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WO2018109747A1 - Film barrière et son procédé de préparation - Google Patents

Film barrière et son procédé de préparation Download PDF

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Publication number
WO2018109747A1
WO2018109747A1 PCT/IB2017/058027 IB2017058027W WO2018109747A1 WO 2018109747 A1 WO2018109747 A1 WO 2018109747A1 IB 2017058027 W IB2017058027 W IB 2017058027W WO 2018109747 A1 WO2018109747 A1 WO 2018109747A1
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Prior art keywords
range
barrier film
molecular weight
machine direction
ultra
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Ceased
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PCT/IB2017/058027
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English (en)
Inventor
Ajit Behari Mathur
Satya Srinivasa Rao GANDHAM
Devesh Kumar SHUKLA
Mahuya BAGUI
Yogesh Popatrao PATIL
Raksh Vir Jasra
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Reliance Industries Ltd
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Reliance Industries Ltd
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Publication of WO2018109747A1 publication Critical patent/WO2018109747A1/fr
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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/04—Homopolymers or copolymers of ethene
    • C08L23/06—Polyethene
    • 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
    • B32B27/18—Layered products comprising a layer of synthetic resin characterised by the use of special additives
    • 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
    • B32B27/18—Layered products comprising a layer of synthetic resin characterised by the use of special additives
    • B32B27/20—Layered products comprising a layer of synthetic resin characterised by the use of special additives using fillers, pigments, thixotroping agents
    • 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
    • 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
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18—Manufacture of films or sheets
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2250/00—Layers arrangement
    • B32B2250/02—2 layers
    • 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
    • B32B2250/00—Layers arrangement
    • B32B2250/24—All layers being polymeric
    • B32B2250/242—All polymers belonging to those covered by group B32B27/32
    • 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
    • B32B2264/00—Composition or properties of particles which form a particulate layer or are present as additives
    • B32B2264/10—Inorganic particles
    • B32B2264/102—Oxide or hydroxide
    • 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
    • B32B2264/00—Composition or properties of particles which form a particulate layer or are present as additives
    • B32B2264/10—Inorganic particles
    • B32B2264/104—Oxysalt, e.g. carbonate, sulfate, phosphate or nitrate particles
    • 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
    • B32B2264/00—Composition or properties of particles which form a particulate layer or are present as additives
    • B32B2264/10—Inorganic particles
    • B32B2264/107—Ceramic
    • B32B2264/108—Carbon, e.g. graphite particles
    • 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
    • B32B2307/50—Properties of the layers or laminate having particular mechanical properties
    • B32B2307/546—Flexural strength; Flexion stiffness
    • 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
    • B32B2307/704—Crystalline
    • 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
    • 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
    • B32B2307/732—Dimensional properties
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2323/04—Homopolymers or copolymers of ethene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2203/00—Applications
    • C08L2203/16—Applications used for films
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2207/00—Properties characterising the ingredient of the composition
    • C08L2207/06—Properties of polyethylene
    • C08L2207/068—Ultra high molecular weight polyethylene

Definitions

  • the present disclosure relates to a barrier film.
  • Ultra-high molecular weight polyethylene is a polyethylene with a viscosity average molecular weight (molecular weight) in the range of 0.5 million g mol -1 to 15 million g mol 1 , bulk density in the range of 0.03 g cm “J 3 to 0.2 g cm “ 3 , crystallinity in the range of 85% to 97% and melt temperature in the range of 141 °C to 145 °C.
  • a barrier film can be a monolayer barrier film or a multilayer barrier film.
  • a monolayer barrier film comprises a single layer of solid-state, hot stretched ultra-high molecular weight polyethylene.
  • a multilayer barrier film comprises multiple layers of solid-state compacted, hot stretched ultra-high molecular weight polyethylene.
  • Solid State compaction is a compaction process of a polymeric material below its melt temperature.
  • Barrier performance of a polymeric film means its ability to resist permeation of small molecules like (3 ⁇ 4, N 2 , C(3 ⁇ 4, moisture, organic fluid and other gases such as inert gases.
  • the barrier performance is assessed in terms of permeation rates of (3 ⁇ 4, N 2 , CO 2 , moisture, organic fluid and other gases such as inert gases across the film.
  • Machine direction is a direction parallel to the direction of the input and the output in a calendering machine.
  • Stretching ratio in the machine direction Stretching ratio in the machine direction is the relative change in the length of a film caused by stretching in the machine direction.
  • Stretching ratio transverse to the machine direction Stretching ratio transverse to the machine direction is the relative change in the width of a film caused by stretching transverse to the machine direction at an angle in the range of 1° to 179°.
  • Plastic products are widely used for general purpose and engineering applications, due to their light weight, ease of processability and an excellent strength-to-weight ratio.
  • plastic products with properties that comprise odor/fragrance barrier and resistant to the permeation of gases and liquids, especially, in the field of packaging material for food and other industrial products.
  • the barrier performance of a polymeric film means its ability to resist permeation of small molecules like (3 ⁇ 4, N 2 , C(3 ⁇ 4, moisture, organic fluid and other gases such as inert gases.
  • Permeation rate is the volume or mass of small molecules passing through a plastic film of certain thickness at a given pressure, temperature and humidity conditions, per unit time per unit area.
  • a low permeation rate of a small molecule through a barrier film indicates better barrier performance of the film, thereby making it a suitable candidate for specific applications.
  • a film of a polymeric material having a low oxygen permeation rate is an excellent candidate for use as a packaging material for food products that are prone to decomposition in the presence of oxygen.
  • a low C(3 ⁇ 4 permeation rate is needed for a polymeric film to be used as a material for packaging carbonated beverages.
  • An object of the present disclosure is to provide a barrier film having high barrier performance.
  • Another object of the present disclosure is to provide a barrier film having high strength.
  • Still another object of the present disclosure is to provide a multilayer barrier film made from a single polymeric material.
  • Still another object of the present disclosure is to provide a barrier film which is easy to manufacture, process and recycle.
  • Still another object of the present disclosure is to provide a process for preparing a barrier film having high barrier performance and high strength.
  • a barrier film comprising at least one layer of solid state compacted, hot stretched ultra-high molecular weight polyethylene.
  • the ultra-high molecular weight polyethylene has molecular weight in the range of 0.5 million
  • the barrier film has a thickness in the range of 5.0 ⁇ to 300 ⁇ .
  • the barrier film comprises at least one layer of solid state compacted, hot stretched ultra-high molecular weight polyethylene having molecular weight in the range of 3.5 million g.mol - " 1 to 5.5 million g.mol - “ 1 , bulk density in the range of 0.05 g cm “ -3 J to 0.1 g.cm - “ 3 and crystallinity in the range of 90% to 95%, wherein the barrier film has a thickness in the range of 35 ⁇ to 250 ⁇ .
  • the barrier film has an oxygen permeation rate in the range of 1.0 cm 3.m- " 2.day - “ 1 to 75 cm 3.m- " 2.day - “ 1 , nitrogen permeation rate in the range of 1.0 cm 3.m- " 2.day - “ 1 to 20 cm 3.m- " 2.day - “ 1 , moisture vapor permeation rate in the range of 0.01 g.m - " 2.day- “ 1 to 0.7 g.m - " 2.day - “ 1 , tensile strength in the range of 500 kg.cm - " 2 to 2500 kg.cm - " 2 and tensile modulus in the range of 1000 kg.cm -2'to 40000 kg .cm -2.
  • the barrier film has an oxygen permeation rate in the range of 40 cm 3 .m "2 .day _1 to
  • the barrier film is a multilayer barrier film comprising at least two layers of solid state compacted, hot stretched ultra-high molecular weight polyethylene.
  • At least two layers of solid state compacted ultra-high molecular weight polyethylene are stacked one on the top of the other in the machine direction, fused and hot stretched.
  • the ultra-high molecular weight polyethylene comprises at least one stabilizer in an amount in the range of 1000 ppm to 8000 ppm.
  • the stabilizer is selected from the group consisting of substituted phenols, amines, alkyl phosphites/phosphonites, aryl phosphites/phosphonites, alkyl-aryl phosphites/phosphonites, alkyl phosphates, aryl phosphates, alkyl-aryl phosphates, lactones, thioesters, thio compounds containing oxidizable sulphur and aryl nitroso compounds,
  • the stabilizer is selected from the group consisting of tetrakis(2,4-di-tert- butylphenyl)-4, 4' -bisphenylene diphosphonite, bis(2,4-di-t-butylphenyl)pentaerythritol diphosphate, tris(2,4-di-t-butylphenyl)phosphate, bis(2,2,6,6-tetramethyl-4- piperidinyl)sebacate, 2,4,6-tri-t-butylphenyl 2-butyl-2-ethy 1-1, 3 -propanediol phosphate, octadecyl 3,5 di-tert-butyl-4-hydroxyhydrocinnamate, 5,7-di-tert-butyl-3-(3,4- dimethylphenyl)-3H-benzofuran-2-one, pentaerythritol tetrakis(3,5-di-tert-
  • a process for preparing the barrier film comprises the following steps:
  • the step of solid state compacting comprises a process selected from the group consisting of compression molding and calendaring.
  • the first predetermined temperature and the second predetermined temperature are temperatures independently selected from temperatures greater than 100° C and less than the melt temperature of the ultra-high molecular weight polyethylene.
  • step (b) the hot stretching in the machine direction and the hot stretching transverse to the machine direction at the angle in the range of 1° to 179° are achieved in batch mode or continuous mode.
  • step (b) the hot stretching in the machine direction and the hot stretching transverse to the machine direction at the angle in the range of 1° to 179° are done sequentially.
  • step (b) the hot stretching in the machine direction and the hot stretching transverse to the machine direction at the angle in the range of 1° to 179° are done simultaneously.
  • the hot stretching in the machine direction and the hot stretching transverse to the machine direction at the angle in the range of 1° to 179° are done iteratively.
  • step (b) the ratio of stretching ratio in the machine direction to the stretching ratio transverse to the machine direction at an angle in the range of 1° to 179° is in the range of 1 :0.11 to 1 : 1.
  • a process for preparing the barrier film wherein the barrier film is a multilayer barrier film.
  • the process comprises the following steps:
  • An ideal polymeric barrier film requires a combination of properties such as gas and liquid permeation resistance, low moisture permeation, good mechanical properties like high tensile strength and high tensile modulus, optical clarity and good sealing strength which are critical for packaging applications.
  • properties such as gas and liquid permeation resistance, low moisture permeation, good mechanical properties like high tensile strength and high tensile modulus, optical clarity and good sealing strength which are critical for packaging applications.
  • several multilayered laminates comprising layers prepared from different polymers are prepared and used in such packaging applications.
  • such multilayered laminates prepared from different polymers are difficult to manufacture and require expensive machinery. Therefore, it is desirable to obtain a barrier film having these desired properties, and it is desired that the barrier film is easy to manufacture, process and recycle.
  • the present disclosure therefore envisages a barrier film having high barrier performance and high strength.
  • the present disclosure provides a barrier film comprising at least one layer of solid state compacted, hot stretched ultra-high molecular weight polyethylene having molecular weight in the range of 0.5 million g.mol "1 to 15 million g.moi "1 , bulk density in the
  • the barrier film has a thickness in the range of 5.0 ⁇ to 300 ⁇ .
  • the barrier film comprises at least one layer of solid state compacted, hot stretched ultra-high molecular weight polyethylene having molecular weight in the range of 3.5 million g.mol “1 to 5.5 million g.mol “1 , bulk density in the range of 0.05 g cm “3 to 0.1 g.cm “ and crystallinity in the range of 90% to 95%, wherein the barrier film has a thickness in the range of 35 ⁇ to 250 ⁇ .
  • the barrier film has an oxygen permeation rate in the range of 1.0 cm 3.m- " 2.day - “ 1 to 75 cm 3.m- " 2.day - “ 1 , nitrogen permeation rate in the range of 1.0 cm 3.m- " 2.day - “ 1 to 20 cm 3.m- " 2.day - “ 1 , moisture vapor permeation rate in the range of 0.01 g.m - " 2.day- “ 1 to 0.7 g.m - " 2.day - “ 1 , tensile strength in the range of 500 kg.cm - " 2 to
  • the barrier film has an oxygen permeation rate in the range of 40 cm 3.m - " 2.day - " 1 to
  • the oxygen permeation rate of the barrier film is 53.4 cm 3 m - " 2 day - " 1. In another embodiment, the oxygen permeation rate of the barrier film is 45 cm 3 m - " 2 day - " 1.
  • the barrier film has a nitrogen permeation rate of 10.7 cm 3 m “2 .day “ ⁇ In another embodiment, the barrier film has a nitrogen permeation rate of 9.0 cm 3 m - “ 2.day - “ 1. In an embodiment, the barrier film has a moisture vapor permeation rate of 0.5 g m " day “ . In another embodiment, the barrier film has a moisture vapor permeation rate of 0.3 g m "2 day “1 .
  • the crystallinity of the barrier film is in the range of 95 % to 98%.
  • the permeation rates for oxygen, nitrogen and moisture of the barrier film are inversely related to the thickness of the barrier film.
  • the thicker barrier films have lower oxygen permeation rate, nitrogen permeation rate and moisture vapor permeation rate than relatively thinner barrier films.
  • the barrier performance of the barrier film improves with the thickness of the barrier film.
  • the tensile strength and tensile modulus of the barrier film are inversely related to the thickness of the barrier film.
  • the thinner barrier films have higher tensile strength and tensile modulus than relatively thicker barrier films as the stretch ratio of a thin film is higher than a thick film.
  • the mechanical properties of the barrier film improve with decrease in thickness of the barrier films.
  • the barrier film is a monolayer barrier film comprising a single layer of ultra-high molecular weight polyethylene that is solid state compacted and hot stretched.
  • the barrier film is a multilayer barrier film comprising multiple layers of ultra-high molecular weight polyethylene that are solid state compacted and hot stretched.
  • the barrier film is a multilayer film comprising at least two layers of solid state compacted, hot stretched ultra-high molecular weight polyethylene, wherein the at least two layers of solid state compacted ultra-high molecular weight polyethylene are stacked one on the top of the other in the machine direction, fused and hot stretched.
  • the ultra-high molecular weight polyethylene comprises at least one stabilizer in an amount in the range of 1000 ppm to 8000 ppm.
  • the stabilizer is at least one selected from the group consisting of substituted phenols, amines, alkyl phosphites/phosphonites, aryl phosphites/phosphonites, alkyl-aryl phosphites/phosphonites, alkyl phosphates, aryl phosphates, alkyl-aryl phosphates, lactones, thioesters, thio compounds containing oxidizable sulphur and aryl nitroso compounds.
  • the stabilizer is preferably selected from the group consisting of tetrakis(2,4-di- tert-butylphenyl)-4, 4' -bisphenylene diphosphonite, bis(2,4-di-t-butylphenyl)pentaerythritol diphosphate, tris(2,4-di-t-butylphenyl)phosphate, bis(2,2,6,6-tetramethyl-4- piperidinyl)sebacate, 2,4,6-tri-t-butylphenyl 2-butyl-2-ethy 1-1, 3 -propanediol phosphate, octadecyl 3,5 di-tert-butyl-4-hydroxyhydrocinnamate, 5,7-di-tert-butyl-3-(3,4- dimethylphenyl)-3H-benzofuran-2-one, pentaerythritol tetrakis(3,5-di-di-
  • the ultra-high molecular weight polyethylene comprises at least one filler selected from the group consisting of carbon black, talc, calcium carbonate and carbon nanotubes.
  • the barrier film prepared without the use of filler is transparent.
  • the present disclosure provides a process for preparing the barrier film.
  • the process comprises the following steps:
  • the step of solid state compacting comprises a process selected from the group consisting of compression molding and calendaring.
  • the compression molding is carried out at a pressure in the range of 50 bar to 250 bar. In an exemplary embodiment, the compression molding is carried out at a pressure of 200 bar.
  • the first predetermined temperature and the second predetermined temperature are temperatures independently selected from temperatures greater than 100° C and less than the melt temperature of the ultra-high molecular weight polyethylene. In one embodiment of the present disclosure, the first predetermined temperature is 128 °C. In another embodiment of the present disclosure, the first predetermined temperature is 125 °C.
  • the second predetermined temperature is 135 °C. In another embodiment of the present disclosure, the second predetermined temperature is 125 °C. In yet another embodiment of the present disclosure, the second predetermined temperature is 138 °C.
  • the hot stretching in the machine direction and the hot stretching transverse to the machine direction at the angle in the range of 1° to 179° is achieved in batch mode. In another embodiment of the present disclosure, the hot stretching in the machine direction and the hot stretching transverse to the machine direction at the angle in the range of 1° to 179° is achieved in continuous mode.
  • the hot stretching in the machine direction and the hot stretching transverse to the machine direction at the angle in the range of 1° to 179° are done sequentially. In another embodiment of the present disclosure, the hot stretching in the machine direction and the hot stretching transverse to the machine direction at the angle in the range of 1° to 179° are done simultaneously.
  • the hot stretching is achieved by means of a roller assembly.
  • Other suitable devices can also be used for hot stretching in place of the roller assembly.
  • the hot stretching in the machine direction and the hot stretching transverse to the machine direction at the angle in the range of 1° to 179° are done iteratively.
  • the number of iterations is in the range of 2 to 5 until a barrier film with thickness in the range of 5.0 ⁇ to 300 ⁇ is obtained.
  • the ratio of stretching ratio in the machine direction to stretching ratio transverse to the machine direction at an angle in the range of 1° to 179° is in the range of 1 :0.11 to 1 :1.
  • a process for preparation of the barrier film wherein the barrier film is multilayer barrier film.
  • the process comprises the following steps:
  • the present disclosure provides a barrier film having high barrier performance, which is observed from the low permeation rates for oxygen, nitrogen and moisture vapor.
  • the barrier film also displays high strength which is observed from high values of tensile strength and tensile modulus.
  • the barrier film of the present disclosure is prepared from a single polymer i.e. UHMWPE. Due to the use of a single polymer, the barrier film is homogeneous and easy to use. This property is in contrast to the conventional barrier films prepared from two or more polymers. These conventional barrier films are non-homogeneous. Due to homogeneity, the barrier films of the present disclosure are easy to manufacture and recycle as it avoids the use of multiple polymeric materials.
  • the required processing machine and tools for processing film as per the present disclosure are simple and are relatively low cost.
  • the present disclosure is further described in light of the following experiments which are set forth for illustration purpose only and not to be construed for limiting the scope of the disclosure. The following experiments can be scaled up to industrial/commercial scale and the results obtained can be extrapolated to industrial scale.
  • the present disclosure provides a barrier film and a process of preparation of barrier film from ultra-high molecular weight polyethylene (UHMWPE).
  • UHMWPE ultra-high molecular weight polyethylene
  • the crystallinity of UHMWPE was measured using x-ray technique.
  • the elastic modulus of UHMWPE was measured in melt form, at 180°C by strain controlled dynamic rheometer using parallel plate geometry in time sweep mode.
  • the oxygen and nitrogen permeability of the barrier film were measured by ASTM D1434 and moisture vapor permeation of the barrier film was measured by ASTM F1249.
  • the tensile properties of the barrier film were measured by ASTM D882 and were restricted to the machine direction only.
  • UHMWPE was subjected to solid state compacting by calendaring.
  • UHMWPE powder having molecular weight (Mv) 5.16 million g mol - " 1 , bulk density of 0.063 g cm - " 3 and crystallinity of 95.2% was homogeneously mixed with pentaerythritol tetrakis(3,5-di-tert- butyl-4-hydroxyhydrocinnamate) (2000 ppm) to obtain UHMWPE mixture.
  • the UHMWPE mixture was subjected to solid state compacting at 128° C by passing through a pair of calendar rolls at a linear speed of 2.69 m/min to obtain a layer of solid state compacted ultra- high molecular weight polyethylene having thickness of 150 ⁇ and width of 160 mm.
  • the layer of solid state compacted ultra-high molecular weight polyethylene was then stretched first in the machine direction and then at an angle of 90 ° to the machine direction at roller temperatures of 135° C, and at a linear speed of 3.7 m/min to obtain a barrier film with ratio of stretch as 1 :0.33.
  • the roller gap setting was set in such a way the barrier film of thickness 50 ⁇ was obtained.
  • the barrier film was then analyzed for oxygen permeation rates and nitrogen permeation rates at 0.1 MPa and 23° C, wherein humidity was 0 %.
  • the barrier film was also analyzed for moisture vapor permeation rate test (MVTR) and tensile properties such as tensile strength and tensile modulus.
  • MVTR moisture vapor permeation rate test
  • the oxygen gas permeation rate of the barrier film was 53.4 cm 3.m - " 2.day - " 1
  • the nitrogen gas permeation rate was 10.7 cm 3.m - " 2.day - " 1
  • the moisture vapor permeation rate of the barrier film was 0.5 g.m - " 2.day - " 1.
  • the tensile strength and tensile modulus of the barrier film was 1350 kg cm “ and 25000 kg cm “2 respectively. It is inferred that the barrier film obtained using the process of the present disclosure has good mechanical properties and low permeation rates for oxygen, nitrogen and moisture vapor. Therefore, the barrier film of the present disclosure is a suitable candidate for packaging of food material and electronic goods.
  • the UHMWPE mixture was subjected to solid state compacting by compression molding at 125°C and a pressure of 200 bar to obtain a layer of solid state compacted ultra-high molecular weight polyethylene having a thickness of 1000 ⁇ and diameter of 120 mm.
  • the layer of solid state compacted ultra-high molecular weight polyethylene was first hot stretched in the machine direction by feeding the film at the nip of a calendaring roller unit at a temperature of 125° C and a linear roller speed of 0.19 m/min to stretch the film in the machine direction and then hot stretched at an angle of 90° to the machine direction to obtain a unidirectionally stretched film.
  • the unidirectionally stretched film so obtained was then stretched at 90 ° to the machine direction with the help of another calendaring roller unit at 125° C and a linear roller speed of 0.19 m/min. These steps were repeated 3 times while progressively reducing the gap between the rollers to obtain a barrier film having thickness of 220 ⁇ .
  • the barrier film was then analyzed for oxygen permeation rates and nitrogen permeation rates at 0.1 MPa and 23° C, wherein humidity was 0 %.
  • the barrier film was also analyzed for moisture vapor permeation rate test (MVTR) and tensile properties such as tensile strength and tensile modulus.
  • the nitrogen permeation rate of the barrier film was 9.0 cm 3 day - " 1 m- " 2 and the oxygen permeation rate of the barrier film was 45 cm 3 day - " 1 m- " 2.
  • the moisture vapor permeation rate (MVTR) value was 0.3 g m "2 day "1 .
  • UHMWPE powder having molecular weight of 3.9 million g mole “1 , bulk density of 0.058 g cm “ and crystallinity of 91% was homogeneously mixed with pentaerythritol tetrakis(3,5-di- tert-butyl-4-hydroxyhydrocinnamate) (2000 ppm) to obtain UHMWPE mixture.
  • the UHMWPE mixture was subjected to solid state compacting at 128 °C by feeding in the nip of two roll mill at a linear speed of 2.69 m/min to obtain a layer of solid state compacted ultrahigh molecular weight polyethylene having thickness of 110 ⁇ and width of 23 cm.
  • the tensile strength of the barrier film was 2000 kg cm " and the tensile modulus of the barrier film was 26800 kg cm " .
  • the stacked layer was fused at 135 °C by feeding at 90° in the nip of the rollers which are maintained at a linear speed of 3.75 m/min, to obtain a fused layer of solid state compacted ultra-high molecular weight polyethylene.
  • the fused layer was hot stretched at 138 °C in the machine direction and at an angle of 90° to the machine direction. The hot stretching steps were repeated while reducing the nip gap to obtain a multilayer barrier film having thickness of 50 ⁇ .
  • the multilayer barrier film was then analyzed for tensile properties such as tensile strength and tensile modulus.
  • the tensile strength of the multilayer barrier film was 1850 kg cm " and the tensile modulus of the multilayer barrier film was 22000 kg cm " .
  • the barrier film obtained using the process of the present disclosure has good physical strength and low permeation rates for oxygen, nitrogen and moisture. Therefore, the barrier film of the present disclosure is a suitable candidate for packaging of food material and electronic goods.
  • the present disclosure described herein above has several technical advantages including, but not limited to, the realization of a barrier film comprising ultra-high molecular weight polyethylene having: - high barrier performance with low gas and moisture permeation rates; and

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Abstract

La présente invention concerne un film barrière et son procédé de préparation. Le film barrière comprend au moins une couche de polyéthylène à ultra haut poids moléculaire étiré à chaud et compacté à l'état solide. Le film barrière a une performance de barrière élevée et une résistance élevée avec une épaisseur dans la plage de 5,0 µm à 300 µm. Le film barrière a de faibles taux de perméation pour l'oxygène, l'azote et la vapeur d'humidité. Le film barrière présente également une résistance à la traction et un module de traction élevés. Le film barrière selon la présente invention trouve une application dans le domaine de l'emballage de produits alimentaires et électroniques nécessitant une barrière élevée contre le gaz et l'humidité.
PCT/IB2017/058027 2016-12-17 2017-12-16 Film barrière et son procédé de préparation Ceased WO2018109747A1 (fr)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0550116A1 (fr) * 1991-12-30 1993-07-07 Dsm N.V. Procédé de préparation d'un objet électroconducteur
JP2938613B2 (ja) * 1990-11-01 1999-08-23 日石三菱株式会社 スプリット化ポリエチレン延伸材料およびその製造方法
EP1497364A1 (fr) * 2002-04-12 2005-01-19 Daramic, Inc. Articles en polyethylene de masse moleculaire tres elevee et procede de fabrication desdits articles
EP2544841A1 (fr) * 2010-03-12 2013-01-16 Celgard LLC Membranes poreuses à orientation biaxiale, composites, et procédés de fabrication et d'utilisation

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2938613B2 (ja) * 1990-11-01 1999-08-23 日石三菱株式会社 スプリット化ポリエチレン延伸材料およびその製造方法
EP0550116A1 (fr) * 1991-12-30 1993-07-07 Dsm N.V. Procédé de préparation d'un objet électroconducteur
EP1497364A1 (fr) * 2002-04-12 2005-01-19 Daramic, Inc. Articles en polyethylene de masse moleculaire tres elevee et procede de fabrication desdits articles
EP2544841A1 (fr) * 2010-03-12 2013-01-16 Celgard LLC Membranes poreuses à orientation biaxiale, composites, et procédés de fabrication et d'utilisation

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