Classifications

• • 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
  • C08J7/00—Chemical treatment or coating of shaped articles made of macromolecular substances
  • C08J7/04—Coating
  • C08J7/042—Coating with two or more layers, where at least one layer of a composition contains a polymer binder
• • 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
  • B65D65/42—Applications of coated or impregnated materials
• • 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
  • B65D81/00—Containers, packaging elements, or packages, for contents presenting particular transport or storage problems, or adapted to be used for non-packaging purposes after removal of contents
  • B65D81/34—Containers, packaging elements, or packages, for contents presenting particular transport or storage problems, or adapted to be used for non-packaging purposes after removal of contents for packaging foodstuffs or other articles intended to be cooked or heated within the package
  • B65D81/343—Containers, packaging elements, or packages, for contents presenting particular transport or storage problems, or adapted to be used for non-packaging purposes after removal of contents for packaging foodstuffs or other articles intended to be cooked or heated within the package specially adapted to be heated in a conventional oven, e.g. a gas or electric resistance oven
• • 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
  • C08J7/00—Chemical treatment or coating of shaped articles made of macromolecular substances
  • C08J7/04—Coating
  • C08J7/0427—Coating with only one layer of a composition containing a polymer binder
• • 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
  • C08J7/00—Chemical treatment or coating of shaped articles made of macromolecular substances
  • C08J7/04—Coating
  • C08J7/043—Improving the adhesiveness of the coatings per se, e.g. forming primers
• • 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
  • C08J7/00—Chemical treatment or coating of shaped articles made of macromolecular substances
  • C08J7/04—Coating
  • C08J7/052—Forming heat-sealable coatings
• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
  • C09D123/00—Coating compositions based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Coating compositions based on derivatives of such polymers
  • C09D123/02—Coating compositions based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Coating compositions based on derivatives of such polymers not modified by chemical after-treatment
  • C09D123/04—Homopolymers or copolymers of ethene
  • C09D123/08—Copolymers of ethene
  • C09D123/0846—Copolymers of ethene with unsaturated hydrocarbons containing other atoms than carbon or hydrogen atoms
  • C09D123/0853—Vinylacetate
• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
  • C09D127/00—Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Coating compositions based on derivatives of such polymers
  • C09D127/02—Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Coating compositions based on derivatives of such polymers not modified by chemical after-treatment
  • C09D127/04—Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Coating compositions based on derivatives of such polymers not modified by chemical after-treatment containing chlorine atoms
  • C09D127/08—Homopolymers or copolymers of vinylidene chloride
• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
  • C09D147/00—Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds; Coating compositions based on derivatives of such polymers
• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
  • C09D5/00—Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
  • C09D5/002—Priming paints
• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
  • C09D7/00—Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
  • C09D7/40—Additives
  • C09D7/65—Additives macromolecular
• • 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
  • C08J2367/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
  • C08J2367/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
• • 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
  • C08J2423/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
  • C08J2423/02—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
  • C08J2423/04—Homopolymers or copolymers of ethene
  • C08J2423/08—Copolymers of ethene
• • 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
  • C08J2427/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers
  • C08J2427/02—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment
  • C08J2427/04—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment containing chlorine atoms
  • C08J2427/08—Homopolymers or copolymers of vinylidene chloride
• • 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
  • C08J2447/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds; Derivatives of such polymers
• • 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
  • C08J2453/00—Characterised by the use of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers
  • C08J2453/02—Characterised by the use of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers of vinyl aromatic monomers and conjugated dienes
• • 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
  • C08J2493/00—Characterised by the use of natural resins; Derivatives thereof
• • 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
  • C08J2493/00—Characterised by the use of natural resins; Derivatives thereof
  • C08J2493/04—Rosin

Definitions

• This invention relates to a composite polymeric film, and a process for the production thereof.
• the film is particularly suitable for use as a sealable film, particularly a sealable and peelable film for packaging applications, particularly for the packaging of food, such as ready-prepared ovenable meals.
• the film of the present invention is suitable for use as a lid for a container which contains a foodstuff such as a ready-prepared ovenable meal.
• Plastic containers are commonplace in packaging applications, such as food packaging, and in particular for packaging convenience foods, for example ready-prepared ovenable meals which are warmed either in a microwave oven or in a conventional oven. Also known are “dual-ovenable” containers which may be warmed in either a microwave or a conventional oven.
• the container may be formed of polyester, such as polyethylene terephthalate (PET), polypropylene (PP), polyethylene (PE) or polystyrene (PS), or may be PVDC-coated.
• PET polyethylene terephthalate
• PP polypropylene
• PE polyethylene
• PS polystyrene
• a container in widespread use for ovenable meals is an APET/CPET container, which consists of a composite material having an amorphous PET layer on top of a crystalline PET layer.
• Other suitable types of container include a foil tray (particularly an aluminium foil tray), a metallised tray and a tray formed from PET-coated cartonboard or paperboard. Of particular utility are trays formed from metallised (particularly flash- metallised) PET cartonboard.
• Container lids are typically made from film comprising a flexible polymeric substrate and a heat-sealable polymeric layer, and are often referred to as “lidding” films.
• the manufacture of sealed containers using lidding films involves the formation of a seal between the lidding film and the container. This seal is formed by placing the lid on top of the container and applying heat and pressure in order to soften or melt the sealable coating layer so that it adheres to the surface of the container and forms an effective seal between the lid and the container.
• Biaxially oriented polyester film has been widely used as a flexible substrate for lidding films because of its excellent mechanical strength, and various functional coatings have been proposed for use as the heat-sealable polymeric layer.
• container substrates to which conventional polyester lidding films exhibit a relatively low heat-seal strength and there remains a need to broaden the range of application of polyester lidding films.
• the term “clean peel” means that no or substantially no residue of the heat- sealable layer is visible on the surface of the container after peeling the lidding film therefrom.
• a clean peel is important from the perspective of the consumer, in order to avoid the impression that the contents of the container might be contaminated by the sealant material.
• a heat-sealable peelable composite film comprising an oriented polyester substrate layer having a first and second surface and disposed on a first surface of the substrate layer a heat-sealable polymeric coating layer comprising a styrenic linear block copolymer thermoplastic elastomer, an ethylene vinyl acetate (EVA) copolymer and a tackifying resin.
• a heat-sealable polymeric coating layer comprising a styrenic linear block copolymer thermoplastic elastomer, an ethylene vinyl acetate (EVA) copolymer and a tackifying resin.
• the first surface of the polyester substrate layer is the surface which faces the container when the film is used as a lidding film as described herein.
• the second surface of the polyester substrate layer is the surface which is outermost, and which faces away from the interior of the container.
• the substrate is a self-supporting film or sheet by which is meant a film or sheet capable of independent existence in the absence of a supporting base.
• the substrate is uniaxially or biaxially oriented, preferably biaxially oriented. It will be appreciated from the disclosure hereinbelow that the substrate may be described as semi-crystalline.
• the term “semi-crystalline” refers to a film which exhibits a crystallinity of at least 5%, preferably at least 10%, preferably at least 15%, preferably at least 20%, preferably at least 25%, and typically no higher than 50% or 45% or 40%.
• the substrate may be formed from any suitable film-forming thermoplastic polyester material. Synthetic linear polyesters are preferred. It will be appreciated that the substrate polyester is crystallisable. Suitable polyesters include those derived from one or more dicarboxylic acids, such as terephthalic acid, isophthalic acid, phthalic acid, 2,5-, 2,6- or 2,7-naphthalenedicarboxylic acid, 4,4'-diphenyldicarboxylic acid, hexahydro-terephthalic acid, 1,10-decanedicarboxylic acid, and in particular aliphatic dicarboxylic acids including those of the general formula C n H 2n (COOH) 2 wherein n is 2 to 8, such as succinic acid, glutaric acid sebacic acid, adipic acid, azelaic acid, suberic acid or pimelic acid; and from one or more glycols, particularly an aliphatic or cycloaliphatic glycol, such as ethylene glycol, 1,3-propan
• the dicarboxylic acid component of the substrate polyester preferably comprises at least one aromatic dicarboxylic acid (which is preferably selected from terephthalic acid and 2,6-naphthalenedicarboxylic acid, and preferably terephthalic acid), and optionally further comprises a second, different dicarboxylic acid preferably selected from the dicarboxylic acids noted above, and preferably from an aromatic dicarboxylic acid (particularly isophthalic acid) and the aliphatic diacids noted above.
• the polyester is preferably derived from an aromatic dicarboxylic acid, preferably terephthalic acid or 2,6- naphthalenedicarboxylic acid, preferably terephthalic acid.
• the dicarboxylic acid component of the substrate polyester contains only one aromatic dicarboxylic acid, which is preferably terephthalic acid or 2,6-naphthalenedicarboxylic acid, and is preferably terephthalic acid.
• the glycol component of the substrate polyester preferably comprises at least one aliphatic diol, at least one of which is ethylene glycol.
• the glycol component of the substrate polyester is an aliphatic diol, preferably ethylene glycol.
• a preferred substrate polyester is selected from polyethylene terephthalate (PET) and polyethylene naphthalate (PEN), or a PET-based or PEN-based copolyester.
• the substrate polyester is PET.
• the film-forming polyester resin is the major component of the substrate, and makes up at least 70% by weight of the total weight of the substrate, preferably at least 80%, preferably at least 85%, preferably at least 90%, preferably at least 95%, more typically at least 98%, more typically at least 99% by weight of the total weight of the substrate.
• the intrinsic viscosity of the polyester from which the substrate is manufactured is preferably at least about 0.60, preferably at least about 0.61, preferably at least 0.62, preferably at least 0.63, preferably at least 0.64, preferably at least 0.65, preferably at least about 0.70, preferably at least about 0.75.
• the intrinsic viscosity of the substrate polyester is not more than 0.85, preferably not more than 0.83.
• the use of polyesters with too high a viscosity can lead to difficulties in film manufacture and/or require specialised, more robust film-forming equipment.
• increasing the viscosity too greatly may mean that it is appropriate to reduce output (i.e. reduce the amount of polyester extruded per unit time, which leads to a less economical process) or to increase the extrusion temperature in order to reduce the viscosity of the melt (which in turn can lead to thermal degradation of the polymer and the loss of associated properties) in order to achieve stable film production.
• polyesters are conveniently effected in a known manner by condensation or ester interchange, generally at temperatures up to about 295°C.
• solid state polymerisation may be used to increase the intrinsic viscosity of the polyesters to the desired value, using conventional techniques well-known in the art, for instance using a fluidised bed such as a nitrogen fluidised bed or a vacuum fluidised bed using a rotary vacuum drier.
• the polyester substrate may further comprise any other additive conventionally employed in the manufacture of polyester films.
• agents such as particulate fillers, hydrolysis stabilisers, anti-oxidants, UV- stabilisers, cross-linking agents, dyes, lubricants, radical scavengers, thermal stabilisers, surface active agents, gloss improvers, prodegradents, viscosity modifiers and dispersion stabilisers may be incorporated as appropriate.
• particulate fillers preferably glycidyl esters of branched monocarboxylic acids
• anti-oxidants preferably hindered phenols, secondary aromatic amines and hindered amines
• suitable additives in this regard are disclosed in WO-2012/120260-A, the disclosure of which additives is incorporated herein by reference.
• UV-stabilisers are also of particular utility.
• Particulate fillers can improve handling and windability during manufacture and/or modulate optical properties, as is well known in the art.
• the particulate filler is typically a particulate inorganic filler (e.g. metal or metalloid oxides, such as alumina, titania, talc and silica (especially precipitated or diatomaceous silica and silica gels), calcined china clay and alkaline metal salts, such as the carbonates and sulphates of calcium and barium).
• metal or metalloid oxides such as alumina, titania, talc and silica (especially precipitated or diatomaceous silica and silica gels)
• calcined china clay and alkaline metal salts such as the carbonates and sulphates of calcium and barium.
• a particulate inorganic filler is preferably finely-divided, and the volume distributed median particle diameter (equivalent spherical diameter corresponding to 50% of the volume of all the particles, read on the cumulative distribution curve relating volume % to the diameter of the particles - often referred to as the "D(v,0.5)" value) thereof is preferably in the range from 0.01 to 5 ⁇ m, more preferably 0.05 to 1.5 ⁇ m, and particularly 0.15 to 1.2 ⁇ m.
• Preferably at least 90%, more preferably at least 95% by volume of the inorganic filler particles are within the range of the volume distributed median particle diameter ⁇ 0.8 ⁇ m, and particularly ⁇ 0.5 ⁇ m.
• Particle size of the filler particles may be measured by electron microscope, coulter counter, sedimentation analysis and static or dynamic light scattering. Techniques based on laser light diffraction are preferred.
• the aforementioned conventionally employed additives may be introduced into the polymer in a conventional manner. For example, by mixing with the monomeric reactants from which the film- forming polymer is derived, or the components may be mixed with the polymer by tumble or dry blending or by compounding in an extruder, followed by cooling and, usually, comminution into granules or chips. Masterbatching technology may also be employed.
• the heat-sealable polymeric layer disposed on a first surface of the substrate is capable of forming a heat-seal bond to the surfaces of a container, particularly a polyolefin container, particularly a polypropylene or polyethylene container, and particularly a polypropylene container.
• the heat- sealable layer is capable of softening to a sufficient extent on heating that its viscosity becomes low enough to allow adequate wetting for it to adhere to the surface to which it is being bonded.
• the styrenic linear block copolymer thermoplastic elastomer of the heat-sealable polymeric layer preferably consists of polystyrene blocks and rubber blocks derived from butadiene (conventionally 1,3 -butadiene) and/or isoprene, or their hydrogenated equivalents.
• the styrene content is preferably in the range from 5 to 50%, preferably from 8 to 30%, preferably 10 to about 20%, and preferably 10 to about 15%, by mass of the copolymer.
• the rubber blocks make up the balance of the mass of the copolymer. If the styrene content is too great then the polymer becomes too stiff, and if the styrene content is too low then the polymer becomes too rubbery.
• the rubber blocks may consist of polybutadiene or polyisoprene or combinations thereof.
• Such copolymers may be described as triblock copolymers with polystyrene blocks at each end of the triblock linked together by a rubber block (polybutadiene and/or polyisoprene), and these copolymers are commonly referred to as SBS or SIS copolymers.
• the hydrogenated butadiene- or isoprene-derived blocks may be prepared by selective hydrogenation according to conventional techniques well-known in the art. Hydrogenation may be carried out using any of the processes known in the prior art, for example, as taught in US-3,494,942, US-3,634,594, US-3,670,054 or US- 3,700,633. Hydrogenation can be carried out under such conditions that at least about 90% (preferably at least 95%, preferably at least 98%) of the conjugated diene double bonds have been reduced, and from 0 to 10% of the arene double bonds have been reduced.
• the hydrogenated styrenic copolymers are preferably selected from (i) triblock copolymers containing styrene blocks and rubber blocks consisting of ethylene and butylene repeating units (referred to herein as SEBS copolymers); and (ii) triblock copolymers containing styrene blocks and rubber blocks consisting of ethylene and propylene repeating units (referred to herein as SEPS copolymers).
• SEBS copolymers triblock copolymers containing styrene blocks and rubber blocks consisting of ethylene and propylene repeating units
• SEPS copolymers triblock copolymers containing styrene blocks and rubber blocks consisting of ethylene and propylene repeating units
• the ethylene/butylene (EB) block is derived from 1,4- and 1,2-polybutadienes, and the ethylene/propylene (EP) block from 1,4-polyisoprene.
• Such copolymers are commercially available under
• the weight average molecular weight (Mw) of the styrenic copolymer is preferably from 50,000 to 400,000, preferably from 50,000 to 200,000.
• the weight average molecular weight (Mw) of the styrene block is preferably from 5,000 to 50,000, preferably from 5,000 to 25,000.
• Molecular weight is suitably measured by conventional GPC techniques, preferably using a polystyrene (PS) standard. For instance, molecular weight determination may be conducted on a Hewlett-Packard 1050 Series HPLC system equipped with two GPC Ultrastyragel columns, 103 and 104 A (5 ⁇ m mixed, 300 mm x 19 mm, Waters Millipore Corporation, Milford, MA, USA) and THF as mobile phase.
• the tensile strength of the styrenic copolymer is at least 5 MPa, preferably at least 10 MPa, preferably at least 15 MPa, preferably at least 20 MPa.
• the tensile strength is in the range of 15 to 30 MPa. If the tensile strength is too low, the cohesive strength of the heat-sealable layer becomes too low, which increases the risk of cohesive failure in the layer and may not allow a clean peel.
• the solution viscosity of the styrenic copolymer is no more than about 250 cPs, preferably no more than about 100 cPs, measured with a Brookfield Viscometer at 25°C in a toluene solution at 10wt%. If the solution viscosity is too high, the coating formulation may become too viscous to easily coat on the substrate, and may the styrenic copolymer may not properly dissolve in the solvent vehicle of the coating formulation.
• the solution viscosity of the styrenic copolymer is at least 5 cPs, preferably at least 10 cPs.
• the solution viscosity is in the range of 5 to 250 cPs, preferably 10 to 100 cPs.
• the glass transition temperature of suitable styrenic copolymers is preferably in the range of -50 to -80°C, preferably -60 to -70°C.
• the melting point of suitable styrenic copolymers is preferably greater than 0°C, and preferably less than 50°C.
• the heat-sealable polymeric layer preferably comprises the styrenic copolymer in an amount of from 10 to 50 wt% of the layer, preferably in an amount of from 20 to 40 wt%, preferably from 25 to 35 wt%, by total weight of the heat-sealable polymeric layer.
• the heat- sealable layer also comprises ethylene vinyl acetate (EVA) copolymer resin, which improves the bond between the styrenic copolymer and the polyester substrate.
• EVA copolymers may be obtained from DuPont as ElvaxTM resins.
• the vinyl acetate (VA) content of these copolymer resins is preferably in the range of 5 to 50 wt%, preferably 15 to 50wt%, and preferably 18 to 40wt% (which may be determined by ASTM E168-16).
• the vinyl acetate (VA) content of these copolymer resins is preferably in the range of 15 to 50wt%, and preferably 18 to 40wt%, preferably 20 to 35wt%, preferably 20 to 30 wt%, preferably 22 to 28wt%, in order to provide excellent clarity, along with excellent peel strength and a clean peel.
• the EVA copolymer may optionally comprise minor amounts of one or more (preferably only one) additional comonomer(s) (i.e.
• ethylene and vinyl acetate comonomers preferably ethylenically unsaturated comonomers (particularly acrylic acid and methacrylic acid), preferably wherein the total amount of additional comonomer(s) is no more than about 10 wt%, preferably no more than about 5wt%, preferably no more than about 2.5wt%, preferably no more than about lwt%.
• the melting point of the EVA copolymer resin is preferably in the range of from 40°C to 95°C, preferably 45°C to 85°C, preferably 45°C to 75°C.
• the melt index of the EVA copolymer resin is preferably in the range of from 5 to 1000, preferably 5 to 600, preferably 5 to 200, preferably 5 to 100 g/10min. Where a single grade of EVA copolymer is present in the heat-sealable layer, the melt index of the EVA copolymer is preferably in the range of from 5 to 200, preferably 5 to 100 g/10min.
• the heat-sealable polymeric layer preferably comprises the EVA copolymer in an amount of from 20 to 70 wt% of the layer, preferably from 20 to 40 wt%, preferably from 25 to 35 wt%, by total weight of the heat-sealable polymeric layer.
• the heat-sealable polymeric layer comprises a blend of a first EVA copolymer (EVA-1) and a second EVA copolymer (EVA-2), wherein the total amount of EVA copolymer is the same as described above.
• the first EVA copolymer (EVA-1) preferably has a VA content in the range of 20 to 50wt%, preferably 20 to 40wt%, and preferably a melt index in the range of from 2.5 to 100, preferably 5 to 100 g/10min.
• the second EVA copolymer (EVA-2) preferably has a VA content in the range of from 5 to 20wt%, preferably 10 to 20wt%, and preferably exhibits a melt index of from 100 to 1000, preferably 150 to 600 g/10min.
• the weight ratio of EVA-2/EVA-1 is preferably in the range of greater than 0/100 to 100/100, more preferably greater than 0/100 to 65/100, more preferably 15/100 to 50/100, more preferably 15/100 to 30/100.
• the heat- sealable layer also comprises a tackifying resin, which improves the adhesive bond between the styrenic copolymer and the polyester substrate.
• the tackifying resin also improves the compatibility between the styrenic copolymer and the EVA component, thereby discouraging phase separation therebetween, which improves the cohesive strength of the heat- sealable layer and its optical properties, particularly clarity.
• suitable tackifying resins for the styrenic copolymers disclosed herein include polystyrene block compatible resins and hydrogenated (mid) block compatible resins, and mixtures thereof.
• Resins compatible with the polystyrene block may be selected from the group of coumarone-indene resin, polyindene resin, poly(methyl indene) resin, polystyrene resin, vinyltoluene-alphamethylstyrene resin, alphamethylstyrene resin and polyphenylene ether, in particular poly(2, 6-dimethyl- 1,4-phenylene ether).
• Such resins are e.g.
• Resins compatible with the hydrogenated (mid) block may be selected from the group consisting of compatible Cs hydrocarbon resins, hydrogenated Cs hydrocarbon resins, styrenated Cs resins, C5/C9 resins, styrenated terpene resins, fully hydrogenated or partially hydrogenated C9 hydrocarbon resins, polyterpenes, rosin and rosin esters, rosin derivatives and mixtures thereof.
• compatible Cs hydrocarbon resins hydrogenated Cs hydrocarbon resins
• styrenated Cs resins C5/C9 resins
• styrenated terpene resins fully hydrogenated or partially hydrogenated C9 hydrocarbon resins
• polyterpenes rosin and rosin esters, rosin derivatives and mixtures thereof.
• Such resins are e.g. sold under the trademarks “REGALITE”, “REGALREZ”, “ESCOREZ” and “ARKON”.
• Particularly suitable tackifying resins are selected from synthetic and natural polyterpenes, hydrocarbon resins, rosin and rosin ester resins, and combinations thereof.
• the tackifying resins suitably exhibit ring and ball softening points from 20°C to 160°C, preferably 90°C to 125°C (preferably tested according to the procedure taught in ASTM E28-18).
• the number average molecular weights of the tackifying resins are preferably at least 200 or 500, and preferably at most 5000, 2000, or 1000 (preferably measured by the GPC techniques described hereinabove).
• Natural polyterpene tackifying resins are based on natural and renewable feedstocks, including alpha-pinene, beta-pinene and d-limonene. Examples include:
• Piccolyte® C resin C85, C105, C115, C125, C135)
• Piccolyte® F resin F105, F115
• Piccolyte® A resin A25, A115, A125, A135)
• Piccolyte® S resin S25, S85, S115, S125, S135); all available from Pinova.
• Hydrocarbon tackifying resins are made from petroleum-based feedstocks, either aliphatic (C 5 ), aromatic (C 9 ), DCPD (dicyclopentadiene), or mixtures of these. Examples include:
• Rosin ester tackifying resins are produced by the reaction between rosin acids and alcohols.
• the rosin acids may be modified by hydrogenation or disproportionation.
• the typical commercial products are methyl, triethylene glycol, glycerol, and pentaerythritol esters. Examples include:
• the heat- sealable polymeric layer preferably comprises the tackifying resin in an amount of from 15 to 50 wt% of the layer, preferably from about 15 to 40 wt%, typically from about 30 to 40 wt%, by total weight of the heat-sealable polymeric layer.
• the heat-sealable polymeric layer preferably comprises the afore-mentioned components in the following amounts:
• the styrenic copolymer in an amount of from 10 to 50 wt%, preferably from 20 to 40 wt%, preferably from 25 to 35 wt%, of the layer;
• the EVA resin in an amount of from 20 to 70 wt%, preferably from 20 to 40 wt%, preferably from 25 to 35 wt% of the layer; and (iii) the tackifying resin in an amount of from 15 to 50 wt%, preferably from about 15 to 40 wt%, typically from about 30 to 40 wt%, of the layer.
• the heat-sealable layer preferably also comprises a slip-aid or anti-blocking agent which improves the handling of the film, as is conventional in the art of sealant coatings.
• Suitable slip-aids include Camauba wax, kemamide and silica. Such components are present in relatively minor amounts, typically no more than 5.0 wt%, typically no more than 2.0 wt%.
• the total amount of said styrenic linear block copolymer thermoplastic elastomer, ethylene vinyl acetate (EVA) copolymer and tackifying resin make up at least 90 wt%, preferably at least 92 wt%, preferably at least 95 wt% of the heat- sealable polymeric coating layer.
• the heat-sealable layer is suitably disposed on the substrate by coating a coating formulation onto the polyester substrate, as discussed hereinbelow.
• the components of the heat-sealable layer are typically dispersed or dissolved in a coating vehicle, typically an organic solvent, preferably toluene.
• the coating formulation preferably comprises the coating vehicle in an amount of from 70 to 90, preferably 75 to 85 wt% of the coating formulation.
• Formation of the composite film may be effected by conventional techniques well-known in the art.
• formation of the substrate is effected by extrusion, in accordance with the procedure described below.
• the process comprises the steps of extruding a layer of molten polymer at a temperature within the range of from about 275 to about 300°C, preferably from about 290 to 295°C, quenching the extrudate and orienting the quenched extrudate in at least one direction.
• the substrate may be uniaxially oriented, but is preferably biaxially oriented by drawing in two mutually perpendicular directions in the plane of the film to achieve a satisfactory combination of mechanical and physical properties.
• Orientation may be effected by any process known in the art for producing an oriented film, for example a tubular or flat film process.
• Biaxial orientation is effected by drawing in two mutually perpendicular directions in the plane of the film to achieve a satisfactory combination of mechanical and physical properties.
• simultaneous biaxial orientation may be effected by extruding a thermoplastics polyester tube which is subsequently quenched, reheated and then expanded by internal gas pressure to induce transverse orientation, and withdrawn at a rate which will induce longitudinal orientation.
• Suitable simultaneous biaxial orientation processes are disclosed in EP-2108673-A and US- 2009/0117362-A1, the disclosure of which processes is incorporated herein by reference.
• the film-forming polyester is extruded through a slot die and rapidly quenched upon a chilled casting drum to ensure that the polyester is quenched to the amorphous state.
• Orientation is then effected by stretching the quenched extrudate in at least one direction at a temperature above the glass transition temperature of the polyester.
• Sequential orientation may be effected by stretching a flat, quenched extrudate firstly in one direction, usually the longitudinal direction, i.e. the forward direction through the film stretching machine, and then in the transverse direction. Forward stretching of the extrudate is conveniently effected over a set of rotating rolls or between two pairs of nip rolls, transverse stretching then being effected in a stenter apparatus.
• Stretching is generally effected so that the dimension of the oriented film is from 2 to 5, more preferably 2.5 to 4.5 times its original dimension in the or each direction of stretching. More preferably, stretching is effect so that the dimension of the oriented film is from 3.0 to 3.3 times its original dimension in the forward draw, and from 3.3 to 3.9 times its original dimension in the sideways draw. Greater draw ratios (for example, up to about 8 times) may be used if orientation in only one direction is required.
• Stretching is conventionally effected at temperatures higher than the T g of the copolyester composition, preferably at least about 5°C higher, preferably at least about 15°C higher than the T g , and preferably in the range of from about T g +5°C to about T g +75°C, preferably from about T g +5°C to about T g +30°C.
• typically stretching is effected at temperatures in the range of about 5 to about 155°C, preferably about 5 to about 110°C. It is not necessary to stretch equally in the machine and transverse directions although this is preferred if balanced properties are desired.
• a stretched film may be, and preferably is, dimensionally stabilised by heat-setting under dimensional support at a temperature above the glass transition temperature of the polyester but below the melting temperature thereof, to induce the desired crystallisation of the polyester.
• TD transverse direction
• Toe-in can involve dimensional relaxation of the order 2 to 4%. While dimensional relaxation in the process or machine direction (MD) is also possible, as is known in the art.
• the actual heat- set temperature and time will vary depending on the composition of the film and its desired final thermal shrinkage but should not be selected so as to substantially degrade the toughness properties of the film such as tear resistance.
• preferred films are heat-set at a temperature from about 80°C less than the melting temperature of the film (i.e. T M -80°C) to about 10°C less than T M (i.e. T M -10°C), preferably from about T M -70°C to about T M -20°C.
• the heat-set temperature is suitably in the range of from about 130 to about 245°C, preferably from about 150 to about 245°C, and preferably at least 180°C, preferably in the range of 190 to 230°C.
• the film is typically quenched rapidly in order induce the desired crystallinity of the polyester.
• the film is further stabilized through use of an in-line relaxation stage.
• the relaxation treatment can be performed off-line.
• the film is heated at a temperature lower than that of the heat- setting stage, and with a much reduced MD and TD tension.
• the tension experienced by the film is a low tension and typically less than 5 kg/m, preferably less than 3.5 kg/m, preferably less than 2.5 kg/m, and typically in the range of 1.0 to 2.0 kg/m of film width.
• the reduction in film speed (and therefore the strain relaxation) is typically in the range 0 to 2.5%, preferably 0.5 to 2.0%. There is no increase in the transverse dimension of the film during the heat-stabilisation step.
• the temperature to be used for the heat stabilisation step can vary depending on the desired combination of properties from the final film, with a higher temperature giving better, i.e. lower, residual shrinkage properties.
• a temperature of 135 to 250 °C is generally desirable, preferably 150 to 230 °C, more preferably 170 to 200 °C.
• the duration of heating will depend on the temperature used but is typically in the range of 10 to 40 seconds, with a duration of 20 to 30 seconds being preferred.
• This heat stabilisation process can be carried out by a variety of methods, including flat and vertical configurations and either “off-line” as a separate process step or “in-line” as a continuation of the film manufacturing process. Film thus processed will exhibit a smaller thermal shrinkage than that produced in the absence of such post heat-setting relaxation.
• the intrinsic viscosity of the polyester film is preferably at least about 0.70, preferably at least about 0.75, preferably at least 0.80, and preferably no more than about 0.85, preferably no more than about 0.83.
• the composite film exhibits a clarity of at least 70%, preferably at least 75%, preferably at least 80%, and preferably at least 85%.
• any filler in the layer is typically present in only small amounts, generally not exceeding 2.5 %, preferably not exceeding 2.0%, preferably not exceeding 1.1%, preferably not exceeding 0.6% and preferably not exceeding 0.3% by weight of a layer, preferably wherein the filler is silica, thereby allowing the windability of the film (i.e. the absence of blocking or sticking when the film is wound up into a roll) to be improved without an unacceptable reduction in optical properties.
• An optically clear film is particularly advantageous for a lidding film, since such films give the impression of freshness and hygiene to the consumer.
• Formation of the heat-sealable layer is effected by coating the coating formulation onto the substrate.
• Coating may be effected using any suitable coating technique, typically roll coating and including gravure roll coating and reverse roll coating. Coating is preferably conducted “off-line”, i.e. after any stretching and subsequent heat-setting employed during manufacture of the substrate. Alternatively, an “in-line” technique may be used, i.e. wherein the coating step takes place before, during or between any stretching operation(s) employed, typically between the forward and sideways stretches of a biaxial stretching operation (“inter-draw” coating).
• the coating formulation is preferably applied to the substrate to provide a dry coat weight of from about 3.5g/m 2 to about 10g/m 2 .
• the exposed surface of the substrate Prior to application of the heat-sealable layer onto the substrate, the exposed surface of the substrate is preferably coated with a surface-modifying primer treatment to improve the bond between the substrate and the subsequently applied heat-sealable polymeric coating layer.
• the primer is a polymer layer selected from polyvinylidene chloride (PVDC), EVA and ethylene acrylic acid (EAA) resins, preferably from PVDC and EVA resins, and preferably PVDC resins.
• a primer layer is disposed on the first surface of the substrate layer of the composite film disclosed herein such that the layer order is substrate layer / primer layer / heat- sealable polymeric coating layer.
• the primer layer is suitably a coating layer.
• a primer coating layer may be coated using the coating techniques described herein, and may be coated in-line or off-line coated.
• the primer layer is preferably applied to the surface of the substrate layer to provide a dry coat- weight of from about 0.05 to about 1.0 g/m 2 , preferably from about 0.1 g/m 2 to about 0.5 g/m 2 .
• the final thickness of the primer layer is preferably no more than 1 ⁇ m, preferably no more than about 0.5 ⁇ m, preferably no more than about 0.3 ⁇ m, preferably at least 0.05 ⁇ m, and typically about 0.1 ⁇ m
• the thickness of the substrate is preferably from about 10 to about 100 ⁇ m, preferably from 10 to about 75 ⁇ m, and particularly from about 12 to about 50 ⁇ m.
• the thickness of the heat-sealable layer is preferably no more than 45%, more preferably no more than 40 % and more preferably no more than 35 %, and preferably at least 5 % more preferably at least 10 %, and preferably from about 12 % to about 35 %, of the total thickness of the composite film.
• the heat-sealable layer has a thickness of up to about 25 ⁇ m, more preferably up to about 15 ⁇ m, more preferably up to about 10 ⁇ m, more preferably from about 2 to about 10 ⁇ m, and more preferably from about 3 to 6 ⁇ m.
• the composite film preferably exhibits a heat-seal strength (or peel strength) as defined herein to a polypropylene substrate (preferably a polypropylene tray) in the range of 600 to 1500 g/25.4mm, preferably at least 700, preferably at least 800, preferably at least 900, preferably at least 1000 g/25.4mm, and preferably no more than 1500, preferably no more than 1200, preferably no more than 1125 g/25.4mm.
• the heat-seal strength of the film to a standard PP tray is in the range of 800 to 1500 g/25.4mm, preferably 800 to 1200 g/25.4mm, preferably 800 to 1125 g/25.4mm. If the heat-seal strength is too high, the composite film can fracture or shred during the peel. If the heat-seal strength is too low, there is inadequate adhesion between the composite film and the substrate.
• the composite film of the present invention is useful for sealing or providing a lid on a receptacle for packaging convenience or ready-prepared foods, for example ovenable meals which are warmed either in a microwave or a conventional oven.
• the receptacle may be a container such as a thermoformed tray or bowl, and may be formed of the tray materials described hereinabove.
• the composite film is particularly useful for sealing or providing a lid on such a receptacle which is made from polyolefin, particularly PP or PE, and particularly PP.
• the present invention provides a sealed container comprising a receptacle containing a food product, particularly an ovenable meal, and a lid formed from a heat-sealable composite film as defined herein.
• said heat- sealable polymeric layer of the composite film is in direct contact with the receptacle and that the composite film is adhered to the receptacle via a peelable heat-seal bond.
• the receptacle is preferably made from polyolefin, particularly PP or PE, and particularly PP.
• the sealed container is produced by techniques well-known to those skilled in the art. Once the food to be packaged has been introduced into the receptacle, the heat- sealable film lid is affixed using temperature and/or pressure using conventional techniques and equipment.
• the present invention provides the use of a composite film as described herein as a lid in the packaging of a food product, particularly an ovenable meal, said packaging further comprising a receptacle, particularly wherein the receptacle is made from polyolefin, particularly PP or PE, and particularly PP. It will be appreciated that the use of the third aspect is suitable for forming the sealed container of the second aspect.
• the optical properties of the film are evaluated by measuring the diffuse transmittance of visible light through the thickness of the film in terms of haze (wide angle scattering (>2.5 to 180°)) and clarity (narrow angle scattering ( ⁇ 2.5°)).
• the diffuse transmittance is the percentage of scattered transmitted visible light at said collection angles, as measured according to the standard test method ASTM D1003-13, preferably using a BYK Haze-gard Plus instrument.
• haze is calculated as 100 x TDIF/TT, where TT is the total amount of transmitted light and TDIF is the amount of diffused transmitted light scattered at an angle of greater than 2.5 from the normal.
• Clarity is calculated as the percentage of light that is subject to narrow angle scattering, i.e. less than 2.5° from the normal.
• T g was determined as the extrapolated onset temperature of the glass transition observed on the DSC scans (heat flow (W/g) against temperature (°C)), as described in ASTM E1356-98.
• the value of a T m was determined from the DSC scans as the peak endotherm of the transition.
• ⁇ H m ° theoretical enthalpy of fusion of the corresponding poly(alkylene- carboxylate) homopolymer at 100 % crystallinity.
• ⁇ H m ° is the theoretical enthalpy of fusion of a 100% crystalline PET polymer (140 J/g)
• PEN (or PEN-based) polyesters ⁇ H m ° is the theoretical enthalpy of fusion of a 100% crystalline PEN polymer (103 J/g), as defined in the literature (B. Wunderlich, Macromolecular Physics , Academic Press, New York, (1976)).
• Heat seal strength (also referred to herein as peel strength) of coatings to mineral filled white polypropylene (30 wt% mineral, 0.36 mm thickness) was assessed as follows.
• the coated film was sealed to PP using a Sentinel heat sealer (Model 12 by Packaging Industries Group Inc.). Unless otherwise stated, the heat seal conditions were: 350°F (top jaw), 100°F (bottom jaw)/0.1 second/80psi. In cases where the top jaw was at some other temperature, the bottom jaw was still at approximately 100°F.
• the sealed sample was marked and cut into 25mm width strips, and the heat seal strength was determined by peel strength testing on an INSTRON® model 4464 test machine. The jaws were set 50 mm apart.
• the upper jaw held film piece of the sealed sample and travelled up at a speed of 250 mm/min, while the lower jaw held PP piece of the sealed sample and was stationary. The average force needed to separate the two pieces of film was recorded. Three sealed sample pieces were measured for each coated sample.
• the melting point of the EVA resin is determined by differential scanning calorimetry at a heating rate of 10°C/min according to ASTM D3418-15.
• PET polyethylene terephthalate
• the cast extrudate was heated to a temperature in the range of about 50 to 80°C and then stretched longitudinally at a forward draw ratio of about 3:1.
• the film was passed into a stenter oven at a temperature of 100°C where the film was stretched in the sideways direction to approximately 3 times its original dimensions.
• the biaxially stretched film was heat- set at a temperature of from 210°C to 230°C in a 3-stage crystallizer by conventional means.
• the PET film thickness was 23 ⁇ m.
• a PVDC primer coating was coated off-line at a coat weight of 0.5 g/m 2 to one surface of the PET film.
• a range of composite films were prepared by coating a heat-sealable coating formulation having the composition shown in Table 2 onto the primed surface of the PET substrate prepared as described above.
• the amounts of the components of the coating formulation are the amounts by weight of each component in the finished heat-sealable coating layer (i.e. the dry weight of the heat-sealable coating layer).
• the coating formulations in Table 2 were prepared at 20 wt% in toluene, except for Examples 1, 2 and 3 which were prepared at 15 wt% in toluene.
• the coating was conducted off-line by gravure coating at a coat- weight of 6.0g/m 2 .
• the composite films were heat-sealed (350°F; dwell time 0.1 second; pressure 80 psi) to a polypropylene substrate and the peel strengths of the composite films were tested as described herein. The results are provided in Table 2.
• the films according to the present invention exhibited an easy and clean peel when manually peeled from the tray.
• the films of Comparative Examples 1, 2 and 3 left a coating residue on the polypropylene substrate after peeling.
• Comparative Example 11 and Examples 12 to 16 A further series of composite films were prepared to investigate the effect of the vinyl acetate content of the EVA copolymer on peel strength and clarity.
• the films were prepared using the procedure described for Examples 5 to 10.
• the coating composition was constituted as follows:
• EVA resin 35.0 wt%
• Styrenic Block Copolymer Kraton® G1657ms 28.0 wt%
• Tackifier Piccolyte® Ml 15 35.5 wt%
• the EVA resin was varied as shown in Table 4 below.
• the coating formulations were prepared at 20 wt% in toluene and off-line coated by gravure coating at a coat-weight of 6.0g/m 2 onto the PVDC-primed surface of the PET substrate described above.
• the clarity and peel strength of each composite film, measured as described herein, are in Table 4.
• Table 4 The results in Table 4 demonstrate that clarity generally decreases with increasing VA content of the EVA resin. The results also demonstrate that adhesion performance becomes unsatisfactory as the VA content is reduced to zero.
• Example 12 A further series of composite films were prepared to investigate the effect of the amount of EVA copolymer in the coating layer on the peel strength. Comparative Example 12 was based on Example 6, except that the amount of Elvax®4260 was varied as shown in Table 6 below, which also shows the peel strength performance. The composition of the coating layer and base layer, and the method of preparation of the composite film, were otherwise identical to Example 6. Table 6

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