the same manner as in Example 1, except that:
  • a modified polyolefin composite film was prepared, marked as S6; wherein, the thickness of the first layer film 810 was 10 ⁇ m; the thickness of the intermediate layer film 830 was 10 ⁇ m; the thickness of the third layer film 850 was 10 ⁇ m, and the modified The total thickness of the polyolefin composite film was 32 ⁇ m.
  • modified polyolefin composite film was tested for maximum puncture force, oxygen permeability and water vapor permeability, and the results are shown in Table 1;
  • This example is to illustrate the preparation of the modified polyolefin composite film by using the modified polyolefin composite film composition of the present invention and the preparation method of the present invention.
  • the modified polyolefin composite membrane was prepared in the same manner as in Example 1, except that:
  • the first glue layer 821 and the second glue layer 822 are polyurethane two-component glue
  • the interlayer film 830 is prepared;
  • a modified polyolefin composite film was prepared, marked as S7; wherein, the thickness of the first layer film 810 was 20 ⁇ m; the thickness of the intermediate layer film 830 was 20 ⁇ m; the thickness of the third layer film 850 was 80 ⁇ m, and the modified The total thickness of the polyolefin composite film was 122 ⁇ m.
  • modified polyolefin composite film was tested for maximum puncture force, oxygen permeability and water vapor permeability, and the results are shown in Table 1;
  • the modified polyolefin composite membrane was prepared in the same manner as in Example 1, except that:
  • the modified polyolefin composite film composition does not include the barrier layer film material
  • the interlayer film 830 is prepared;
  • a modified polyolefin composite film was prepared, marked as D1; wherein, the thickness of the first layer film 810 was 20 ⁇ m; the thickness of the intermediate layer film 830 was 20 ⁇ m; the thickness of the third layer film 850 was 80 ⁇ m, and the modified The thickness of the polyolefin composite film was 122 ⁇ m.
  • modified polyolefin composite film was tested for maximum puncture force, oxygen permeability and water vapor permeability, and the results are shown in Table 1;
  • the modified polyolefin composite membrane was prepared in the same manner as in Example 1, except that:
  • the first glue layer 821 and the second glue layer 822 are modified polyolefin adhesives
  • the interlayer film 830 is prepared;
  • a modified polyolefin composite film was prepared, marked as D2; wherein, the thickness of the first layer film 810 was 20 ⁇ m; the thickness of the intermediate layer film 830 was 20 ⁇ m; the thickness of the third layer film 850 was 80 ⁇ m, and the modified The thickness of the polyolefin composite film was 128 ⁇ m.
  • modified polyolefin composite film was tested for maximum puncture force, oxygen permeability and water vapor permeability, and the results are shown in Table 1;
  • the modified polyolefin composite membrane was prepared in the same manner as in Example 1, except that:
  • the modified polyolefin composite film was prepared, marked as D3; wherein, the thickness of the first layer film 810 was 30 ⁇ m.
  • modified polyolefin composite film was tested for maximum puncture force, oxygen permeability and water vapor permeability, and the results are shown in Table 1;
  • the modified polyolefin composite membrane was prepared in the same manner as in Example 1, except that:
  • a modified polyolefin composite film was prepared, marked as D4; wherein, the thickness of the first layer film 810 was 30 ⁇ m.
  • modified polyolefin composite film was tested for maximum puncture force, oxygen permeability and water vapor permeability, and the results are shown in Table 1;
  • the modified polyolefin composite membrane was prepared in the same manner as in Example 1, except that:
  • the modified polyolefin composite film was prepared, marked as D5; wherein, the thickness of the first layer film 810 was 30 ⁇ m.
  • modified polyolefin composite film was tested for maximum puncture force, oxygen permeability and water vapor permeability, and the results are shown in Table 1;
  • the modified polyolefin composite membrane was prepared in the same manner as in Example 1, except that:
  • a modified polyolefin composite film was prepared, marked as D6; wherein, the thickness of the first layer film 810 was 30 ⁇ m.
  • modified polyolefin composite film was tested for maximum puncture force, oxygen permeability and water vapor permeability, and the results are shown in Table 1;
  • the modified polyolefin composite membrane was prepared in the same manner as in Example 1, except that:
  • the modified polyolefin composite film composition does not include the interlayer film material
  • the first layer of film 810 and the third layer of film 850 are sequentially bonded through the first glue layer 821 and the second glue layer 822;
  • a modified polyolefin composite film was prepared, marked as D7; wherein, the thickness of the first layer film 810 was 20 ⁇ m; the thickness of the intermediate layer film 830 was 0 ⁇ m; the thickness of the third layer film 850 was 80 ⁇ m, and the modified The thickness of the polyolefin composite film was 101 ⁇ m.
  • modified polyolefin composite film was tested for maximum puncture force, oxygen permeability and water vapor permeability, and the results are shown in Table 1;
  • the modified polyolefin composite membrane was prepared in the same manner as in Example 1, except that:
  • the modified polyolefin composite film composition does not include the first layer of film material
  • the intermediate layer film 830 and the third layer film 850 are sequentially bonded through the first glue layer 821 and the second glue layer 822;
  • a modified polyolefin composite film was prepared, marked as D8; wherein, the thickness of the first layer film 810 was 0 ⁇ m; the thickness of the intermediate layer film 830 was 20 ⁇ m; the thickness of the third layer film 850 was 80 ⁇ m, and the modified The thickness of the polyolefin composite film was 101 ⁇ m.
  • modified polyolefin composite film was tested for maximum puncture force, oxygen permeability and water vapor permeability, and the results are shown in Table 1;
  • the modified polyolefin composite membrane was prepared in the same manner as in Example 1, except that:
  • the modified polyolefin composite film composition does not include PE corona layer material, barrier layer film material and PE heat sealing layer material;
  • the first layer film 810 and the intermediate layer film 830 are bonded through the first glue layer 821 and the second glue layer 822 in sequence;
  • a modified polyolefin composite film was prepared, marked as D9; wherein the thickness of the first layer film 810 was 20 ⁇ m; the thickness of the intermediate layer film 830 was 20 ⁇ m; the thickness of the third layer film 850 was 0 ⁇ m, and the modified The thickness of the polyolefin composite film was 41 ⁇ m.
  • modified polyolefin composite film was tested for maximum puncture force, oxygen permeability and water vapor permeability, and the results are shown in Table 1;
  • the thin-film vapor-deposited aluminum oxide layer can obtain excellent oxygen barrier properties.
  • the oxygen barrier property of polyvinyl alcohol glue is higher than that of ordinary commercial glue; the larger the amount of polyvinyl alcohol glue applied, the better the oxygen barrier property.
  • Polypropylene has large steric hindrance due to its side methyl groups. Under the same film manufacturing process conditions, polypropylene has better oxygen barrier properties than polyethylene.
  • the thin-film vapor-deposited aluminum oxide layer can obtain excellent water vapor barrier properties.
  • Polyolefin film and polyolefin vapor-deposited alumina film have good water vapor resistance.
  • the barrier property of the thermoplastic polyvinyl alcohol barrier layer plays a positive role in superposition, and the water vapor barrier property is the best.
  • Polypropylene has large steric hindrance due to its side methyl groups. Under the same film manufacturing process conditions, polypropylene has better water vapor barrier properties than polyethylene.
  • the non-corona layer (heat-sealing layer) of the multilayer co-extrusion cast barrier film 850 has a low or no layer thickness ratio, and under the condition that the glue 820 is applied in a small or no amount, the heat-sealing strength is low, and the interlayer peeling strength is low.
  • the bag has poor pressure resistance and poor drop resistance. Bags leaking and bursting.
  • the multi-layer co-extruded biaxially oriented polyethylene and the multi-layer co-extruded biaxially oriented polypropylene film are stretched, the molecular chains are neatly arranged, the crystallinity is high, and there is no heat sealing, so the pressure resistance of the bag is poor. , poor drop resistance.
  • the bag leaks and ruptures; the multi-layer co-extrusion cast polyethylene film is not stretched, the molecular chain is flexible, and the thermal bonding strength is slightly higher than that of the multi-layer co-extrusion cast polypropylene film. Therefore, the pressure resistance of the bag is slightly better, and the drop resistance is slightly stronger. The bag does not leak or rupture.

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Abstract

提供了一种改性聚烯烃复合膜组合物和改性聚烯烃复合膜及其制备方法和应用，组合物包括第一层膜材、中间层膜材和第三层膜材，以及第三层膜材包括PE电晕层料、阻隔层膜料和PE热封层料；第一层膜材和中间层膜材均各自含有C4-C8的聚乙烯、一元均聚聚丙烯、二元共聚聚丙烯和三元共聚聚丙烯中的一种或多种；阻隔层膜料含有乙烯-乙烯醇共聚物和/或热塑性聚乙烯醇。复合膜具有优异的阻隔性、优异抗穿刺性、优异耐压性和优异跌落性。

Description

改性聚烯烃复合膜组合物和改性聚烯烃复合膜及其制备方法和应用
相关申请的交叉引用
本申请享有申请号为No.202011323168.8，申请日为2020年11月23日，以及申请号为No.202011577800.1，申请日为2020年12月28日提交的中国专利申请的权益，该申请的内容通过引用被合并于本文。
技术领域
本发明涉及复合包装加工技术领域，具体涉及一种改性聚烯烃复合膜组合物和改性聚烯烃复合膜及其制备方法和应用。
背景技术
随着人们生活水平提高及审美多样化，消费者及生产者对包装不论是品质还是感观的追求达到极致。绝大多数包装为满足功能性及外观要求采用了多材质薄膜进行复合。例如液体奶的单品复合包装结构是：BOPA薄膜//胶水//PET镀铝膜//胶水//吹塑PE薄膜；坚果类复合包装结构：BOPP薄膜//胶水//纸//胶水//BOPET镀铝膜//胶水//吹塑PE薄膜。
包装作为商品保护上不可或缺的材料，包装需求量及产量在增长，但废弃多材质复合包装分类、回收却不易，目前仍没有有效的方法使复合不同材质的薄膜分开并分类回收。土地掩埋废弃包装材料会造成土壤贫瘠、恶化，农作物减产或不产；焚化废弃塑胶会产生大量CO 2、CO等有毒气体以及灰分中残留重金属，加重环境污染和温室效应；大量的研究发现海洋生物正在被废弃包装材料危害生命。循环再利用任务任重道远。
另外，消费者不希望消费品包装视觉感受变差，希望在不增添化学物质的前提下，食品及日化用品的保持期延长、不串味、无异味。
因此，研究和开发一种具有高阻隔性、且在完成包装使用丢弃后易回收可再次热塑性加工循环利用的改性聚烯烃复合膜组合物和改性聚烯烃复合膜具有重要意义。
发明内容
本发明的目的是为了克服现有技术存在的复合包装材料不易于回收循环再利用的问题，复合包装材料的抗穿刺力、阻湿阻水和阻气阻氧性差的问题，以及复合包装材料的耐压性和跌落性差的问题，提供一种改性聚烯烃复合膜组合物和改性聚烯烃复合膜及其制备方法和应用。该复合膜具有优异的阻隔性、优异抗穿刺性、优异耐压性和优异跌落性，且复合膜材质主要为聚烯烃，具有可实现完全回收循环利用的优点。
为了实现上述目的，本发明第一方面提供了一种改性聚烯烃复合膜组合物，其中，组 合物包括第一层膜材、中间层膜材和第三层膜材，以及所述第三层膜材包括PE电晕层料、阻隔层膜料和PE热封层料；
其中，所述第一层膜材和所述中间层膜材均各自包括C4-C8的聚乙烯、一元均聚聚丙烯、二元共聚聚丙烯和三元共聚聚丙烯中的一种或多种；以及所述阻隔层膜料含有乙烯-乙烯醇共聚物和/或热塑性聚乙烯醇。
本发明第二方面提供了一种由前述所述的组合物制得的阻隔聚烯烃复合膜，其中，所述复合膜包括依次叠加的第一层膜810、中间层膜830和第三层膜850，以及所述第一层膜810由含有第一层膜材的第一物料挤出得到；，所述中间层膜830由含有中间层膜料的第二物料挤出得到；
其中，所述第三层膜850包括依次叠加的PE电晕层610、热塑性阻隔层950和PE热封层611；以及所述PE电晕层610由含有PE电晕层料的第三物料挤出得到；所述热塑性阻隔层950由含有热塑性乙烯-乙烯醇共聚物和/或热塑性聚乙烯醇的第四物料挤出得到；所述PE热封层611由含有PE热封层料的第五物料挤出得到。
本发明第三方面提供了一种前述所述的复合膜的制备方法，其中，所述的制备方法包括：
(1)采用第一物料制备第一层膜810；
(2)采用第二物料制备中间层膜830；
(3)采用第三物料制备PE电晕层610、第四物料制备热塑性阻隔层950、第五物料制备PE热封层611，以及将所述PE电晕层610、所述热塑性阻隔层950和所述PE热封层611依次通过第一高分子粘合层210和第二高分子粘合层220粘合，制备第三层膜850；
(4)将第一层膜810、中间层膜830和第三层膜850依次通过第一胶水层821和第二胶水层822粘合，制备改性聚烯烃复合膜。
本发明第四方面提供了一种前述所述的复合膜在食品包装、工业品、日化用品包装和医药及医疗器械中的一种或多种中的应用。
通过上述技术方案，本发明的改性聚烯烃复合膜具有优异的阻隔性、优异抗穿刺性、优异耐压性和优异跌落性；另外，符合环保趋势，其功能和外观符合市场需求，具有重大社会意义。
附图说明
图1是本发明的改性聚烯烃复合膜的结构示意图；
图2是本发明的改性聚烯烃复合膜中第三层膜850的结构示意图；
图3是采用本发明的改性聚烯烃复合膜制备成品的流程示意图。
具体实施方式
在本文中所披露的范围的端点和任何值都不限于该精确的范围或值，这些范围或值应当理解为包含接近这些范围或值的值。对于数值范围来说，各个范围的端点值之间、各个范围的端点值和单独的点值之间，以及单独的点值之间可以彼此组合而得到一个或多个新的数值范围，这些数值范围应被视为在本文中具体公开。
根据本发明的第一方面，本发明提供了一种改性聚烯烃复合膜组合物，其中，所述组合物包括第一层膜材、中间层膜料和第三层膜材，以及所述第三层膜材包括PE电晕层料、阻隔层膜料和PE热封层料；
其中，所述第一层膜材和所述中间层膜料均各自包括C4-C8的聚乙烯、一元均聚聚丙烯、二元共聚聚丙烯和三元共聚聚丙烯中的一种或多种；以及所述阻隔层膜料含有乙烯-乙烯醇共聚物和/或热塑性聚乙烯醇。
根据本发明，本发明的发明人经过大量科学实验发现：在多层共挤聚烯烃复合膜生产过程中使用含有乙烯-乙烯醇共聚物和/或热塑性聚乙烯醇的阻隔层膜料，具有高阻隔性及可降解特性，在合适配比及挤出工艺条件下，形成的高阻隔层具有优异的阻气阻氧性，同时该聚烯烃复合膜能保持良好的透明度，具有良好的阻湿阻水性。
根据本发明，一元均聚聚丙烯，一般也称为均聚聚丙烯，在本发明中，所述一元均聚聚丙烯为等规度大于95％均聚聚丙烯。
二元共聚聚丙烯是乙烯丙烯共聚聚丙烯和/或乙烯丁烯共聚聚丙烯。
三元共聚聚丙烯是乙烯丙烯丁烯共聚聚丙烯和/或乙烯丙烯己烯共聚聚丙烯。
根据本发明，优选情况下，所述阻隔层膜料含有热塑性聚乙烯醇(TPVA)，其中，所述热塑性聚乙烯醇在2.16kg载荷下210℃时的熔体流动速率为2.0-5.0g/10min，密度为0.92-1.30g/cm 3；优选地，所述热塑性聚乙烯醇在2.16kg载荷下210℃时的熔体流动速率为2.5-4.0g/10min，密度为1.0-1.28g/cm 3；更优选地，所述热塑性聚乙烯醇在2.16kg载荷下210℃时的熔体流动速率为2.7-2.9g/10min，密度为1.05-1.15g/cm 3。
在本发明中，所述热塑性聚乙烯醇和所述乙烯-乙烯醇共聚物均可通过商购获得，例如，可以购自中国石化，型号分别为为TPVA-1，EVOH-1。
根据本发明，所述PE电晕层料含有第一中密度线性聚乙烯(MLDPE)和第一抗粘连母料；优选地，以所述PE电晕层料的总重量为基准，所述第一中密度线性聚乙烯的含量为 80.0-99.5重量％，所述第一抗粘连母料的含量为0.5-20重量％；更优选地，以所述PE电晕层料的总重量为基准，所述第一中密度线性聚乙烯的含量为90-98重量％，所述第一抗粘连母料的含量为2-10重量％；更进一步优选地，以所述PE电晕层料的总重量为基准，所述第一中密度线性聚乙烯的含量为95-97重量％，所述第一抗粘连母料的含量为3-5重量％。
根据本发明，所述PE热封层料含有第二中密度线性聚乙烯(MLDPE)、茂金属催化聚乙烯(m-LLDPE)、高压聚乙烯(LDPE)、第二抗粘连母料和高分子爽滑母料中的一种或多种；优选地，以所述PE热封层料的总重量为基准，所述第二中密度线性聚乙烯的含量为10.0-58.5重量％，所述茂金属催化聚乙烯的含量为20-30重量％，所述高压聚乙烯的含量为20-40重量％，所述第二抗粘连母料的含量为0.5-10重量％，所述高分子爽滑母料的含量为1.0-10重量％。更优选地，以所述PE热封层料的总重量为基准，所述第二中密度线性聚乙烯的含量为25-40重量％，所述茂金属催化聚乙烯的含量为25-29重量％，所述高压聚乙烯的含量为25-30重量％，所述第二抗粘连母料的含量为5-8重量％，所述高分子爽滑母料的含量为5-8重量％。
根据本发明，所述茂金属催化聚乙烯为C6-C8茂金属催化聚乙烯，优选地，所述茂金属催化聚乙烯在2.16kg载荷下190℃时的熔体流动速率为0.5-4.0g/10min，密度为0.86-0.930g/cm 3；优选地，所述茂金属催化聚乙烯在2.16kg载荷下190℃时的熔体流动速率为0.5-3.0g/10min，密度为0.86-0.89g/cm 3。
根据本发明，所述高压聚乙烯在2.16kg载荷下190℃时的熔体流动速率为1.5-4.0g/10min，密度为0.89-0.935g/cm 3；优选地，所述高压聚乙烯在2.16kg载荷下190℃时的熔体流动速率为1.5-3.0g/10min，密度为0.89-0.92g/cm 3。
根据本发明，所述高分子爽滑母料为共混物E经共混改性制备得到，其中，所述共混物E中含有可选的硅硐、芥酸酰胺和第三中密度线性聚乙烯。优选地，以所述共混物E总重量为基准，所述硅硐的含量为0-20重量％；所述芥酸酰胺的含量为0.5-10重量％，所述第三中密度线性聚乙烯的含量为70-99.5重量％。
根据本发明，所述第一中密度线性聚乙烯、所述第二中密度线性聚乙烯和所述第三中密度线性聚乙烯相同或不同，各自在2.16kg载荷下190℃时的熔体流动速率为1.5-4.5g/10min，密度为0.87-0.940g/cm 3；优选地，各自在2.16kg载荷下190℃时的熔体流动速率为1.5-3.5g/10min，密度为0.89-0.92g/cm 3。
根据本发明，所述第一抗粘连母料和所述第二抗粘连母料相同或不同，各自由二氧化硅和中密度聚乙烯组成，其中，以所述第一抗粘连母料或所述第二抗粘连母料的总重量为基 准，所述二氧化硅(SiO 2)的含量为0.5-1重量％，所述中密度聚乙烯的含量为99-99.5重量％。
根据本发明的第二方面，本发明提供了一种由前述所述的组合物制得的阻隔聚烯烃复合膜，其中，所述复合膜包括依次叠加的第一层膜810、中间层膜830和第三层膜850，以及所述第一层膜810由含有第一层膜材的第一物料挤出得到；所述中间层膜830由含有中间层膜料的第二物料挤出得到；
其中，所述第三层膜850包括依次叠加的PE电晕层610、热塑性阻隔层950和PE热封层611；以及所述PE电晕层610由含有PE电晕层料的第三物料挤出得到；所述热塑性阻隔层950由含有热塑性乙烯-乙烯醇共聚物和/或热塑性聚乙烯醇的第四物料挤出得到；所述PE热封层611由含有PE热封层料的第五物料挤出得到。
根据本发明，所述中间层膜830的表面上还镀有铝膜，优选地，所述铝膜包括气化铝膜和/或氧化铝膜。
根据本发明，本发明的发明人经过大量科学实验发现：所述中间层膜830的表面上还镀有铝膜，该铝膜能够在中间层膜830的表面上形成致密的阻隔层，能够获得优异的阻湿阻水、阻气阻氧性；另外，本发明的发明人还发现，该铝膜具有较高的脆性，如果单独使用，则在薄膜收卷或后道加工中易有裂痕，使阻隔性下降，而在本发明中，将该铝膜蒸镀在所述中间层膜830的表面，能够克服上述缺陷；同时，能够保证聚烯烃复合膜的透明度。
根据本发明，所述第一层膜810的厚度为5-80μm；所述第二层膜830的厚度为5-150μm；所述第三层膜850的厚度为5-200μm；优选地，所述第一层膜810的厚度为9-60μm；所述第二层膜830的厚度为10-50μm；所述第三层膜850的厚度为40-100μm；更优选地，所述第一层膜810的厚度为20-30μm；所述第二层膜830的厚度为20-30μm；所述第三层膜850的厚度为70-90μm。
根据本发明，所述复合膜的总厚度为15-430μm，优选为59-150μm，更优选为110-130μm。
根据本发明，所述复合膜还包括依次叠加的第一层膜810、第一胶水层821、中间层膜830、第二胶水层822和第三层膜850。
根据本发明，所述第一胶水层821和所述第二胶水层822相同或不同，各自为聚乙烯醇复配胶水、聚氨酯双组份胶水和改性聚烯烃胶粘剂中的一种或多种，优选为聚乙烯醇复配胶水。
根据本发明，所述聚乙烯醇复配胶水包括聚乙烯醇主剂和固化剂，且以所述聚乙烯醇复配胶水的总重量为基准，聚乙烯醇主剂的固含量为15-32重量％，固化剂的固含量为10-25 重量％。
根据本发明，聚乙烯醇主剂与所述固化剂的配比为10∶(0.5-1.5)。
根据本发明，所述第一胶水层821和所述第二胶水层822各自的上胶量为1.0-10.0g/m 2，优选为2.5-5.0g/m 2。
根据本发明，所述第三层膜850还包括依次叠加的PE电晕层610、第一高分子粘合层210、热塑性阻隔层950、第二高分子粘合层220和PE热封层611。
根据本发明，所述第一高分子粘合层210和所述第二高分子粘合层220相同或不同，各自为马来酸酐接枝共聚物，熔融温度119-125℃，在2.16kg载荷下190℃时的熔体流动速率为2.8-3.5g/10min，密度为0.935-0.942g/cm 3。
根据本发明，所述PE电晕层610、所述第一高分子粘合层210、所述热塑性阻隔层950、所述第二高分子粘合层220、所述PE热封层611的含量的重量比为1∶(0.02-0.95)∶(0.02-0.95)∶(0.02-0.95)∶(0.5-2)；优选为1∶(0.1-0.6)∶(0.1-0.6)∶(0.1-0.6)∶(1.0-1.8)。
根据本发明的第三方面，本发明提供了一种前述所述的复合膜的制备方法，其中，所述的制备方法包括：
(1)采用第一物料制备第一层膜810；
(2)采用第二物料制备中间层膜830；
(3)采用第三物料制备PE电晕层610、第四物料制备热塑性阻隔层950、第五物料制备PE热封层611，以及将所述PE电晕层610、所述热塑性阻隔层950和所述PE热封层611依次通过第一高分子粘合层210和第二高分子粘合层220粘合，制备第三层膜850；
(4)将第一层膜810、中间层膜830和第三层膜850依次通过第一胶水层821和第二胶水层822粘合，制备改性聚烯烃复合膜。
根据本发明，所述的制备方法还包括：所述第一层膜810、所述中间层膜830和所述第三层膜850通过共挤出以及拉伸法、吹塑管泡法或流延法制得。
根据本发明，所述第一层膜810选自多层共挤拉伸聚烯烃薄膜、多层共挤流延聚烯烃薄膜和多层共挤吹塑聚烯烃薄膜中的一种或多种。
其中，所述多层共挤拉伸薄膜选自多层共挤单向拉伸聚丙烯(MOPP)薄膜、多层共挤双向拉伸聚丙烯(BOPP)薄膜、多层共挤单向拉伸聚乙烯(MOPE)薄膜和多层共挤双向拉伸聚乙烯(BOPE)薄膜中的任一种。
其中，所述多层共挤流延聚烯烃薄膜为多层共挤流延聚丙烯(CPP)薄膜和/或多层共 挤流延聚乙烯(CPE)薄膜。
其中，所述多层共挤吹塑聚烯烃薄膜为多层共挤吹塑聚丙烯(IPP)薄膜和/或多层共挤吹塑聚乙烯(IPE)薄膜。
根据本发明，优选地，所述功能聚乙烯薄膜810为多层共挤双向拉伸聚乙烯(BOPE)薄膜。
根据本发明，采用蒸镀的方法在所述中间层膜830的表面上镀铝膜。
根据本发明，所述中间层膜830通过共挤出以及单向拉伸法、双向拉伸法或流延法制得，优选地，所述中间层膜830选自多层共挤拉伸聚烯烃蒸镀气化铝膜、多层共挤拉伸聚烯烃蒸镀氧化铝膜、多层共挤流延聚烯烃蒸镀气化铝膜、多层共挤流延聚烯烃蒸镀氧化铝膜中的一种；
其中，所述多层共挤拉伸聚烯烃薄膜是多层共挤单向拉伸聚丙烯(MOPP)薄膜、多层共挤双向拉伸聚丙烯(BOPP)薄膜、多层共挤单向拉伸聚乙烯(MOPE)薄膜、多层共挤双向拉伸聚乙烯(BOPE)薄膜中的任一种；
其中，所述多层共挤流延聚烯烃是多层共挤流延聚丙烯(CPP)薄膜、多层共挤流延聚乙烯(CPE)薄膜中的任一种；
优选地，所述功能聚乙烯薄膜830为多层共挤双向拉伸聚乙烯蒸镀氧化铝膜。
根据本发明，所述第三层膜850通过共挤出以及拉伸法、吹塑管泡法或流延法制得。
优选地，所述第三层膜850为多层共挤流延阻隔薄膜；优选地，为五层共挤流延薄膜；优选地，五层共挤流延阻隔薄膜层结构依次为PE电晕层610、第一高分子粘合层210、热塑性阻隔层950、第二高分子粘合层220、PE热封层611通过挤出机熔融共挤出而成薄膜。
根据本发明的第三方面，本发明提供了一种前述所述的复合膜在食品包装、工业品、日化用品包装和医药及医疗器械中的一种或多种中的应用。
根据本发明的一种优选的具体实施方式，采用本发明的改性聚烯烃复合膜组合物以及本发明的制备方法制备改性聚烯烃复合膜包括：
(1)改性聚烯烃复合膜组合物包括：
第一层膜材：多层共挤双向拉伸聚乙烯(BOPE)薄膜。
中间层膜材：多层共挤双向拉伸聚乙烯蒸镀氧化铝膜。
第三层膜材：
PE电晕层料：第一中密度线性聚乙烯(MLDPE)和第一抗粘连母料；以所述PE电晕层料的总重量为基准，所述第一中密度线性聚乙烯的含量为95.5-96.5重量％，所述第一 抗粘连母料的含量为3.5-4.5重量％。
阻隔层膜料：热塑性聚乙烯醇，在2.16kg载荷下210℃时的熔体流动速率为2.7-2.8g/10min，密度为1.05-1.15g/cm 3。
PE热封层料：第二中密度线性聚乙烯(MLDPE)、茂金属催化聚乙烯(m-LLDPE)、高压聚乙烯(LDPE)、第二抗粘连母料和高分子爽滑母料；以所述PE热封层料的总重量为基准，所述第二中密度线性聚乙烯的含量为29-40重量％，所述茂金属催化聚乙烯的含量为25-27重量％，所述高压聚乙烯的含量为25-30重量％，所述第二抗粘连母料的含量为5-7重量％，所述高分子爽滑母料的含量为5-7重量％。
在2.16kg载荷下190℃时，所述茂金属催化聚乙烯的熔体流动速率为0.5-3.0g/10min，密度为0.86-0.89g/cm 3，所述高压聚乙烯的熔体流动速率为1.5-3.0g/10min，密度为0.89-0.92g/cm 3，所述第一中密度线性聚乙烯和所述第二中密度线性聚乙烯相同，熔体流动速率为1.5-3.0g/10min，密度为0.89-0.92g/cm 3。
第一高分子粘合层210的组分为马来酸酐接枝共聚物；
第二高分子粘合层220的组分为马来酸酐接枝共聚物；
第一胶水层821的组分为聚乙烯醇；
第二胶水层822的组分为聚乙烯醇。
(2)改性聚烯烃复合膜的制备方法
(2-1)由第一层膜材的第一物料通过挤出和双向拉伸法制备第一层膜810；
由中间层膜材通过挤出和双向拉伸法制备成膜后，采用蒸镀氧化铝法制备中间层膜830；
由PE电晕层料通过挤出流延法制备PE电晕层610；
由热塑性聚乙烯醇通过挤出流延法制备阻隔层950；
由PE热封层料通过挤出流延法制备PE热封层611；
(2-2)按照图2所示，将所述PE电晕层610、所述热塑性阻隔层950和所述PE热封层611依次通过第一高分子粘合层210和第二高分子粘合层220粘合，制备第三层膜850；
(4)按照图1所示，将第一层膜810、中间层膜830和第三层膜850依次通过第一胶水层821和第二胶水层822粘合；
其中，PE电晕层610、高分子粘合层210、热塑性阻隔层950、高分子粘合层210、PE热封层611，挤出量比例为1∶(0.1-0.6)∶(0.1-0.6)∶(0.1-0.6)∶(1.0-1.8)；
另外，按照图3所示的流程图，进行涂胶、复合、干燥、固化、制袋：复合上胶量2.8g/m 2 胶水821和822，复合结构为810/胶水/830/胶水/850，复合后经干燥箱后进行干燥，随后在温度48℃±5℃、湿度50％RH以下环境下，静置2天固化；取出后进行分切、制袋；其中，虚框为可选择不进行的工序。
结果制备得到改性聚烯烃复合膜，标记为S1；其中，第一层膜810的厚度为20-30μm；中间层膜830的厚度为20-30μm；第三层膜850的厚度为70-90μm，以及所述改性聚烯烃复合膜的总厚度为110-130μm。
以下将通过实施例对本发明进行详细描述。
以下实施例和对比例中：
(1)耐穿刺强度测试：样品状态调节和试验的标准环境按GB/T 2918规定进行，试验环境条件为温度23℃±2℃，相对湿度50％±1％，按GB/T 37841-2019《塑料薄膜和薄片耐穿刺性测试方法》进行测试。
(2)氧气透过量测试：样品状态调节和试验的标准环境按GB/T 2918规定进行，试验环境条件为温度23℃±2℃，相对湿度50％±1％，按GB/T 1038-2000《塑料薄膜和薄片气体透过性试验方法压差法》进行测试。
(3)水蒸气透过量测试：样品状态调节和试验的标准环境按GB/T 2918规定进行，试验环境条件为温度23℃±2℃，相对湿度50％±1％，按GB/T 1037-1988《塑料薄膜和片材透水蒸气性试验方法杯式法》进行测试。
(4)袋的耐压性能：样品状态调节和试验的标准环境按GB/T 2918规定进行，试验环境条件为温度23℃±2℃，相对湿度50％±1％，按GB/T 10004-2008《包装用塑料复合膜、袋干法复合、挤出复合》进行测试。制成三边封袋，袋与内包装物质量1000g。
(5)袋的跌落性能：样品状态调节和试验的标准环境按GB/T 2918规定进行，试验环境条件为温度23℃±2℃，相对湿度50％±1％，按GB/T 10004-2008《包装用塑料复合膜、袋干法复合、挤出复合》进行测试。袋与内包装物质量1000g，跌落高度为500mm。
实施例1
本实施例在于说明采用本发明的改性聚烯烃复合膜组合物以及本发明的制备方法制备改性聚烯烃复合膜。
(1)改性聚烯烃复合膜组合物包括：
第一层膜材：多层共挤双向拉伸聚乙烯(BOPE)薄膜。
中间层膜材：多层共挤双向拉伸聚乙烯蒸镀氧化铝膜。
第三层膜材：
PE电晕层料：第一中密度线性聚乙烯(MLDPE)和第一抗粘连母料；以所述PE电晕层料的总重量为基准，所述第一中密度线性聚乙烯的含量为96.5重量％，所述第一抗粘连母料的含量为3.5重量％。
阻隔层膜料：热塑性聚乙烯醇，在2.16kg载荷下210℃时的熔体流动速率为2.8g/10min，密度为1.05g/cm 3。
PE热封层料：第二中密度线性聚乙烯(MLDPE)、茂金属催化聚乙烯(m-LLDPE)、高压聚乙烯(LDPE)、第二抗粘连母料和高分子爽滑母料；以所述PE热封层料的总重量为基准，所述第二中密度线性聚乙烯的含量为35重量％，所述茂金属催化聚乙烯的含量为25重量％，所述高压聚乙烯的含量为30重量％，所述第二抗粘连母料的含量为5重量％，所述高分子爽滑母料的含量为5重量％。
在2.16kg载荷下190℃时，所述茂金属催化聚乙烯的熔体流动速率为3.0g/10min，密度为0.89g/cm 3，所述高压聚乙烯的熔体流动速率为3.0g/10min，密度为0.92g/cm 3，所述第一中密度线性聚乙烯和所述第二中密度线性聚乙烯相同，熔体流动速率为3.0g/10min，密度为0.92g/cm 3。
第一高分子粘合层210的组分为马来酸酐接枝共聚物；
第二高分子粘合层220的组分为马来酸酐接枝共聚物；
第一胶水层821的组分为聚乙烯醇；
第二胶水层822的组分为聚乙烯醇。
(2)改性聚烯烃复合膜的制备方法
(2-1)由第一层膜材的第一物料通过挤出和双向拉伸法制备第一层膜810；
由中间层膜材通过挤出和双向拉伸法制备成膜后，采用蒸镀氧化铝法制备中间层膜830；
由PE电晕层料通过挤出流延法制备PE电晕层610；
由聚乙烯醇通过挤出流延法制备阻隔层膜950；
由PE热封层料通过挤出流延法制备PE热封层611；
(2-2)按照图2所示，将所述PE电晕层610、所述热塑性阻隔层950和所述PE热封层611依次通过第一高分子粘合层210和第二高分子粘合层220粘合，制备第三层膜850；
(4)按照图1所示，将第一层膜810、中间层膜830和第三层膜850依次通过第一胶 水层821和第二胶水层822粘合；
其中，PE电晕层610、高分子粘合层210、热塑性阻隔层950、高分子粘合层210、PE热封层611，挤出量比例为1∶0.6∶0.6∶0.6∶1.8；
另外，按照图3所示的流程图，进行涂胶、复合、干燥、固化、制袋：复合上胶量2.8g/m 2胶水821和822，复合结构为810/胶水/830/胶水/850，复合后经干燥箱后进行干燥，随后在温度48℃±5℃、湿度50％RH以下环境下，静置2天固化；取出后进行分切、制袋；其中，虚框为可选择不进行的工序。
结果制备得到改性聚烯烃复合膜，标记为S1；其中，第一层膜810的厚度为20μm；中间层膜830的厚度为20μm；第三层膜850的厚度为80μm，以及所述改性聚烯烃复合膜的总厚度为122μm。
另外，对该改性聚烯烃复合膜进行最大穿刺力、氧气透过量、水蒸气透过量性能测试，结果如表1所示；
另外，对由该改性聚烯烃复合膜制成的袋成品的耐压性能、跌落性能测试，结果如表2所示。
实施例2
本实施例在于说明采用本发明的改性聚烯烃复合膜组合物以及本发明的制备方法制备改性聚烯烃复合膜。
(1)改性聚烯烃复合膜组合物包括：
第一层膜材：多层共挤双向拉伸聚乙烯(BOPE)薄膜。
中间层膜材：多层共挤双向拉伸聚乙烯蒸镀氧化铝膜。
第三层膜材：
PE电晕层料：第一中密度线性聚乙烯(MLDPE)和第一抗粘连母料；以所述PE电晕层料的总重量为基准，所述第一中密度线性聚乙烯的含量为80重量％，所述第一抗粘连母料的含量为20重量。
阻隔层膜料：热塑性聚乙烯醇，在2.16kg载荷下210℃时的熔体流动速率为2.0g/10min，密度为0.92g/cm 3。
PE热封层料：第二中密度线性聚乙烯(MLDPE)、茂金属催化聚乙烯(m-LLDPE)、高压聚乙烯(LDPE)、第二抗粘连母料和高分子爽滑母料；以所述PE热封层料的总重量为基准，所述第二中密度线性聚乙烯的含量为10重量％，所述茂金属催化聚乙烯的含量为30重量％，所述高压聚乙烯的含量为40重量％，所述第二抗粘连母料的含量为10重量％， 所述高分子爽滑母料的含量为10重量％。
在2.16kg载荷下190℃时，所述茂金属催化聚乙烯的熔体流动速率为0.5g/10min，密度为0.86g/cm 3，所述高压聚乙烯的熔体流动速率为1.5g/10min，密度为0.89g/cm 3，所述第一中密度线性聚乙烯和所述第二中密度线性聚乙烯相同，熔体流动速率为1.5g/10min，密度为0.89g/cm 3。
第一高分子粘合层210的组分为马来酸酐接枝共聚物；
第二高分子粘合层220的组分为马来酸酐接枝共聚物；
第一胶水层821的组分为聚乙烯醇；
第二胶水层822的组分为聚乙烯醇。
(2)改性聚烯烃复合膜的制备方法
(2-1)由第一层膜材的第一物料通过挤出和双向拉伸法制备第一层膜810；
由中间层膜材通过挤出和双向拉伸法制备成膜后，采用蒸镀氧化铝法制备中间层膜830；
由PE电晕层料通过挤出流延法制备PE电晕层610；
由聚乙烯醇通过挤出流延法制备阻隔层膜950；
由PE热封层料通过挤出流延法制备PE热封层611；
(2-2)按照图2所示，将所述PE电晕层610、所述热塑性阻隔层950和所述PE热封层611依次通过第一高分子粘合层210和第二高分子粘合层220粘合，制备第三层膜850；
(4)按照图1所示，将第一层膜810、中间层膜830和第三层膜850依次通过第一胶水层821和第二胶水层822粘合；
其中，PE电晕层610、高分子粘合层210、热塑性阻隔层950、高分子粘合层210、PE热封层611，挤出量比例为1∶0.6∶0.6∶0.6∶1.8；
另外，按照图3所示的流程图，进行涂胶、复合、干燥、固化、制袋：复合上胶量10g/m 2胶水821和822，复合结构为810/胶水/830/胶水/850，复合后经干燥箱后进行干燥，随后在温度48℃±5℃、湿度50％RH以下环境下，静置2天固化；取出后进行分切、制袋；其中，虚框为可选择不进行的工序。
结果制备得到改性聚烯烃复合膜，标记为S2；其中，第一层膜810的厚度为20μm；中间层膜830的厚度为20μm；第三层膜850的厚度为80μm，以及所述改性聚烯烃复合膜的总厚度为128μm。
另外，对该改性聚烯烃复合膜进行最大穿刺力、氧气透过量、水蒸气透过量性能测试， 结果如表1所示；
另外，对由该改性聚烯烃复合膜制成的袋成品的耐压性能、跌落性能测试，结果如表2所示。
实施例3
本实施例在于说明采用本发明的改性聚烯烃复合膜组合物以及本发明的制备方法制备改性聚烯烃复合膜。
(1)改性聚烯烃复合膜组合物包括：
第一层膜材：多层共挤双向拉伸聚乙烯(BOPE)薄膜。
中间层膜材：多层共挤双向拉伸聚乙烯蒸镀氧化铝膜。
第三层膜材：
PE电晕层料：第一中密度线性聚乙烯(MLDPE)和第一抗粘连母料；以所述PE电晕层料的总重量为基准，所述第一中密度线性聚乙烯的含量为99.5重量％，所述第一抗粘连母料的含量为0.5重量％。
阻隔层膜料：热塑性聚乙烯醇，在2.16kg载荷下210℃时的熔体流动速率为5g/10min，密度为1.3g/cm 3。
PE热封层料：第二中密度线性聚乙烯(MLDPE)、茂金属催化聚乙烯(m-LLDPE)、高压聚乙烯(LDPE)、第二抗粘连母料和高分子爽滑母料；以所述PE热封层料的总重量为基准，所述第二中密度线性聚乙烯的含量为58.5重量％，所述茂金属催化聚乙烯的含量为20重量％，所述高压聚乙烯的含量为20重量％，所述第二抗粘连母料的含量为0.5重量％，所述高分子爽滑母料的含量为1重量％。
在2.16kg载荷下190℃时，所述茂金属催化聚乙烯的熔体流动速率为4.0g/10min，密度为0.93g/cm 3，所述高压聚乙烯的熔体流动速率为4.0g/10min，密度为0.935g/cm 3，所述第一中密度线性聚乙烯和所述第二中密度线性聚乙烯相同，熔体流动速率为4.5g/10min，密度为0.94g/cm 3。
第一高分子粘合层210的组分为马来酸酐接枝共聚物；
第二高分子粘合层220的组分为马来酸酐接枝共聚物；
第一胶水层821的组分为聚乙烯醇；
第二胶水层822的组分为聚乙烯醇。
(2)改性聚烯烃复合膜的制备方法
(2-1)由第一层膜材的第一物料通过挤出和双向拉伸法制备第一层膜810；
由中间层膜材通过挤出和双向拉伸法制备成膜后，采用蒸镀氧化铝法制备中间层膜830；
由PE电晕层料通过挤出流延法制备PE电晕层610；
由聚乙烯醇通过挤出流延法制备阻隔层膜950；
由PE热封层料通过挤出流延法制备PE热封层611；
(2-2)按照图2所示，将所述PE电晕层610、所述热塑性阻隔层950和所述PE热封层611依次通过第一高分子粘合层210和第二高分子粘合层220粘合，制备第三层膜850；
(4)按照图1所示，将第一层膜810、中间层膜830和第三层膜850依次通过第一胶水层821和第二胶水层822粘合；
其中，PE电晕层610、高分子粘合层210、热塑性阻隔层950、高分子粘合层210、PE热封层611，挤出量比例为1∶0.02∶0.02∶0.02∶1.8；
另外，按照图3所示的流程图，进行涂胶、复合、干燥、固化、制袋：复合上胶量1g/m 2胶水821和822，复合结构为810/胶水/830/胶水/850，复合后经干燥箱后进行干燥，随后在温度48℃±5℃、湿度50％RH以下环境下，静置2天固化；取出后进行分切、制袋；其中，虚框为可选择不进行的工序。
结果制备得到改性聚烯烃复合膜，标记为S3；其中，第一层膜810的厚度为20μm；中间层膜830的厚度为20μm；第三层膜850的厚度为80μm，以及所述改性聚烯烃复合膜的总厚度为120μm。
另外，对该改性聚烯烃复合膜进行最大穿刺力、氧气透过量、水蒸气透过量性能测试，结果如表1所示；
另外，对由该改性聚烯烃复合膜制成的袋成品的耐压性能、跌落性能测试，结果如表2所示。
实施例4
本实施例在于说明采用本发明的改性聚烯烃复合膜组合物以及本发明的制备方法制备改性聚烯烃复合膜。
按照与实施例1相同的方法制备改性聚烯烃复合膜，所不同之处在于：
(1)中间层膜材通过挤出和双向拉伸法制备成膜后，不进行蒸镀氧化铝，制备中间层膜830；
结果制备得到改性聚烯烃复合膜，标记为S4；其中，第一层膜810的厚度为20μm；中间层膜830的厚度为20μm；第三层膜850的厚度为80μm，以及所述改性聚烯烃复合膜 的总厚度为122μm。
另外，对该改性聚烯烃复合膜进行最大穿刺力、氧气透过量、水蒸气透过量性能测试，结果如表1所示；
另外，对由该改性聚烯烃复合膜制成的袋成品的耐压性能、跌落性能测试，结果如表2所示。
实施例5
本实施例在于说明采用本发明的改性聚烯烃复合膜组合物以及本发明的制备方法制备改性聚烯烃复合膜。
按照与实施例1相同的方法制备改性聚烯烃复合膜，所不同之处在于：
(1)810与850的厚度不同。
结果制备得到改性聚烯烃复合膜，标记为S5；其中，第一层膜810的厚度为60μm；中间层膜830的厚度为50μm；第三层膜850的厚度为100μm，以及所述改性聚烯烃复合膜的总厚度为212μm。
另外，对该改性聚烯烃复合膜进行最大穿刺力、氧气透过量、水蒸气透过量性能测试，结果如表1所示；
另外，对由该改性聚烯烃复合膜制成的袋成品的耐压性能、跌落性能测试，结果如表2所示。
实施例6
本实施例在于说明采用本发明的改性聚烯烃复合膜组合物以及本发明的制备方法制备改性聚烯烃复合膜。
按照与实施例1相同的方法制备改性聚烯烃复合膜，所不同之处在于：
(1)810、830、850的厚度不同。
结果制备得到改性聚烯烃复合膜，标记为S6；其中，第一层膜810的厚度为10μm；中间层膜830的厚度为10μm；第三层膜850的厚度为10μm，以及所述改性聚烯烃复合膜的总厚度为32μm。
另外，对该改性聚烯烃复合膜进行最大穿刺力、氧气透过量、水蒸气透过量性能测试，结果如表1所示；
另外，对由该改性聚烯烃复合膜制成的袋成品的耐压性能、跌落性能测试，结果如表2所示。
实施例7
本实施例在于说明采用本发明的改性聚烯烃复合膜组合物以及本发明的制备方法制备改性聚烯烃复合膜。
按照与实施例1相同的方法制备改性聚烯烃复合膜，所不同之处在于：
(1)第一胶水层821、第二胶水层822为聚氨酯双组份胶水；
(2)中间层膜材通过挤出和双向拉伸法制备成膜后，不进行蒸镀氧化铝，制备中间层膜830；
结果制备得到改性聚烯烃复合膜，标记为S7；其中，第一层膜810的厚度为20μm；中间层膜830的厚度为20μm；第三层膜850的厚度为80μm，以及所述改性聚烯烃复合膜的总厚度为122μm。
另外，对该改性聚烯烃复合膜进行最大穿刺力、氧气透过量、水蒸气透过量性能测试，结果如表1所示；
另外，对由该改性聚烯烃复合膜制成的袋成品的耐压性能、跌落性能测试，结果如表2所示。
对比例1
按照与实施例1相同的方法制备改性聚烯烃复合膜，所不同之处在于：
(1)改性聚烯烃复合膜组合物不包括阻隔层膜料；
(2)中间层膜材通过挤出和双向拉伸法制备成膜后，不进行蒸镀氧化铝，制备中间层膜830；
结果制备得到改性聚烯烃复合膜，标记为D1；其中，第一层膜810的厚度为20μm；中间层膜830的厚度为20μm；第三层膜850的厚度为80μm，以及所述改性聚烯烃复合膜的厚度为122μm。
另外，对该改性聚烯烃复合膜进行最大穿刺力、氧气透过量、水蒸气透过量性能测试，结果如表1所示；
另外，对由该改性聚烯烃复合膜制成的袋成品的耐压性能、跌落性能测试，结果如表2所示。
对比例2
按照与实施例1相同的方法制备改性聚烯烃复合膜，所不同之处在于：
(1)PE电晕层(610)、高分子粘合层(210)、热塑性阻隔层(950)、高分子粘合层(210)、PE热封层(611)，挤出量比例为1∶1.0∶1.0∶1.0∶1.8。
(2)第一胶水层821、第二胶水层822为改性聚烯烃胶粘剂；
(3)中间层膜材通过挤出和双向拉伸法制备成膜后，不进行蒸镀氧化铝，制备中间层膜830；
结果制备得到改性聚烯烃复合膜，标记为D2；其中，第一层膜810的厚度为20μm；中间层膜830的厚度为20μm；第三层膜850的厚度为80μm，以及所述改性聚烯烃复合膜的厚度为128μm。
另外，对该改性聚烯烃复合膜进行最大穿刺力、氧气透过量、水蒸气透过量性能测试，结果如表1所示；
另外，对由该改性聚烯烃复合膜制成的袋成品的耐压性能、跌落性能测试，结果如表2所示。
对比例3
按照与实施例1相同的方法制备改性聚烯烃复合膜，所不同之处在于：
只有聚烯烃面层薄膜810：多层共挤双向拉伸聚乙烯薄膜。
结果制备得到改性聚烯烃复合膜，标记为D3；其中，第一层膜810的厚度为30μm。
另外，对该改性聚烯烃复合膜进行最大穿刺力、氧气透过量、水蒸气透过量性能测试，结果如表1所示；
另外，对由该改性聚烯烃复合膜制成的袋成品的耐压性能、跌落性能测试，结果如表2所示。
对比例4
按照与实施例1相同的方法制备改性聚烯烃复合膜，所不同之处在于：
只有聚烯烃面层薄膜810：多层共挤双向拉伸聚丙烯薄膜。
结果制备得到改性聚烯烃复合膜，标记为D4；其中，第一层膜810的厚度为30μm。
另外，对该改性聚烯烃复合膜进行最大穿刺力、氧气透过量、水蒸气透过量性能测试，结果如表1所示；
另外，对由该改性聚烯烃复合膜制成的袋成品的耐压性能、跌落性能测试，结果如表2所示。
对比例5
按照与实施例1相同的方法制备改性聚烯烃复合膜，所不同之处在于：
只有聚烯烃面层薄膜810：多层共挤流延聚乙烯薄膜。
结果制备得到改性聚烯烃复合膜，标记为D5；其中，第一层膜810的厚度为30μm。
另外，对该改性聚烯烃复合膜进行最大穿刺力、氧气透过量、水蒸气透过量性能测试，结果如表1所示；
另外，对由该改性聚烯烃复合膜制成的袋成品的耐压性能、跌落性能测试，结果如表2所示。
对比例6
按照与实施例1相同的方法制备改性聚烯烃复合膜，所不同之处在于：
只有聚烯烃面层薄膜810：多层共挤流延聚丙烯薄膜。
结果制备得到改性聚烯烃复合膜，标记为D6；其中，第一层膜810的厚度为30μm。
另外，对该改性聚烯烃复合膜进行最大穿刺力、氧气透过量、水蒸气透过量性能测试，结果如表1所示；
另外，对由该改性聚烯烃复合膜制成的袋成品的耐压性能、跌落性能测试，结果如表2所示。
对比例7
按照与实施例1相同的方法制备改性聚烯烃复合膜，所不同之处在于：
(1)改性聚烯烃复合膜组合物不包括中间层膜料；
(2)改性聚烯烃复合膜的制备方法
将第一层膜810和第三层膜850依次通过第一胶水层821和第二胶水层822粘合；
结果制备得到改性聚烯烃复合膜，标记为D7；其中，第一层膜810的厚度为20μm；中间层膜830的厚度为0μm；第三层膜850的厚度为80μm，以及所述改性聚烯烃复合膜的厚度为101μm。
另外，对该改性聚烯烃复合膜进行最大穿刺力、氧气透过量、水蒸气透过量性能测试，结果如表1所示；
另外，对由该改性聚烯烃复合膜制成的袋成品的耐压性能、跌落性能测试，结果如表2所示。
对比例8
按照与实施例1相同的方法制备改性聚烯烃复合膜，所不同之处在于：
(1)改性聚烯烃复合膜组合物不包括第一层膜材；
(2)改性聚烯烃复合膜的制备方法
将中间层膜830和第三层膜850依次通过第一胶水层821和第二胶水层822粘合；
结果制备得到改性聚烯烃复合膜，标记为D8；其中，第一层膜810的厚度为0μm； 中间层膜830的厚度为20μm；第三层膜850的厚度为80μm，以及所述改性聚烯烃复合膜的厚度为101μm。
另外，对该改性聚烯烃复合膜进行最大穿刺力、氧气透过量、水蒸气透过量性能测试，结果如表1所示；
另外，对由该改性聚烯烃复合膜制成的袋成品的耐压性能、跌落性能测试，结果如表2所示。
对比例9
按照与实施例1相同的方法制备改性聚烯烃复合膜，所不同之处在于：
(1)改性聚烯烃复合膜组合物不包括PE电晕层料、阻隔层膜料和PE热封层料；
(2)改性聚烯烃复合膜的制备方法
将第一层膜810和中间层膜830依次通过第一胶水层821和第二胶水层822粘合；
结果制备得到改性聚烯烃复合膜，标记为D9；其中，第一层膜810的厚度为20μm；中间层膜830的厚度为20μm；第三层膜850的厚度为0μm，以及所述改性聚烯烃复合膜的厚度为41μm。
另外，对该改性聚烯烃复合膜进行最大穿刺力、氧气透过量、水蒸气透过量性能测试，结果如表1所示；
另外，对由该改性聚烯烃复合膜制成的袋成品的耐压性能、跌落性能测试，结果如表2所示。
表1
Figure PCTCN2021098847-appb-000001
Figure PCTCN2021098847-appb-000002
通过表1的结果可以看出，采用本发明的技术方案的实施例及对比例的阻隔性和抗穿刺性测试结果表明：多层共挤双向拉伸聚乙烯薄膜厚度比例占比越大，最大穿刺力越大；同样条件下，胶水固含量比例大，复合包装趋变硬脆，最大穿刺力下降；聚乙烯的最大穿刺力大于聚丙烯薄膜。
(2)氧气透过量：
测试结果表明：
薄膜蒸镀氧化铝层可获得优异的阻隔氧气性。
多层共挤流延聚乙烯阻隔薄膜的阻隔层越厚，阻隔性越好。
聚乙烯醇胶水阻氧气性高于市售普通胶水；聚乙烯醇胶水涂胶量越大，阻氧气性越好。
聚丙烯由于有侧甲基，空间位阻大，同样的薄膜制造工艺条件下，聚丙烯的阻隔氧气性优于聚乙烯。
(3)水蒸气透过量：
测试结果表明：
薄膜蒸镀氧化铝层可获得优异的阻隔水蒸气性。
聚烯烃薄膜、聚烯烃蒸镀氧化铝薄膜阻水蒸气性好。与热塑性聚乙烯醇阻隔层的阻隔性起到正向叠加作用，阻水蒸气性最好。双向拉伸聚乙烯薄膜厚度比例占比越大，阻水蒸气性越好。
聚丙烯由于有侧甲基，空间位阻大，同样的薄膜制造工艺条件下，聚丙烯的阻隔水蒸气性优于聚乙烯。
表2
项目 袋的耐压性 袋的跌落性
实施例1 无渗漏，不破裂 不破裂
实施例2 无渗漏，不破裂 不破裂
实施例3 渗漏，破裂 破裂
实施例4 无渗漏，不破裂 不破裂
实施例5 无渗漏，不破裂 不破裂
实施例6 渗漏，破裂 破裂
实施例7 无渗漏，不破裂 不破裂
对比例1 无渗漏，不破裂 不破裂
对比例2 无渗漏，不破裂 不破裂
对比例3 破裂 破裂
对比例4 破裂 破裂
对比例5 不破裂 不破裂
对比例6 破裂 不破裂
对比例7 无渗漏，不破裂 不破裂
对比例8 无渗漏，不破裂 不破裂
对比例9 渗漏，破裂 破裂
从表2可以看出：
多层共挤流延阻隔薄膜850的非电晕层(热封层)层厚比例越高，以及胶水820涂胶量合适的条件下，热封强度高，层间剥离强度高，袋子耐压性好，抗跌落性强。袋子不渗漏、不破裂。
多层共挤流延阻隔薄膜850的非电晕层(热封层)层厚比例低或无，以及胶水820涂胶量少或无的条件下，热封强度低，层间剥离强度低，袋子耐压性差，抗跌落性差。袋子渗漏、破裂。
聚烯烃面层薄膜810中，多层共挤双向拉伸聚乙烯、多层共挤双向拉伸聚丙烯薄膜经过拉伸，分子链排列整齐，结晶度高，无热封，因此袋子耐压性差，抗跌落性差。袋子渗漏、破裂；多层共挤流延聚乙烯薄膜未经过拉伸，分子链柔顺，热粘合强度略高于多层共挤流延 聚丙烯薄膜。因此袋子耐压性稍好，抗跌落性稍强。袋子不渗漏、不破裂。
以上详细描述了本发明的优选实施方式，但是，本发明并不限于此。在本发明的技术构思范围内，可以对本发明的技术方案进行多种简单变型，包括各个技术特征以任何其它的合适方式进行组合，这些简单变型和组合同样应当视为本发明所公开的内容，均属于本发明的保护范围。

Claims (12)

  1. 一种改性聚烯烃复合膜组合物，其特征在于，所述组合物包括第一层膜材、中间层膜材和第三层膜材，以及所述第三层膜材包括PE电晕层料、阻隔层膜料和PE热封层料；
    其中，所述第一层膜材和所述中间层膜材均各自包括C 4-C 8的聚乙烯、一元均聚聚丙烯、二元共聚聚丙烯和三元共聚聚丙烯中的一种或多种；以及所述阻隔层膜料含有乙烯-乙烯醇共聚物和/或热塑性聚乙烯醇。
  2. 根据权利要求1所述的组合物，其中，所述阻隔层料为热塑性聚乙烯醇；
    优选地，所述热塑性聚乙烯醇在2.16kg载荷下210℃时的熔体流动速率为2-5g/10min，密度为0.92-1.3g/cm 3；
    优选地，所述热塑性聚乙烯醇在2.16kg载荷下210℃时的熔体流动速率为2.5-4g/10min，密度为1-1.28g/cm 3。
  3. 根据权利要求1所述的组合物，其中，所述PE电晕层料含有第一中密度线性聚乙烯和第一抗粘连母料；
    优选地，以所述PE电晕层料的总重量为基准，所述第一中密度线性聚乙烯的含量为80-99.5重量％，所述第一抗粘连母料的含量为0.5-20重量％。
  4. 根据权利要求1所述的组合物，其中，所述PE热封层料含有第二中密度线性聚乙烯、茂金属催化聚乙烯、高压聚乙烯、第二抗粘连母料和高分子爽滑母料中的一种或多种；
    优选地，以所述PE热封层料的总重量为基准，所述第二中密度线性聚乙烯的含量为10-58.5重量％，所述茂金属催化聚乙烯的含量为20-30重量％，所述高压聚乙烯的含量为20-40重量％，所述第二抗粘连母料的含量为0.5-10重量％，所述高分子爽滑母料的含量为1-10重量％；
    优选地，所述茂金属催化聚乙烯为C 6-C 8茂金属催化聚乙烯，优选地，所述茂金属催化聚乙烯在2.16kg载荷下190℃时的熔体流动速率为0.5-4.0g/10min，密度为0.86-0.930g/cm 3；
    优选地，所述高压聚乙烯在2.16kg载荷下190℃时的熔体流动速率为1.5-4.0g/10min，密度为0.89-0.935g/cm 3；
    优选地，所述高分子爽滑母料为共混物E经共混改性制备得到，其中，所述共混物E中含有可选的硅硐、芥酸酰胺和第三中密度线性聚乙烯；
    优选地，以所述共混物E总重量为基准，所述硅硐的含量为0-20重量％；所述芥酸酰胺的含量为0.5-10重量％，所述第三中密度线性聚乙烯的含量为70-99.5重量％；
    优选地，所述第一中密度线性聚乙烯、所述第二中密度线性聚乙烯和所述第三中密度线性聚乙烯相同或不同，各自在2.16kg载荷下190℃时的熔体流动速率为1.5-4.5g/10min，密度为0.87-0.940g/cm 3；
    优选地，在2.16kg载荷下190℃时的熔体流动速率为1.5-3.5g/10min，密度为0.89-0.92g/cm 3。
  5. 一种由权利要求1-4中任意一项所述的组合物制得的阻隔聚烯烃复合膜，其特征在于，所述复合膜包括依次叠加的第一层膜(810)、中间层膜(830)和第三层膜(850)，以及所述第一层膜(810)由含有第一层膜材的第一物料挤出得到；所述中间层膜(830)由含有中间层膜材的第二物料挤出得到；
    其中，所述第三层膜(850)包括依次叠加的PE电晕层(610)、热塑性阻隔层(950)和PE热封层(611)；以及所述PE电晕层(610)由含有PE电晕层料的第三物料挤出得到；所述热塑性阻隔层(950)由含有热塑性乙烯-乙烯醇共聚物和/或热塑性聚乙烯醇的第四物料挤出得到；所述PE热封层(611)由含有PE热封层料的第五物料挤出得到。
  6. 根据权利要求5所述的复合膜，其中，所述中间层膜(830)的表面上还镀有铝膜，优选地，所述铝膜包括气化铝膜和/或氧化铝膜。
  7. 根据权利要求5所述的复合膜，其中，所述第一层膜(810)的厚度为5-80μm；所述第二层膜(830)的厚度为5-150μm；所述第三层膜(850)的厚度为5-200μm；
    优选地，所述第一层膜(810)的厚度为9-60μm；所述第二层膜(830)的厚度为10-50μm；所述第三层膜(850)的厚度为40-100μm；
    优选地，所述复合膜的总厚度为15-430μm，优选为59-150μm。
  8. 根据权利要求5-7中任意一项所述的复合膜，其中，所述复合膜还包括依次叠加的第一层膜(810)、第一胶水层(821)、中间层膜(830)、第二胶水层(822)和第三层膜(850)；
    优选地，所述第一胶水层(821)和所述第二胶水层(822)相同或不同，各自为聚乙烯醇复配胶水、聚氨酯双组份胶水和改性聚烯烃胶粘剂中的一种或多种，优选为聚乙烯醇复配胶水；
    优选地，所述聚乙烯醇复配胶水包括聚乙烯醇主剂和固化剂，且以所述聚乙烯醇复配胶水的总重量为基准，聚乙烯醇主剂的固含量为15-32重量％，固化剂的固含量为10-25重量％；
    优选地，聚乙烯醇主剂与所述固化剂的配比为10∶(0.5-1.5)；
    优选地，所述第一胶水层(821)和所述第二胶水层(822)各自的上胶量为1-10g/m 2，优选为2.5-5g/m 2。
  9. 根据权利要求5-7中任意一项所述的复合膜，其中，所述第三层膜(850)还包括依次叠加的PE电晕层(610)、第一高分子粘合层(210)、热塑性阻隔层(950)、第二高分子粘合层(220)和PE热封层(611)；
    优选地，所述PE电晕层(610)、所述第一高分子粘合层(210)、所述热塑性阻隔层(950)、所述第二高分子粘合层(220)、所述PE热封层(611)的含量的重量比为1∶(0.02-0.95)∶(0.02-0.95)∶(0.02-0.95)∶(0.5-2)；优选为1∶(0.1-0.6)∶(0.1-0.6)∶(0.1-0.6)∶(1.0-1.8)。
  10. 一种权利要求5-9中任意一项所述的复合膜的制备方法，其特征在于，所述的制备方法包括：
    (1)采用第一物料制备第一层膜(810)；
    (2)采用第二物料制备中间层膜(830)；
    (3)采用第三物料制备PE电晕层(610)、第四物料制备热塑性阻隔层(950)、第五物料制备PE热封层(611)，以及将所述PE电晕层(610)、所述热塑性阻隔层(950)和所述PE热封层(611)依次通过第一高分子粘合层(210)和第二高分子粘合层(220)粘合，制备第三层膜(850)；
    (4)将第一层膜(810)、中间层膜(830)和第三层膜(850)依次通过第一胶水层(821)和第二胶水层(822)粘合，制备改性聚烯烃复合膜。
  11. 根据权利要求10所述的方法，其中，所述的制备方法还包括：所述第一层膜(810)、所述中间层膜(830)和所述第三层膜(850)通过共挤出以及拉伸法、吹塑管泡法或流延法制得；
    优选地，采用蒸镀的方法在所述中间层膜(830)的表面上镀铝膜。
  12. 一种权利要求5-9中任意一项所述的复合膜在食品包装、工业品、日化用品包装和医药及医疗器械中的一种或多种中的应用。
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