Patent Application
20190283383
The present U.S. patent application claims priority to European Patent Application No. 18161559.2, filed Mar. 13, 2018, the disclosure of which is incorporated herein by reference in its entirety.
The invention relates to a multilayer plastic film with high permeability to oxygen, to the use of such films and to polymer packaging comprising said film.
Plastic films are increasingly used for packing of different food species. Seafood is considered a food category with specific requirements as per the packing and distribution cycle, as under anaerobic conditions (e.g. vacuum) it may develop Clostridium botulinum toxin, which may prove lethal to consumers. A way to avoid this is to keep the pack temperature at temperatures lower than 3° C. This has proven to be unrealistic with the current distribution status especially after reaching the supermarket or retail point.
Based on this, the FDA has set a rule that a plastic film can be used for vacuum packing of seafood if the oxygen permeability of the pack, measured as per ASTM D3985 is higher than 10,000 cc/m2*atm*24 h. It is a challenge for the skilled person to produce a film with high permeability while keeping its functional and organoleptic properties.
Thus, one problem of the present invention is to provide plastic films with sufficient oxygen permeability, while keeping at the same time the functional and organoleptic properties of the film. It is a further desired effect of the film to be able to be used in a thermoforming and/or a vacuum skin packaging process.
Thermoforming is a known packaging process in which a container (e.g. a tray) is formed by a plastic film in a mold by application of vacuum, air pressure or a plug under increased temperature. Then food is placed in the container and air is drawn from the packaging prior to sealing it close. Such vacuum packaging has very good storage and preservation characteristics.
Thermoforming process in general involves two packaging films
Vacuum skin packaging (VSP) is in one sense a type of thermoforming process in which an article to be packaged serves as a mold of the forming web. An article may be placed on a rigid or semi-rigid support member, that can be flat or shaped e.g. tray-shaped (herein referred as “bottom web”) and the supported article is then passed to a chamber where a flexible film (herein referred as “top” or “skin” film) is first drawn against a heated dome and then draped down over the article. The movement of the top web is controlled by vacuum and/or air pressure and in a vacuum skin packaging arrangement, the interior of the container is vacuumized before final welding of the top web to the bottom web. The distinguishing feature of the vacuum skin package is that the upper heated film forms a tight skin around the product and is sealed to the part of the bottom web that is not covered by the product.
Because of the aesthetic appeal of the thermoforming and especially the VSP packs, it is highly desirable to pack seafood in these configurations. But as said before, the film must conform to the high oxygen permeability requirement.
Another desirable effect of the film is to be able to seal and peel directly to APET (amorphous PET) or PP (polypropylene) trays. This allows the packer to use simpler and cheaper trays than APET or PP laminated to a polyethylene based sealing layer that allows an efficient sealing between the bottom and top films.
Different approaches have been followed in order to develop such a film.
EP 1 599 337 A1 describes the use of a thick oxygen permeable layer alongside a thin seal layer and outer layer. The preferred oxygen permeable material is ethylene butyl acrylate copolymer which is known to be odorous. Thus there is a need to use odorless ethylene alpha olefin copolymers to keep the organoleptic properties. However, such polymers are challenging to process (e.g. the screw pressures are increased to a very high level). Thus also this problem must be handled by the person skilled in the art.
US 2007/0275196 A1 describes the use of styrenic rubbers in order to make such films stiffer and easier to process in the packing equipment e.g. in a Vertical Form-Fill-Seal (VFFS) machine. However, as these materials are known to be very sticky, their used in VSP equipment is questionable, given the adherence of the outer layer of the film to a heated dome.
Thus, it is an object of the present invention to avoid the above mentioned deficiencies of the known films and to provide a film with sufficient oxygen permeability, good organoleptic properties, efficient processing properties and sealability to an APET tray.
The present invention provides a multilayer film comprising: an intermediate layer comprising an ethylene alpha olefin copolymer of density 0.855-0.895 in a blend with at least 10% LDPE per weight, an outer layer comprising an ethylene alpha olefin copolymer of density 0.92 to 0.950, a sealing layer comprising EMA and/or EVA.
Preferably the density of the ethylene alpha olefin copolymer of the intermediate layer is in the range 0.860 to 0.885 g/cc.
Preferably the film comprises an additional intermediate layer of a blend of ethylene alpha olefin copolymer and LDPE.
The present invention further relates to the use of the multilayer film according to the present invention as top lidding film and/or bottom film in a thermoforming process.
The present invention further relates to the use of the multilayer film according to the present invention for packaging food, preferably sea food.
In a further embodiment the present invention relates to a polymer packaging comprising a top lidding film and a bottom film, wherein the top lidding film is a multilayer film according to the invention, and as bottom film is also a multilayer film according to the present invention or APET.
The inventors found out that the above film has surprisingly a preferred oxygen permeability of more than 10,000 cc/m2*atm*24 h measured according to ASTM D3985 at 23° C. and 0% relative humidity, more preferably of more than 11,000 cc/m2*atm*24 h.
As used herein, the term “plastic film” or simply “film” refers to a flat or tubular flexible structure of thermoplastic material.
The term “bottom film” refers to a film which is converted to a formed flexible tray during thermoforming process.
The term “top lidding film” or simply “top film” refers to a film which seals to the bottom film during the thermoforming process.
The term “skin film” refers to a film that forms and drapes over a food product during the VSP process.
The term “outer layer” refers to the film that is in immediate contact with the outside environment (atmosphere).
The term “inner layer” refers to the film that comes in contact with the product packed. It is also called “sealing layer” as this layer must be hermetically sealed in order to protect the product from ingress of air.
The term “intermediate layer” refers to any layer of the film that is neither the outer nor the inner layer. A film may comprise more than one intermediate layer.
As used herein the term “homopolymer” refers to a polymer resulting from polymerization of single monomers.
As used herein, the term “copolymer” refers to a polymer resulting from polymerization of at least two different monomers.
As used herein, the term “polymer” includes both types of homopolymers and copolymers.
As used herein, the term “polyolefin” includes all the products produced by polymerization of olefins. Polyethylene and polypropylene homopolymers and copolymers are the most common polyolefins.
As used herein, the term “polyethylene” identifies polymers comprising basically ethylene repeating units. Polyethylene homopolymers may be HDPE (high density polyethylene) or LDPE (low density polyethylene) as well known in the art.
As used herein the term “ethylene alpha olefin copolymers” refers to copolymers of ethylene with butene, hexene, octene or other alkenes. Such polymers are linear low density polyethylene (LLDPE), medium density polyethylene (MDPE), very low density polyethylene (VLDPE), ultra-low density polyethylene (ULDPE), metallocene catalyzed polyethylene and polyethylene plastomers and elastomers.
In the scope of the present application, the term “copolymer” may include the maleic anhydride modified polymers, often used as adhesives to bond dissimilar materials.
As used herein the term “homogeneous ethylene alpha olefin copolymers” refer to ethylene alpha olefin copolymers having a molecular weight distribution (Mw/Mn) of less than 2.7 as measured by GPC.
As used herein the term “styrene polymers” refers to styrene homopolymer such as polystyrene and to styrene copolymers such as styrene-butadiene copolymers, styrene-butadiene-styrene copolymers, styrene-isoprene-styrene copolymers, styrene-ethylene-butadiene-styrene copolymers and the like.
As used herein the term “ethylene methacrylate copolymers” refers to polymers of ethylene and methacrylate. EMA is abbreviation for this polymer.
As used herein the term “ethylene butyl acrylate” refers to polymers of ethylene and butyl acrylate. EBA is abbreviation for this polymer.
As used herein the term “ethylene vinyl acetate copolymers” refers to polymers of ethylene and vinyl acetate. EVA is abbreviation for this polymer.
As used herein the term “ethylene vinyl alcohol” or EVOH refers to saponified products of ethylene vinyl acetate polymers. The ethylene content is typically in the range of 25 to 55% per mol.
As used herein the term PVDC refers to vinylidene chloride copolymer wherein a major amount of the copolymer comprises vinylidene chloride and a minor amount of the copolymer comprises one or more monomers such as vinyl chloride and or/alkyl acrylates and methacrylates.
As used herein the term “polyamide” refers to well-known polymers such as polyamide 6, polyamide 66, polyamide 610, polyamide 6/66, polyamide 6/12, polyamide 11, polyamide 12, polyamide 6/66/12, polyamide 6/66/11, amorphous polyamides, aromatic polyamides and others.
As used herein, the term “ionomer” refers to ethylene-acid copolymers which have been neutralized by metal cations such as sodium, zinc, lithium or others. The acid used is usually methacrylic or acrylic acid.
As used herein the term “ethylene acid copolymer” refers to copolymers of ethylene with acid, most usually methacrylic or acrylic acid.
As used herein, the term “polyester” includes polymers such as PET (polyethylene terephthalate) in amorphous, semi crystalline or crystalline state, PETG (glycol modified polyethylene terephthalate), PBT (polybutylene terephthalate, PTT (polytrimethylene terephthalate), PBN (polybutylene naphthalate), PEN (polyethylene naphthalate), polyester block copolymers and others.
As used herein the term “polybutylene” refers to butene-1 homopolymers and copolymers.
As used herein the term “cycloolefin copolymers” refers to copolymers of olefins with cyclic monomers such as norbornene.
As used herein the term “hot blown film” refers to a film production process where the film is oriented from the melt state. The hot blown film may be cooled by air, water or other cooling media. Tubular dies as well known in the art are used for this process as opposed to cast production process.
The present invention provides a multilayer film comprising an intermediate layer comprising an ethylene alpha olefin copolymer of density 0.855-0.895 in a blend with at least 10% LDPE per weight, an outer layer comprising an ethylene alpha olefin copolymer of density 0.92 to 0.950, a sealing layer comprising EMA and/or EVA.
Preferably, the density of the ethylene alpha olefin copolymer of the intermediate layer is in the range 0.860 to 0.885 g/cc.
In a further preferred embodiment the multilayer film comprises an additional intermediate layer of a blend of ethylene alpha olefin copolymer and LDPE.
The multilayer film has preferably an oxygen permeability of more than 10,000 cc/m2*atm*24 h as measured according to ASTM D3985 at 23° C. and 0% relative humidity, and more preferably an oxygen permeability of more than 11,000 cc/m2*atm*24 h as measured according to ASTM D3985 at 23° C. and 0% relative humidity.
The present invention further relates to the use of the multilayer film according to the present invention as top lidding film and/or bottom film in a thermoforming process.
The present invention further relates to the use of the multilayer film according to the present invention for packaging food, preferably sea food.
In a further embodiment the present invention relates to a polymer packaging comprising a top lidding film and a bottom film, wherein the top lidding film is a multilayer film according to the invention, and as bottom film is also a multilayer film according to the present invention or APET.
Preferably the film is produced by the hot blown film method.
Preferably the film is of the structure:
or
or
or films with more than seven layers, e.g. up to 20 layers, comprising additional INTERMEDIATE LAYERs.
The intermediate layers may have the same or different compositions.
The film of the present invention may have a thickness from 14 to 120 microns, preferably 50 to 90 microns, even more preferably 60 to 80 microns.
The sealing layer comprises EVA and/or EMA. Appeel® from Dupont or Lotryl® Bestpeel from Arkema are preferred.
The sealing layer must be sealable to APET. This means that the heat seal strength of the film to APET trays must be more than 2N/15 mm in at least a temperature of range 120-200° C. under a typical heat seal time of 2 seconds and seal pressure of 3 bars. The two films are heat sealed and the seal strength is measured at a 15 mm width according to ASTM F88.
The film comprises at least one intermediate layer comprising a blend of an ethylene alpha olefin copolymer of density 0.855-0.895 g/cc and at least 10% wt of low density polyethylene (LDPE). Preferably the density of the ethylene alpha olefin copolymer is from 0.860 to 0.885 g/cc.
Preferably, at least a second intermediate layer comprises an ethylene alpha olefin copolymer of density 0.855-0.895 g/cc in a blend with LDPE.
The film may comprise further intermediate layers comprising ethylene alpha olefin copolymer of density 0.855-0.895 g/cc, preferably the density is from 0.860 to 0.885 g/cc.
The use of LDPE in the blends with such low density alpha olefin copolymers improve
The outer layer comprises an ethylene alpha olefin copolymer of density 0.920 to 0.950. Using an ethylene alpha olefin copolymer with said specific density of 0.920 to 0.950 the film works in the proximity of a heated dome (VSP process) while surprisingly the oxygen permeability is maintained at high levels.
Preferably the thickness of the outer layer is less than 5 microns, more preferably less than 3 microns.
The film preferably undergoes ionizing radiation crosslinking in a dose of at least 5 megarads. Gamma radiation crosslinking is also possible.
Preferably the film is produced by the hot blown film method.
In a commercial blown film line, the following plastic films were produced
EAO1=an ethylene hexene copolymer of density 0.934
EAO2=an ethylene octene copolymer of density 0.870
LDPE=a low density polyethylene of density 0.924
EMA1=An EMA based peel seal material
Production of the film (sample 1) was stable with no processing issues.
Production of the film (sample 2) was stable with no processing issues.
Same film as example 2 but all intermediate layers contained 100% EAO2 and no LDPE.
In Example 3 a deterioration of the processing behavior of the film was noticed. There were frequent breakages possibly due to the inadequate melt strength of the film. Further to this the extruder pressures increased substantially and the line productivity significantly decreased.
Prior to further testing both samples 1 and 2 were irradiated at a dose of 12 MRads.
The above irradiated samples were tested at a commercial thermoforming machine and a commercial VSP machine.
Both films were tested as both top lidding films and bottom films in thermoforming. Surprisingly, both films could function as both top lidding and bottom films.
Both films were tested as skin films with good results. Irradiated sample 1 was sealed to APET to form pack 1. Irradiated sample 2 was sealed to APET to form pack 2.
Sealing strength to APET sheet was measured in Instron machine per 15 mm width according to ASTM F88.
Seal strength of pack 1 and of pack 2 was average 6N/15 mm. There were no leakages and unsealed areas.
A panel of five people evaluated the smell of the films in comparison to a commercial high barrier VSP film of FLEXION series. It was concluded that the organoleptic properties of the film were similar to the commercial film (acceptable).
Both films were tested as per oxygen permeability according to ASTM D3985 at conditions 23° C., 0% RH.
Film 1 had an oxygen permeability of 11,200 cc/m2*atm*24 h while film 2 showed an oxygen permeability of 11,800.
| Number | Date | Country | Kind |
|---|---|---|---|
| 18161559.2 | Mar 2018 | EP | regional |
