CA2106889C - Multi-ply backseamable film - Google Patents
Multi-ply backseamable film Download PDFInfo
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- CA2106889C CA2106889C CA 2106889 CA2106889A CA2106889C CA 2106889 C CA2106889 C CA 2106889C CA 2106889 CA2106889 CA 2106889 CA 2106889 A CA2106889 A CA 2106889A CA 2106889 C CA2106889 C CA 2106889C
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Abstract
A multilayer heat-shrinkable film is provided which includes at least one heat sealing layer which is a blend of a propylene copolymer and a homogeneous ethylene alpha-olefin copolymer having a density below about 0.90 g/cc. Prefera-bly, the outermost layer is compatible with the. heat sealing layer for ready formation of a lap seal for end use applica-tions such as backseamed casings. An internal polyamide-con-taining layer provides excellent elastic recovery:
Description
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~iULTI-PLY BACKSEAMABLE FILM
FTELD OF TILE INVENTION
The field of the invention is a packaging film from which bags and casings can. be made which have improved struc-tural soundness so that they may be fully aharacteri~ed as "cook-in." The term "cook-in" as used herein is intended to refer to packaging material structurally capable of withstand-ing exposure to time-temperature conditions while containing a food product.
This invention relates generally to thermoplastic films suitable for cook-in packaging; and more particularly to food cook-in films. These films may have food contact surf ace characteristics which promote binding adherence to a contained food product during cook-in. The films of the invention exhib-it improved hot and cold seal strength, improved optics and are more readily processable than known films. The present invention is particularly directed to backseamed casings.
PRIOR ART
Cook-in packaged'foods are essentially foods cooked in the package in which they are distributed to the consumer and which may be consumed with or without warming. Cook-in time-temperature conditions typically refer to a long slow cook, for example, submersion in hot water at about 55°C to about 65°C for about 1 to about 4 hours. These conditions are repre-5/920915.1/SPECFLDR
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sentative of institutional c~o~ g~requirements. Submersion at about 7 0 ° C to about 10 0 ° C f or up to about 12 hours repre-sents the limiting case. Under such conditions, a cook-in packaging material should maintain seal integrity, i.e., any heat sealed seams should resist being pulled apart during cook-in. The film should also be heat sealable to itself and, the packaging film substantially conformable to the contained food product. Preferably, this substantial conformability is achieved by the film being heat shrinkable under these condi-tions so as to form a tightly fitting package, i.e., the film should be heat shrinkable under these time-temperature condi-tions and should possess sufficient shrink energy so that submerging the packaged food product in hot water will shrink the packaging film snugly around the contained product, and especially up to about 55o monoaxial and/or biaxial shrink-age.
The film may also have food product adherence to re-strict "cook-oft" or collection of juices between the surface of the contained food product and the food contact surface of the packaging material during cook-in, thereby increasing product yield. More particularly, in the types of multilayer films wherein the first "sealing and food contact" layer is of the type of material that adheres to a contained food product during cook-in, this first layer may alternatively be referred to as the "adhering layer." As used herein, the term "adhere"
is intended to mean that the food contact surface of the film bonds during cook-in to the contained food product to an ex-tent sufficient to substantially prevent accumulation of flu-ids between the ~ilm and the contained product.
A heat shrinkable, cook-in film is described by Oberle et al, U. S. Patent No. 4,469,742 that includes a first "seal-ing or food contact" layer of a nonlipophillic polymeric mate-rial which has a softening point greater than that of the following shrink layer; a second layer, of an ethylene homopol-ymer or copolymer melt bonded to the first layer; a third or adhesive layer, melt bonded to the second layer, of a chemical-5/920915.1/SPECFLDR
~iULTI-PLY BACKSEAMABLE FILM
FTELD OF TILE INVENTION
The field of the invention is a packaging film from which bags and casings can. be made which have improved struc-tural soundness so that they may be fully aharacteri~ed as "cook-in." The term "cook-in" as used herein is intended to refer to packaging material structurally capable of withstand-ing exposure to time-temperature conditions while containing a food product.
This invention relates generally to thermoplastic films suitable for cook-in packaging; and more particularly to food cook-in films. These films may have food contact surf ace characteristics which promote binding adherence to a contained food product during cook-in. The films of the invention exhib-it improved hot and cold seal strength, improved optics and are more readily processable than known films. The present invention is particularly directed to backseamed casings.
PRIOR ART
Cook-in packaged'foods are essentially foods cooked in the package in which they are distributed to the consumer and which may be consumed with or without warming. Cook-in time-temperature conditions typically refer to a long slow cook, for example, submersion in hot water at about 55°C to about 65°C for about 1 to about 4 hours. These conditions are repre-5/920915.1/SPECFLDR
~ n.
sentative of institutional c~o~ g~requirements. Submersion at about 7 0 ° C to about 10 0 ° C f or up to about 12 hours repre-sents the limiting case. Under such conditions, a cook-in packaging material should maintain seal integrity, i.e., any heat sealed seams should resist being pulled apart during cook-in. The film should also be heat sealable to itself and, the packaging film substantially conformable to the contained food product. Preferably, this substantial conformability is achieved by the film being heat shrinkable under these condi-tions so as to form a tightly fitting package, i.e., the film should be heat shrinkable under these time-temperature condi-tions and should possess sufficient shrink energy so that submerging the packaged food product in hot water will shrink the packaging film snugly around the contained product, and especially up to about 55o monoaxial and/or biaxial shrink-age.
The film may also have food product adherence to re-strict "cook-oft" or collection of juices between the surface of the contained food product and the food contact surface of the packaging material during cook-in, thereby increasing product yield. More particularly, in the types of multilayer films wherein the first "sealing and food contact" layer is of the type of material that adheres to a contained food product during cook-in, this first layer may alternatively be referred to as the "adhering layer." As used herein, the term "adhere"
is intended to mean that the food contact surface of the film bonds during cook-in to the contained food product to an ex-tent sufficient to substantially prevent accumulation of flu-ids between the ~ilm and the contained product.
A heat shrinkable, cook-in film is described by Oberle et al, U. S. Patent No. 4,469,742 that includes a first "seal-ing or food contact" layer of a nonlipophillic polymeric mate-rial which has a softening point greater than that of the following shrink layer; a second layer, of an ethylene homopol-ymer or copolymer melt bonded to the first layer; a third or adhesive layer, melt bonded to the second layer, of a chemical-5/920915.1/SPECFLDR
1y modified polyethylene beir~'~ ~~r'a~~.~tively cross-linkable and having functional groups with a relatively strong affinity for the following barrier layer; a fourth or barrier layer of a hydrolyzed ethylene vinyl acetate copolymer melt bonded to the third layer; a fifth or adhesive layer as in said third layer, melt bonded to the fourth layer; and a sixth or abuse layer, melt bonded to the fifth layer. In one embodiment, the first "sealing and food contact" layer is an ionomer, a metal salt neutralized copolymer of an olefin and a carboxylic acid, representatively Surlyn(TM), which is a type of material that adheres to a contained meat product during cook-in. This Surlyn(TM) layer also functions as a protein-adhering layer.
In another embodiment, the sealing layer is a propylene-ethylene random copolymer having from to to 6o by weight of ethylene: The patent also describes a method for making the film including full coextrusion and selective irradiation and orientation.
In the conventional method of manufacturing heat shrink-able film as described by Oberle et al, a tubular orientation process is utilized wherein a primary tube of the film is biaxially oriented by formation of a bubble to create internal pressure and induce stretching in the transverse direction and with the use of pinch rolls at different speeds to induce stretching in the machine direction. The films of the present invention are easily oriented with the incidence of bubble breakage during orientation minimized, and in some cases, eliminated. The stretched bubble is then collapsed, and may be wound up as flattened, seamless, tubular film to use later to make bags, e~.g., either end-seal bags typically made by transversely heat sealing across the width of flattened tubing followed by severing the tubing so that the transverse seal forms the bag bottom, or side-seal bags in which the trans-verse heat seals farm the bag sides and one edge of the tubing forms the bag bottom. Such bags are typically used by placing the food product in the bag, evacuating the bag, and either heat sealing the bag mouth or gathering and applying a metal clip around the gathered mouth of the bag to form a seal.
5/920915.1/SPECELDR
In another embodiment, the sealing layer is a propylene-ethylene random copolymer having from to to 6o by weight of ethylene: The patent also describes a method for making the film including full coextrusion and selective irradiation and orientation.
In the conventional method of manufacturing heat shrink-able film as described by Oberle et al, a tubular orientation process is utilized wherein a primary tube of the film is biaxially oriented by formation of a bubble to create internal pressure and induce stretching in the transverse direction and with the use of pinch rolls at different speeds to induce stretching in the machine direction. The films of the present invention are easily oriented with the incidence of bubble breakage during orientation minimized, and in some cases, eliminated. The stretched bubble is then collapsed, and may be wound up as flattened, seamless, tubular film to use later to make bags, e~.g., either end-seal bags typically made by transversely heat sealing across the width of flattened tubing followed by severing the tubing so that the transverse seal forms the bag bottom, or side-seal bags in which the trans-verse heat seals farm the bag sides and one edge of the tubing forms the bag bottom. Such bags are typically used by placing the food product in the bag, evacuating the bag, and either heat sealing the bag mouth or gathering and applying a metal clip around the gathered mouth of the bag to form a seal.
5/920915.1/SPECELDR
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Alternatively, the collapsed tube may be slit into a film or two, or more films, depending on the width desired. The film can then be folded longitudinally about a forming shoe with opposed edges being joined in a lap seal in order to form a backseamed casing. Backseamed casings are often desirable when process limitations preclude formation of an oriented tube or sufficiently small diameter for a given cook-in appli-catian. However, the lap seal of such a casing requires that the inner layer of the cook-in material (optionally an adher-ing layer) is heat sealable to the outermost layer. This required sealing compatibility is most easily achieved by providing inner and outer layers of identical chemical composi-tion. However, the inner and outer layers need not be identi-cal as long as their respective compositions are sufficiently compatible for forming seals which are delamination resistant under rigorous cook-in conditions.
Formation of a backseamed .tube from a film may be by a continuous or ~an intermittent process. By the intermittent process the film is typically sealed to form a length of tub ing required for a given end-use application and then cut transversely. As the film indexes forward and the sealing and cutting steps are repeated, a series of tubular .casings of the desired diameter and length are provided. The casings may be clipped at one end for subsequent stuffing and clipping of the opposite end or they may be heat sealed and treated as bags produced from seamless tubing. Alternatively, an intermittent process may be employed for forming a continuous tube so long as the individually formed seals have at least some overlap.
By the continuous process the entire length of the film is sealed to form a continuous tuba for later clipping, stuffing and clipping.
Cook-in tubing, whether seamless or backseamed, may be shirred; that is, folded or pleated into a relatively short length for ease of handling during stuffing. Regardless of the method of manufacture, the bag or casing is then immersed in hot water at. approximately the same temperature at which 5/920915.1/SPECFLDR
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Alternatively, the collapsed tube may be slit into a film or two, or more films, depending on the width desired. The film can then be folded longitudinally about a forming shoe with opposed edges being joined in a lap seal in order to form a backseamed casing. Backseamed casings are often desirable when process limitations preclude formation of an oriented tube or sufficiently small diameter for a given cook-in appli-catian. However, the lap seal of such a casing requires that the inner layer of the cook-in material (optionally an adher-ing layer) is heat sealable to the outermost layer. This required sealing compatibility is most easily achieved by providing inner and outer layers of identical chemical composi-tion. However, the inner and outer layers need not be identi-cal as long as their respective compositions are sufficiently compatible for forming seals which are delamination resistant under rigorous cook-in conditions.
Formation of a backseamed .tube from a film may be by a continuous or ~an intermittent process. By the intermittent process the film is typically sealed to form a length of tub ing required for a given end-use application and then cut transversely. As the film indexes forward and the sealing and cutting steps are repeated, a series of tubular .casings of the desired diameter and length are provided. The casings may be clipped at one end for subsequent stuffing and clipping of the opposite end or they may be heat sealed and treated as bags produced from seamless tubing. Alternatively, an intermittent process may be employed for forming a continuous tube so long as the individually formed seals have at least some overlap.
By the continuous process the entire length of the film is sealed to form a continuous tuba for later clipping, stuffing and clipping.
Cook-in tubing, whether seamless or backseamed, may be shirred; that is, folded or pleated into a relatively short length for ease of handling during stuffing. Regardless of the method of manufacture, the bag or casing is then immersed in hot water at. approximately the same temperature at which 5/920915.1/SPECFLDR
the film was stretch oriented, typically about 160° to 205°F.
(61° to 96°C), hot water immersion being one of the quickest and most economical means of transferring sufficient heat to the film to shrink it uniformly. Alternatively, the bag, film or casing may serve as a liner of a cooking mold.
A plastic, adhering cook-in package such as a casing is described by Schirmer, in U. S. Patent No. 4,606,922 as well as a method for enhancing yield of a cook-in packaged meat product.' The method includes first providing an adhering cook-in container including a flexible thermoplastic envelope being substantially conformable to a contained meat product and having an inner meat-contacting surface of a selectively irradiated ionomer, then conforming the container about a selected meat product and cooking the packaged product, where-upon the inner surface of the envelope bonds to the meat prod-uct substantially to prevent cook-out of fluids.
A flexible plastic adhering cook-in package is de-scribed by Thompson in U. S. Patent No. 4,411,919, as well as a method for enhancing yield of cook-in packaged meat prod-uct. The method includes: providing an adhering cook-in package comprising a flexible plastic container substantially conformable to a selected meat product and having an inner meat product contacting surface of polymeric olefin. This container is subjected to an energetic radiation surface treat-ment in the presence of oxygen sufficient to cause the inner surface to adhere to the meat product during cook-in, the container having been formed from hot blown tubular film. The package is conformed about a selected meat product followed by cooking the packaged product, whereupon the inner surface adheres to the meat product to substantially prevent cook-out of fluids.
Erk pt al, U. S. Patent No. 4,303,711, describes a tubular film consisting of biaxially stretched plastic materi-al for packing and casing, paste type foodstuffs that are heated after packing or are packed in a hot fluid state. The 5/920915.1/SPECFLDR
f1 C1 film is a mixture of approximately 50-99 parts by weight of at least one aliphatic polyamide and approximately 1-50 parts by weight of one or more members of the group consisting of an ionomer resin, a modified ethylene vinyl acetate copolymer and a modified polyolefin.
Erk et al, U. S. Patent No. 4,601,929, relates to a single layer of polyamide film for packing and casing food-stuffs in paste form, especially foodstuffs that are packed when hot or are subject to heat treatment after packing.
Ghiradello et al, U. S. Patent No. 4,568,580, relates to an article of manufacture for packaging food products com-prising a first film section having at least one surface com-prising a copolyamide obtained by random copolymerization of precursor monomers of at least two different.polyamides. The article includes a second film section of a film having a surface comprising the aforesaid copolyamide and at least one heat weld between the copolyamide surfaces of said first and second film sections. The article is capable of withstanding heat treatment at temperatures from 70°C to 120°C for at least minutes without suffering damage to the heat weld.
Oberle, U. S. Patent No. 4,855,183 discloses a cook-in film having a first food contact layer comprising a polyamide composition.
obey 1e, U.S. Patent No. 4,762,748 describes a cook-in shrink film characterized by the presence of ethylene alkyl acrylate copolymer in core layer and abuse layers, in adhesive layers, or both. The sealing layer is selected from the group consisting of a propylene ethylene copolymer, an ionomer, a blend of a linear low density polyethylene and an ionomer, and a blend. of a linear low density polyethylene and an ethylene acrylic acid copolymer.
Schirmer, U.S. Patent No. 4,448,792, describes a cook-in shrink bag having a sealing and food contact layer of a 5/920915.1/SPECFLDR
(61° to 96°C), hot water immersion being one of the quickest and most economical means of transferring sufficient heat to the film to shrink it uniformly. Alternatively, the bag, film or casing may serve as a liner of a cooking mold.
A plastic, adhering cook-in package such as a casing is described by Schirmer, in U. S. Patent No. 4,606,922 as well as a method for enhancing yield of a cook-in packaged meat product.' The method includes first providing an adhering cook-in container including a flexible thermoplastic envelope being substantially conformable to a contained meat product and having an inner meat-contacting surface of a selectively irradiated ionomer, then conforming the container about a selected meat product and cooking the packaged product, where-upon the inner surface of the envelope bonds to the meat prod-uct substantially to prevent cook-out of fluids.
A flexible plastic adhering cook-in package is de-scribed by Thompson in U. S. Patent No. 4,411,919, as well as a method for enhancing yield of cook-in packaged meat prod-uct. The method includes: providing an adhering cook-in package comprising a flexible plastic container substantially conformable to a selected meat product and having an inner meat product contacting surface of polymeric olefin. This container is subjected to an energetic radiation surface treat-ment in the presence of oxygen sufficient to cause the inner surface to adhere to the meat product during cook-in, the container having been formed from hot blown tubular film. The package is conformed about a selected meat product followed by cooking the packaged product, whereupon the inner surface adheres to the meat product to substantially prevent cook-out of fluids.
Erk pt al, U. S. Patent No. 4,303,711, describes a tubular film consisting of biaxially stretched plastic materi-al for packing and casing, paste type foodstuffs that are heated after packing or are packed in a hot fluid state. The 5/920915.1/SPECFLDR
f1 C1 film is a mixture of approximately 50-99 parts by weight of at least one aliphatic polyamide and approximately 1-50 parts by weight of one or more members of the group consisting of an ionomer resin, a modified ethylene vinyl acetate copolymer and a modified polyolefin.
Erk et al, U. S. Patent No. 4,601,929, relates to a single layer of polyamide film for packing and casing food-stuffs in paste form, especially foodstuffs that are packed when hot or are subject to heat treatment after packing.
Ghiradello et al, U. S. Patent No. 4,568,580, relates to an article of manufacture for packaging food products com-prising a first film section having at least one surface com-prising a copolyamide obtained by random copolymerization of precursor monomers of at least two different.polyamides. The article includes a second film section of a film having a surface comprising the aforesaid copolyamide and at least one heat weld between the copolyamide surfaces of said first and second film sections. The article is capable of withstanding heat treatment at temperatures from 70°C to 120°C for at least minutes without suffering damage to the heat weld.
Oberle, U. S. Patent No. 4,855,183 discloses a cook-in film having a first food contact layer comprising a polyamide composition.
obey 1e, U.S. Patent No. 4,762,748 describes a cook-in shrink film characterized by the presence of ethylene alkyl acrylate copolymer in core layer and abuse layers, in adhesive layers, or both. The sealing layer is selected from the group consisting of a propylene ethylene copolymer, an ionomer, a blend of a linear low density polyethylene and an ionomer, and a blend. of a linear low density polyethylene and an ethylene acrylic acid copolymer.
Schirmer, U.S. Patent No. 4,448,792, describes a cook-in shrink bag having a sealing and food contact layer of a 5/920915.1/SPECFLDR
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propylene homopolymer or copolymer, preferably a propylene-ethylene copolymer of low ethylene content. A core layer adjacent the sealing layer is a blend of a propylene homopoly-mer or copolymer. Also included are a barrier layer, an abuse layer and adhesive layers sandwiching the barrier.
Oberle, U.S. Patent No. 4,879,124, describes a perforat-ed cook-in shrink bag. Preferable materials for the sealing layer include ethylene-acrylic acid copolymers, ethylene methacrylic acid copolymers, ionomers and blends of such.
Schirmer, U.S. Patent No. 4,608,302, describes oriented ..S
films from propylene copolymers and unplasticized Saran which are suitable for use in the packaging of prepared food prod-ucts. A core layer may comprise an ethylene vinyl acetate copolymer having a vinyl acetate content if from loo to 12o by weight and a fractional melt index. The core layer is adja-cent a sealing layer which is a propylene homopolymer or copolymer which may be a propylene ethylene copolymer.
Bekele, U.S. Patent No. 4,909,726, describes an impact resistant film for chub packaging. Various layers may contain ?a.' polymeric materials of fractional melt index.
Mueller, U.S. Patent No. 4,977,022, describes a barrier =w stretch film with at least one interior layer which may com prise an ethylene vinyl acetate copolymer of fractional melt index.
Schirmer, ~.U.S. Patent No. 4,937,112, describes a film for chub packaging which includes an olefin sealing layer and a core layer adjacent the sealing layer which comprises a polymeric material of high molecular weight and fractional melt index selected from the group consisting of high density .;
polyethylene, low density polyethylene and ethylene vinyl acetate copolymer.
5/920915.1/SPECFLDR
propylene homopolymer or copolymer, preferably a propylene-ethylene copolymer of low ethylene content. A core layer adjacent the sealing layer is a blend of a propylene homopoly-mer or copolymer. Also included are a barrier layer, an abuse layer and adhesive layers sandwiching the barrier.
Oberle, U.S. Patent No. 4,879,124, describes a perforat-ed cook-in shrink bag. Preferable materials for the sealing layer include ethylene-acrylic acid copolymers, ethylene methacrylic acid copolymers, ionomers and blends of such.
Schirmer, U.S. Patent No. 4,608,302, describes oriented ..S
films from propylene copolymers and unplasticized Saran which are suitable for use in the packaging of prepared food prod-ucts. A core layer may comprise an ethylene vinyl acetate copolymer having a vinyl acetate content if from loo to 12o by weight and a fractional melt index. The core layer is adja-cent a sealing layer which is a propylene homopolymer or copolymer which may be a propylene ethylene copolymer.
Bekele, U.S. Patent No. 4,909,726, describes an impact resistant film for chub packaging. Various layers may contain ?a.' polymeric materials of fractional melt index.
Mueller, U.S. Patent No. 4,977,022, describes a barrier =w stretch film with at least one interior layer which may com prise an ethylene vinyl acetate copolymer of fractional melt index.
Schirmer, ~.U.S. Patent No. 4,937,112, describes a film for chub packaging which includes an olefin sealing layer and a core layer adjacent the sealing layer which comprises a polymeric material of high molecular weight and fractional melt index selected from the group consisting of high density .;
polyethylene, low density polyethylene and ethylene vinyl acetate copolymer.
5/920915.1/SPECFLDR
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U.5. Patent No. 4,495,249 issued to Ohya et al disclos-es a multi-layer laminate film with a core layer of a hydrolized ethylene-vinyl acetate copolymer, and two outer layers of a mixture of copolymer of ethylene and vinyl acetate and a copolymer of propylene and ethylene or linear low densi-ty polyethylene. The multilayer laminate film of the refer-ence can be made heat shrinkable and has gas barrier proper-ties.
U.5. Patent No. 4,182,457 (Yamada et al) discloses a container with an EVOH core, adhesive layers, and additional layers of e.g. polypropylene or ethylene propylene copolymer.
U.5. Patent No. 4,511,610 (Yazaki et al) discloses a container with an EVOH core, adhesive layers, and additional layers of e.g. polypropylene or ethylene propylene copolymer.
U.5. Patent No. 4,405,667 issued to Christensen et al appears to di$close a retortable pouch having a linear low density polyethylene heat seal layer, a second layer of a blend of linear low density polyethylene and propylene ethylene copolymer, optional third, fourth, and fifth layers of propylene ethylene copolymer, a sixth layer of an anhydride modified polypropylene, a seventh layer of nylon, an eighth layer of EVOH and a ninth layer o:r nylon.
U.S. Patent No. 4,532,189 issued to Mueller discloses a shrink film having two skin layers each comprising e.g. a blend of polypropylene and ethylene propylene copolymer.
Also of interest is U.S. Patent No. 4,400,428 issued to Rosenthal et a1 which discloses a composite film having a biaxially oriented polypropylene based film (BOPP) laminated on at least one surface with a multilayer structure including a gas barrier layer of a hydrolyzed ethylene vinyl acetate copolymer and a layer adaacent to the base film, and a heat sealable outer layer which may be, for example, modified propylene/ethylene copolymer.
/ 9 2 0 915 .1 / SPECELIaR
U.5. Patent No. 4,495,249 issued to Ohya et al disclos-es a multi-layer laminate film with a core layer of a hydrolized ethylene-vinyl acetate copolymer, and two outer layers of a mixture of copolymer of ethylene and vinyl acetate and a copolymer of propylene and ethylene or linear low densi-ty polyethylene. The multilayer laminate film of the refer-ence can be made heat shrinkable and has gas barrier proper-ties.
U.5. Patent No. 4,182,457 (Yamada et al) discloses a container with an EVOH core, adhesive layers, and additional layers of e.g. polypropylene or ethylene propylene copolymer.
U.5. Patent No. 4,511,610 (Yazaki et al) discloses a container with an EVOH core, adhesive layers, and additional layers of e.g. polypropylene or ethylene propylene copolymer.
U.5. Patent No. 4,405,667 issued to Christensen et al appears to di$close a retortable pouch having a linear low density polyethylene heat seal layer, a second layer of a blend of linear low density polyethylene and propylene ethylene copolymer, optional third, fourth, and fifth layers of propylene ethylene copolymer, a sixth layer of an anhydride modified polypropylene, a seventh layer of nylon, an eighth layer of EVOH and a ninth layer o:r nylon.
U.S. Patent No. 4,532,189 issued to Mueller discloses a shrink film having two skin layers each comprising e.g. a blend of polypropylene and ethylene propylene copolymer.
Also of interest is U.S. Patent No. 4,400,428 issued to Rosenthal et a1 which discloses a composite film having a biaxially oriented polypropylene based film (BOPP) laminated on at least one surface with a multilayer structure including a gas barrier layer of a hydrolyzed ethylene vinyl acetate copolymer and a layer adaacent to the base film, and a heat sealable outer layer which may be, for example, modified propylene/ethylene copolymer.
/ 9 2 0 915 .1 / SPECELIaR
u_ ~~ l~ (~ !'~ p EPO Patent Application No. 0149321 discloses a heat shrinkable tubular film having a gas barrier layer of vinylidene chloride copolymer, outer layers of polyolefin such as ethylene propylene copolymer, polypropylene and mixtures thereof, at least one intermediate layer of for example a polyamide, and adhesive layers disclosed between any of the above layers.
U.K. Patent Application GB 2,139,948A discloses a multilayer, preferably coextruded fiber-layer heat sealable film having a surface layer of a heat sealable polymer such as linear low density polyethylene of LLDPE blended With other polymers such as EVA, an EVOH layer, and a layer of polypropylene. These layers can be bonded by polymeric adhe-sive tie layers.
U.K. Patent Application GB 2,221,649 discloses a compos-ite film with improved heat shrinkable properties comprising a core layer of a copolymer or propylene and one or more alpha-olefins having a Vicat softening point of 70-110°C and two outer layers of a crystalline polypropylene resin having a melting point of 135-150°C.
EPO Patent Application No. 435498-A is directed to a multilayer heat-shrinkable film which includes a heat sealing layer which is a copolymer of propylene and at least two other alpha-olefins .
Japanese Patent Application 3063133-A is directed to a heat shrinkable ~multilayer film which includes at least one layer which is a blend of an aliphatic polyamide and a non' crystalline polyamide.
Japanese Patent Application 3121842-A is directed to a packaging material which contains an inner layer which is a polyamide/polyethylene blend.
5/920915.1/SPECFLDR
,.... 9 German Patent Application 3943024-A is directed to a monolayer casing which is a blend of nylon 6 and a copolyamide.
Summary of the Invention The present invention provides a novel cook-in film which is readily biaxially oriented. Further, the present invention provides a novel cook-in film that has improved biaxial orientability as a tube by means of forming a bubble wherein bubble breakage is substantially minimized or eliminated. Further, the present invention provides a method for manufacturing such a novel cook-in film wherein the sealing layer comprises a blend of a propylene based copolymer and an ethylene alpha-olefin copolymer. Further, the present invention provides a method for manufacturing such a novel cook-in film wherein the outermost layer comprises a blend of a propylene based copolymer and an ethylene alpha-olefin copolymer. The present invention also provides a cook-in film with good elastic recovery for a tight package appearance. Still further, the present invention provides a cook-in film which can be formed into backseamed casings.
These as well as other aspects of the invention are achieved by providing a heat-shrinkable multilayer film which has a heat sealing outer layer of a blend of about 50%
to about 95% by weight of a propylene based copolymer and from about 5% to about 50% by weight of a homogeneous ethylene alpha-olefin copolymer having a density below about 0.90 g/cc. Such aspects are further achieved by providing such a film which also includes at least one layer containing a polyamide, a copolyamide, an amorphous copolyamide, or blends of such.
Additional aspects and advantages of the invention will be set forth in part in the description which follows and in part will be apparent to a person with ordinary skill in the art from the description, or may be learned by practice of the invention. The advantages of the invention may be realized and attained by means of the instrumentalities and combinations particularly pointed out in the appended claims.
Detailed Description ef the Invention The present invention is directed generally to multi-layer heat shrinkable films which have a heat sealing layer which is a blend of a propylene based copolymer and a homoge-neous ethylene alpha-olefin copolymer with a density below about 0.90 g/cc. Specifically, films with improved process-ability and heat seal characteristics in accordance with the present invention have the structure: (inner sealing and food contact layer)/(nylon layer)/outer sealing layer) or (inner sealing and food cor_tact layer)/(nylon layer)/(barrier lay-er)/(outer sealing layer). Here again, the inner sealing and food contact layer is a blend of a propylene based copolymer with an ethylene a~ pha-of efin copoiT .~er having a densi ty below about 0.90 g/cc. 'the propylene based copolymer is preferably an ethylene propylene copolymer which contains from about 94°-, to about 99-% by wei ght of propylene and from about 1% to about 6o by weight of ethylene.
Alternatively, the propylene based copolymer may be a copolymer of propylene with ethylene and butene. Such ethylene propylene butene copolymer should preferably contain from about 90% to about 99o by weight of propylene, from about 1% to about 6% by weight of ethylene, and from about to to abcut 10 o by weight oz butene. It SilOUld be noted that nor S's a (t ~
,~. ~~ t.u .~ LV
purposes of the present specification, the term "copolymer" is intended to broadly describe the products of polymerization of two or more comonomers.
Although the present heat sealing layer may comprise anywhere from 50o to about 95a by weight of such propylene based copolymer, a more preferred range is 70% to about 85%
with 750 of the heat sealing layer being the optimum amount of such copolymer. As noted above, the propylene based copolymer is blended with a homogeneous ethylene alpha-olefin copolymer which has a density below about 0.90 g/cc.
Ethylene alpha-olefins are, generally speaking, copolymers of ethylene with one or more comonamers selected from C3 to about C1o alpha olefins but especially compris-es ethylene copolymers with CQ to about C1o alpha olefins such as butane-1, pentane-1, hexane-1, octane-l, and the like, in which the polymer molecules comprise long chains with few side chains or. branches and sometimes are referred to as lin-ear polymers. These polymers are obtained by low pressure polymerization processes and the side branching which is present will be short compared to non-linear ethylenes.
Ethylene/alpha-olefin copolymers have a density in the range of fram about 0.860 g/cc to about 0.940 g/cc. The term linear low density polyethylene is generally understood to include that group of ethylene/alpha-olefin copolymers which fall into the density range of about 0.915 to about 0.940 g/cc. Some-times linear polyethylene in the density range from about 0.926 to about 0.940 is referred to a linear medium density polyethylene (LMDPE). Lower density ethylene alpha olefins may be referred to as very low density polyethylene (VLDPE, typically used to refer to the ethylene butane copolymers supplied by Union Carbide) and ultra-low density polyethylene (ULDPE,. typically used to refer to the ethylene octane copolymers supplied by Dow). It should be noted although specific density ranges is for VLDPE, ULDPE, LLDPE, and LMDPE
have been set forth herein, that no bright line can be drawn for density classification and such will vary by supplier.
5/920915.1/SPECFLDR
Heretofore, conventional ethylene alpha-olefins have been produced by Ziegler-Natta catalyst polymerization. The traditional Ziegler-Natta homogeneous system includes a metal halide activated by a metal alkyl cocatalyst. These are sys-tems in which there are various oxidation states of the metal, and a variety of ligand environments, depending upon where the site is located in the catalyst, all leading to a relatively broad molecular weight distribution and a generally heteroge-neous composition. Generally speaking, Ziegler-rT~tta cata-lysts incorporate comonomer poorly and produce some polymer chains with much comonomer and others with substantially less. Fox example, with conventional Ziegler-Natta catalysis, a linear ethylene alpha-olefin having an average of l00 comonomer may have a range of Oo to 40% comonomer in any given individual chain.
Recently a new type of ethylene based linear polymers have been introduced. These new resins are produced by metallacene catalyst polymerization and are characterized by narrow or more homogenous compositional properties, such as molecular weight distribution, than resins produced by conven-tianal Ziegler-Natta polymerization processes. Conventional Ziegler-Natta polymerization systems have discreet catalyst composition differences which axe manifested as different catalyst reaction sites with each site having different reac-tion rates and selectivities. Metallocene catalyst systems are characterized as a single identifiable chemical type which has a singular rate in selectivity. Thus the conventional systems produce resins that reflect the differential character of the different catalyst sites while resins produced by metallocene systems reflect the single catalytic site. Howev-er, it should be noted that at least some previously available ethylene based linear polymers exhibited the physical and compositional properties achieved by the present metallocene catalyzed polyolefins. Although not produced by metallocene catalysis, such copolymers were produced by non-metallocene single cite catalysts yielding resins which achieve the homoge-neity of metallocene catalyzed resins. An example of such are 5/920915.1/SPECFLDR
the resins sold under the trade-mark Tafmer(TM) by Mitsui.
Both metallocene catalyzed ethylene alpha olefins and the Tafmer-type of resins are appropriate for use in the heat seal layer of the present invention.
Thus, the ethylene alpha-olefin of the present heat sealing layer is a homogeneous metallocene catalyzed resin or, at least, a single site catalyzed resin such as a Tafmer. The density is limited to below about 0.90 g/cc in order to aid in processability of the overall film structure and for improved sealing. The homogeneous ethylene alpha-olefin employed is preferably an ethylene butene copolymer or an ethylene propylene copolymer which will exhibit excellent compatibility with the propylene-based resin. The ethylene alpha-olef in will comprise from about 5o to about 50o by weight of the heat sealing layer, most preferably between 15% and 300.
The present film structure further includes at least one polyamide or nylon-containing layer. Such layer is present to impart elastic recovery properties to the overall structure. Specifically, in a cook-in application, as noted above, the food product is literally cooked in the film pack-age. Because the present film is biaxially oriented it shrinks during cooking to closely conform to the enclosed food product. After cooking, the product is typically 'chilled which, at least in the case of a meat product, often results in product shrinkage. It is desirable that the film have good elastic recovery in order to tightly conform to the meat dur-ing such shrinkage.
It is generally known that nylons provide such elastic recovery properties to thermoplastic films. For purposes of the present invention, various combinations of polyamides, copolyamides and amorphous nylons were investigated for deter-mining a preferred combination of processability, stiffness imparting properties and elastic recovery. A layer of nylon 6/12 was found to produce the optimum combination of proper-ties for the present invention.
Thus, the invention preferably comprises the foregoing (inner sealing and food contact layer)/(nylon layer)/(outer sealing layer) and in further embodiments the structure:
(inner sealing and food contact layer)/(nylon layer)/(barrier layer)/(outer sealing layer). Each of the layers may also be optionally banded to one anothEr by a tie layer as well.
The food contact layer can optionally be subjected to an energetic radiation treatment, including, but not limited to corona discharge, plasma, flame, ultraviolet, and high energy electron treatment. For instance, the food contact layer may be selectively irradiated with high energy electrons which advantageously may be accomplished during irradiation of the overall multilayer film structure for cook-in integrity, as further discussed below. Radiation dosages are referred to herein in terms of the radiation unit "RAD," with one million RADS or a megarad being designated as "MR." A suitable radia -tion dosage of high energy electrons is in the range of up to about 12 MR, more preferably about 2 to about 9 MR.
The adhesive or tie layer will also comprise any poly mer that will have excellent adhesion to the barrier layer and the core layer or the abuse layer or both the core layer and the abuse layer. The various polyethylenes includ~,ng the polyethylene copolymers as described herein and the ethylene vinyl acetate copolymers are useful as tie layers employed according to the present invention. Preferably, the tie layer comprises an anhydride modified alpha-olef in copolymer having rubber moieties such as is contained in the core layer, dis TM
cussed above. A preferred resin is T~:ror 1203 from Morton International. Also suitable is BynelTM4107 from du Pont.
However, any of the various adhesives well known in the art of film making may be employed, such as, for example, the Plexar (TM) adhesives supplied by Chemplex Co.
The term "ethylene vinyl acetate copolymer" (EVA) as used herein for a type of polyethylene refers to a copolymer formed from ethyl:vw.:.~ and v,~njl a~~~~tate monomers wherein the ethylene derived units in the copolymer are present in major amounts and the vinyl acetate derived units in the copolymer are present in minor amounts. EVA is known not only for hav-ing structural strength, as ethylene alpha-olefin polymer does, but also for providing excellent adhesion to an adjacent layer, which. decrease or even obviate the need for an "adhe-sive." EVA copolymers can be hydrolyzed to ethylene vinyl alcohol copolymers, (EVOH), which are employed principally as a barrier layer according to the present invention. For en-hanced orientability a modifier such as an ethylene/acrylic esterfmaleic anhydride terpolymer may be blended with the present EVOH barrier layer.
The term "oriented" is also used herein interchangeably with the term "heat shrinkable," these terms designating a material which has been stretched and set by cooling while substantially retaining its stretched dimensions. An oriented (i.e. heat shrinkable) material will tend to return to its original unstretched (unextended) dimensions when heated to an appropriate elevated temperature.
The cook-in film of the present invention is preferably oriented and is formed by extrusion processes especially art-known coextrusion methods. It is initially cooled by, for example, cascading water quenching, after which it is reheated to within its orientation temperature range and oriented by stretching. The stretching to orient may be accomplished in many ways such as, for example, by "blown bubble" techniques or "tenter framing." These processes are well known to those skilled in the art and refer to orientation procedures whereby the material is stretched in the cross or transverse direction (TD) and/or in the longitudinal or machine direction (MD).
After being stretched, the film is quickly quenched while substantially retaining its stretched dimensions to cool the film rapidly and thus set or lock in the oriented molecular configuration.
~'~_~""''~
If a film having little or no orientation is desired, e.g. nonoriented or non-heat shrinkable film, the film may be formed from a nonorientable material or, if formed from an orientable material may be "hot blown." In forming a hot blown film, the film is not cooled immediately after extrusion or coextrusion but rather is first stretched shortly after extrusion while the film is still at an elevated temperature abave the orientation temperature range of the material.
Thereafter, the film is cooled, by well known methods. Those having skill in the art are familiar with this process and the fact that the resulting film has substantially unoriented characteristics. Other methods for forming unoriented films are well known such as cast extrusion or cast coextrusion methods.
As noted, the film layers may be formed by coextrusion, with additional layers thereafter being extrusion coated there-on to form multilayer films. Two multilayer tubes may also be formed with one of the tubes thereafter being extrusion coated or laminated onto the other. The extrusion coating method of film formation is preferable to coextruding the entire film when it is desired to subject one or more layers of the film to a treatment which may be harmful to one or more of the other layers. This may be done where it is desired to irradi-ate one or more layers of a film with high energy electrons where the film contains a baxrier layer of one or more copolymers of vinylidene chloride (e.g., Saran(TM)), such as vinylidene chloride and vinyl chloride or vinylidene chloride and methyl acrylate as well as vinylidene chloride with ethyl acrylate or acryl.onitrile.
Films of this type would, for example, comprise those where the barrier layer is a Saran(TM) layer in addition to or instead . of an EVOH layer . Those skilled in the art generally recognise that irradiation with high energy electrons is gener-ally harmful to such Saran(TM) barrier layer compositions, as irradiation may degrade and discolor Saran(TM), making it turn brown. Thus, if full coextrusion followed by high energy 5/920915.1/SPECFLDR
_ c~ °,'.i ~ ' .
electron irradiation of the multilayer structure is carried out on a film having a barrier layer containing a Saran(TM) layer, the irradiation should be conducted at low levels and with care. Alternatively, this may be avoided by extruding a first layer or layers, subjecting the layer or layers to high energy electron irradiation and thereafter applying the Saran(TM) barrier layer and, for that matter, other layers (which may or may not have been irradiated) sequentially onto the outer surf ace of the extruded previously irradiated tube.
This sequence allows for high energy electron irradiation of the first layer or layers without subjecting the Saran(TM) barrier layer to harmful discoloration.
Thus, as used herein the term "extrusion" or the term °'extruding" is intended to include coextrusion, extrusion coating, or combinations thereof.
The above general outline for manufacturing of films is not meant to be all inclusive since such processes are well.
known as set forth in U. S. Patent Nos. 4,274,900; 4,229,241;
4,194,039; 4,188,443; 4,048,428; 3,821,182 and 3,022,543.
5/920915.1/SPECE'LDR
.. 1 8 ~~.~~'~?j?~
EXAMPLES
An attempt was made to produce the following film struc-tures. Tt was believed that the polyamide composition of the internal layers would provide good elastic recovery properties to a conventional inner sealant / tie / barrier / tie / outer sealant structure. However, these comparative film structures proved difficult and sometimes impossible to orient. Relative percent thicknesses for each layer are also given.
manr.~ T
Layers Tnner Tie Nylon Barrier Nylon Tie Out, Sealant Seal:
Comp.
Ex. 1 EPC-1 R-AD PA(90%) EVOH PA(90%) R-AD EPC
APA (10%) APA (10%) 7.35% 8.82% 7.35% 8.82% 29.41% 29.41% 8.8 Comp.
Ex. 2 EPC-1 P-AD ~ PA(90%) EVOH PA(90%) P-AD EPC
APA ( :10 APA ( 10 % ) % ) 29.41% 8.82% 7.35% 8.82% 7.35% 8.82% 29.4 Comp.
Ex. 3 EPC-1 R=AD PA(90%) EVOH PA(90%) R°AD EPC
APA (10%) APA (10%) 31.75% 9.52%- 3.97% 9.52% 3.97% 9.52% 31.7 Comp.
Ex. 4 EPC-1 R-AD PA(90%) EVOH-2 PA(90%) R-AD EPC
APA (10%) APA (10%) 31.75% 9.52% 3.97% 9.52% 3.97% 9.52% 31.7' 5/920915.1/SPECFLDR
~~.~~~'j?.~
comp.
Ex. 5 EPC-1 R-AD PA(85%) EVOH PA(85%) R-AD EPC
APA (15%) APA (15%) 31.75% 9.52% 3.97% 9.52% 3.97% 9.52% 31.7 Comp.
Ex. 6 EPC-1 R-AD PA(85%) EVOH(85%~A(85%)R-AD EPC
APA (15%) M (15%I~PA (15%) 31.75% 9.52% 3.97% 9.52% 3.97% 9.52% 31.7 Comp.
Ex. 7 EPC-1 R-AD PA(93%) EVOH-2 PA(93%) R-AD EPC
APA (7%) APA (7%) 31.75% 9.52% 3.97% 9.52% 3.97% 9.52% 31.7 Comp.
Ex. 8 EPC-1 P-AD PA(90%) EVOH-2 PA(90%) P-AD EPC
APA (10%) APA (10%) 30.30% 11.36% 3.79% 9.09% 3.79% 11.36% 30.3 comp.
Ex. 9 EPC-1 P-AD PA(90%) EVOH-2 PA(90%) P-AD EPC
APA ( 10% APA ( 10% ) ) 31.50% 11.81% 1.97% 9.45% 1.97% 11.81% 31.5 The following film structures, all containing a blend of a propylene-based copolymer and an ethylene alpha-olefin in the sealant were readily processed with little or no difficulty in orientation. It should be noted that the structures of the present Examples include polyamide-contain-ing layers of comparable thicknesses to those of Comparative Examples 1 - 9 above. In those earlier structures the polyamide was split into twn separate layers to sandwich the barrier layer and to provide a palindromic, film structure.
It was believed that a symmetrical structure would preclude curling. However, for the present Examples it was determined that the stiffness of the barrier layer balanced that of a single polyamide-containing layer to prevent curling.
5/920915.1/SPECFLDR
,. ,. , ?_ 0 f-, p cu~
'_ ;.i ;. ~ it TABLE II
Layers Inner Tie Nylon Barrier Tie Outer Sealant Sealant EX. 1 EPC-1(75%) R-AD CPA-1(80%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA (20%) M (15%) EAO-1(25%) 25.81% 16.13% 6.45% 9.68% 16.13%25.81%
Ex. 2 EPC-1(75%) R-AD CPA-1(80%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA (20%) M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.24%
Ex. 3 EPC-1(75%) R-AD CPA-1(90%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA (10%) M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.24%
Ex. 4 EPC-1(75%) R-AD CPA-1(90%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA (10%) M (15%) EAO-1(25%) 25.81% 16.13% 6.45% 9.68% 16.13%25.81%
Ex. 5 EPC1(75%) ,R-AD CPA-2(90%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA (10%) M (15%) EAO-1(25%) 25.81% 16.13% 6.45% 9.68% 16.13%25.81%
Ex. 6' EPC-1(75%) R-AD CPA-2(90%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA (10%) M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.24%
Ex. 7 EPC-1(75%) R-AD CPA-1(60%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) CPA-2 (40%) M (15%) EAO-1(25%) 25.81% 16.13% 6.45% 9.68% 16.13%25.81%
Ex. 8 EPC-1(75%) R-AD CPA-1(60%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) CPA-2 (40%) M (115%) EAO-1(25%) 24.24% 15.'15% 12.90% 9.09% 15.15%24.24%
Ex. 9 EPC-1(75%) R-AD PA-1(60%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) CPA-1 (40%) M (15%) EAO-1(25%) 25.81% 16.13% 6.45% 9.68% 16.13%25.81%
Ex. 10 EPC-1(75%) R-AD PA-1(60%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) CPA-1 (40%) M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.24%
5/920915.1/S~ECFLDR
,e ~ !' f ' C ~ f .,? y f ~ .)_ 4,~ ~.~ ,. J .J e~
Ex. 11 EPC-1(75%) R-AD PA-1(60%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) CPA-2 (40%) M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.24%
Ex. 12 EPC-1(75%) R-AD PA-1(60%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) CPA-2 (40%) M (15%) EAO-1(25%) 25.81% 16.13% 6.45% 9.68% 16.13%25.81%
Ex. 13 EPC-1(75%) R-AD PA-1(90%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA (10%) M (15%) EAO-1(25%) 25.81% 16.13% 6.45% 9.68% 16.13%25.81%
Ex. 14 EPC-1(75%) R-AD PA-1(90%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA (10%) M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.240 Ex. 15 EPC-1(75%) R-AD CPA-1 EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) M (15%) EAO-1(25%) 25.81% 16.13% 6.45% 9.68% 16.13%25.81%
Ex. 16 EPC-1(75%) R-AD CPA-1 EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) . M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.24%
Ex. 17 EPC-1(75%) R-AD CPA-3 EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) M (15%) EAO°1(25%) 25.00% 15.63% 9.37% 9.37% 15.63%25.00%
Ex. 18 EPC-1(75%)R-AD CPA-1(70%) EVOH(85%)R-ADEPC1(75%) EAO1(25%) CPA-4(30%) M (15%) EAO1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.24%
Ex. 19 EPC1(75%) R-AD CPA-4(50%) EVOH(85%)R-ADEPC-1(75%) EAO1(25%) CPA-1(500) M (15%) EAO-1(25%) 25.00% 15.63% 9.37% 9.37% 15.63%25.00%
Ex. 20 EPC-1(750)R-AD CPA-4(70%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) CPA-1(30%) M (15%) EAO-1(25%) 25.00% 15.63% 9.37% 9.37% 15.63%25.00%
Ex. 21 EPC-1(75%) R-AD PA-2(60%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) CPA-4(40%) M (15%) EAO-1(25%) 25.81% 16.13% 6.45% 9.68% 16.13%25.81%
5/920915.1/SPECFLDR
.. .
~~ 4/
Ex. 22 EPC-1(75%)R-AD PA-2(60%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) CPA-4(40%) M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.240 Ex. 23 EPC-1(75%)R-AD CPA-3(90%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA(10%) M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.24%
Ex. 24 EPC-1(75%)R-AD CPA-2(90%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA(10%) M (15%) EAO-1(25%) 25.81% 16.13% 6.45% 9.68% 16.13%25.81%
Ex. 25 EPC-1(75%) R-AD CPA-2(90%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA(10%) M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.24%
Ex. 26 EPB(75%) R-AD CPA-3(40%) EVOH(85%)R-AD EPB(75%) EAO-1(25%) GPA°1(60%) M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.24%
Ex. 27 EPC-2(75%) R-AD CPA-3(40%) EVOH(85%)R-ADEPC-2(75%) EAO-1 ( 25 % ) ~ CPA-1 ( 60 % ) M ( 15 % ) EAO-1 ( 25 % ) 24.24% 15.15% 22.90% 9.09% 15.15%24.24%
Ex. 28 EPC-2(75%) R-AD CPA--4 EVOH R-ADEPC-2(75%) EAO-1(25%) EAO-1(25%) 23.33% 16.66% 13.33% 6.66% 16.66%23.33%
Ex. 29 EPC-2(75%) R-AD CPA-4(70%) EVOH R-ADEPC-2(75%) EAO-1(25%) CPA-1(30%) EAO-1(25%) 23.33% 16.66% 13.33% 6.66% 16.66%23.33%
Ex: 30 EPB(75%) R-AD CPA-4(70%) EVOH R-AD EPB(75%) EAO-1(25%) CPA-1(30%) EAO-1(25%) 22.67% 17.00% 12.59% 6.17% 16.37%25.19%
Ex. 31 EPB(75%) R-AD CPA-4 EVOH R-AD EPB(75%) EAO-1(25%) EAO-1(25%) 23.12% 16.87% 12.50% 6.25% 16.25%25.00%
Ex. 32 EPB(75%) R-AD CPA-4 EVOH R-AD EPB(75%) EAO-1(25%) EAO-1(25%) 27.7$% 13.89% 11.11% 5.55% 13.89%27.78%
5/920915.1/SPECFI~DR
CA 02106889 2002-12-19 ' Ex. 33 EPC-2 ( 60 a ) R-AD CPA-1 ( '>0 a ) EVOH R-ADEPC-2 ( 60 0 ) EAO-1(40%) CPA-4(500) EAO-1(40x) 26 . 44°, 14 _ 67.° 7 . 6'p'~ 6 _ 75° __I5 . 31°
29 . 23 ~ _ Ex. 34 EPC-2 ( 60 0 ) R-AD PA-1 ( 90 0 ) EVOI3 R-ADEPC-2 ( 60 0 ) EAO-1 ( 40 0 ) CPA-1 ( 1_0 0 ) EAO-1 ( 40 ~ ) 26 . 44°-" ' 14 . 61. ~ -l . 6'-~° 6 _ 75° 1.5 .
31.° 29 . 23 0 In the Foregoing Exampl_~s ~~he following materials were employed:
EPC-1 F'inaM8473 sold by Fina, a prorylen~/ethyl~ne copolymer wit_.h 3 . I_ ~ ethylene .
EPC-Z Eltn.TMP KJ 409 sold by Solway, a pr~p~y'_~ne ethy l ene copolymer with 3 . 2~~; ethylene .
EPB w531Dr~old by Sumitomo, an ethylene propy7_ene butene copolyrner .
R-AD an ethylene alpha-olefin copolymer, Tymor('"M) 1203 sold by Morton INtl., rubber and malc~~_c anhydride grafted.
P-AD F3ynelME30Z sold by Dupont, an anhyctrl_de c; rafted polypropylFne.
PA or PA-1 8209 F'2d Sold by Al Lied, Nylon 6.
TM
PA-2 Vestamid 1,1940 Natural so~'d by Hul:~ America, Inc. contains Irc~anox 1098, an antioxidant, anti calcium stearate.
APA
Celar PA 3526 sold by DuPcnt, ' an amorphous nylon.
TM
CPA-1 Xh 3303 sold by E~mser, a Nylon 6 G/6 10.
TM
CPA-2 CF62BSE sold by Emser, a Nylon C / 0 9 .
'1'M
CPA-3 Ultra.mid C35 sold by HASF , a Nylon 666..
TM
CPA-4 Grilcn ~~'6S sold by Emser, a Nylon 6/12.
~4 EVOH Ethylene vinyl.~Mlcohol copolymer, Evai~ a~C-E105A sold by Eval of America.
EVOH-2 ECG--156B~ sold by Eval of America, an ethylene vinyl alco-hol copolymer.
M ~ an ethylene - acrylic ester -maleic anhydride copolymer modi-fier.
EAO-1 Tafmer A-4085 sold by Mitsui, a homogeneous ethylene butene copolymer, density = 0.885 g/cc.
EAO-1 Lower density ethylene alpha-olefin copolymer ATTANE(TM) 4203, sold 'ay Dow Chemical, ethylene polymerized with 1-octene having a den=pity of 0.905 g/cc EAO-2 ethylene 1-octene copolymer, Dowlex(TM) 2045 ~~old by Dow Chemical EBA EA 705-009TM so7_d by Quantum Chemical Company, e-~.hylene butyl acrvlate copolymer having a butyl acrylate content oz 50 by weight.
COLOR-1 whi~._o c~i-or concentrate, EPE
102.4-C~~:>old by Teknor Color, a 50 o TiOzI 50 o LDPE blend.
The foregoing description of preferred embodiments of the invention have been presented for purpose: of illustra-tion and description. It is not intended to be exhaustive or to limit the invention to the prec:i.se form disclosed, and modifications and variations are possible in light of the above teachings or may be acquired from practice of the inven-tion- The embodiments were chosen and described in order to explain the principles of the invention and its practical application to enable one skilled in the art to utilize the invention in various embodiments and with various modifica-tions as are suited to the particular use contemplated. I'or example, although backseamed casings are discussed herein, thermoplastic films employing the present seal layer and other strucr~ural layers are also within the scope cf the present invention. It is intended that the scope of the invention be defined by the claims appended hereto, an~vtheir equivalents.
U.K. Patent Application GB 2,139,948A discloses a multilayer, preferably coextruded fiber-layer heat sealable film having a surface layer of a heat sealable polymer such as linear low density polyethylene of LLDPE blended With other polymers such as EVA, an EVOH layer, and a layer of polypropylene. These layers can be bonded by polymeric adhe-sive tie layers.
U.K. Patent Application GB 2,221,649 discloses a compos-ite film with improved heat shrinkable properties comprising a core layer of a copolymer or propylene and one or more alpha-olefins having a Vicat softening point of 70-110°C and two outer layers of a crystalline polypropylene resin having a melting point of 135-150°C.
EPO Patent Application No. 435498-A is directed to a multilayer heat-shrinkable film which includes a heat sealing layer which is a copolymer of propylene and at least two other alpha-olefins .
Japanese Patent Application 3063133-A is directed to a heat shrinkable ~multilayer film which includes at least one layer which is a blend of an aliphatic polyamide and a non' crystalline polyamide.
Japanese Patent Application 3121842-A is directed to a packaging material which contains an inner layer which is a polyamide/polyethylene blend.
5/920915.1/SPECFLDR
,.... 9 German Patent Application 3943024-A is directed to a monolayer casing which is a blend of nylon 6 and a copolyamide.
Summary of the Invention The present invention provides a novel cook-in film which is readily biaxially oriented. Further, the present invention provides a novel cook-in film that has improved biaxial orientability as a tube by means of forming a bubble wherein bubble breakage is substantially minimized or eliminated. Further, the present invention provides a method for manufacturing such a novel cook-in film wherein the sealing layer comprises a blend of a propylene based copolymer and an ethylene alpha-olefin copolymer. Further, the present invention provides a method for manufacturing such a novel cook-in film wherein the outermost layer comprises a blend of a propylene based copolymer and an ethylene alpha-olefin copolymer. The present invention also provides a cook-in film with good elastic recovery for a tight package appearance. Still further, the present invention provides a cook-in film which can be formed into backseamed casings.
These as well as other aspects of the invention are achieved by providing a heat-shrinkable multilayer film which has a heat sealing outer layer of a blend of about 50%
to about 95% by weight of a propylene based copolymer and from about 5% to about 50% by weight of a homogeneous ethylene alpha-olefin copolymer having a density below about 0.90 g/cc. Such aspects are further achieved by providing such a film which also includes at least one layer containing a polyamide, a copolyamide, an amorphous copolyamide, or blends of such.
Additional aspects and advantages of the invention will be set forth in part in the description which follows and in part will be apparent to a person with ordinary skill in the art from the description, or may be learned by practice of the invention. The advantages of the invention may be realized and attained by means of the instrumentalities and combinations particularly pointed out in the appended claims.
Detailed Description ef the Invention The present invention is directed generally to multi-layer heat shrinkable films which have a heat sealing layer which is a blend of a propylene based copolymer and a homoge-neous ethylene alpha-olefin copolymer with a density below about 0.90 g/cc. Specifically, films with improved process-ability and heat seal characteristics in accordance with the present invention have the structure: (inner sealing and food contact layer)/(nylon layer)/outer sealing layer) or (inner sealing and food cor_tact layer)/(nylon layer)/(barrier lay-er)/(outer sealing layer). Here again, the inner sealing and food contact layer is a blend of a propylene based copolymer with an ethylene a~ pha-of efin copoiT .~er having a densi ty below about 0.90 g/cc. 'the propylene based copolymer is preferably an ethylene propylene copolymer which contains from about 94°-, to about 99-% by wei ght of propylene and from about 1% to about 6o by weight of ethylene.
Alternatively, the propylene based copolymer may be a copolymer of propylene with ethylene and butene. Such ethylene propylene butene copolymer should preferably contain from about 90% to about 99o by weight of propylene, from about 1% to about 6% by weight of ethylene, and from about to to abcut 10 o by weight oz butene. It SilOUld be noted that nor S's a (t ~
,~. ~~ t.u .~ LV
purposes of the present specification, the term "copolymer" is intended to broadly describe the products of polymerization of two or more comonomers.
Although the present heat sealing layer may comprise anywhere from 50o to about 95a by weight of such propylene based copolymer, a more preferred range is 70% to about 85%
with 750 of the heat sealing layer being the optimum amount of such copolymer. As noted above, the propylene based copolymer is blended with a homogeneous ethylene alpha-olefin copolymer which has a density below about 0.90 g/cc.
Ethylene alpha-olefins are, generally speaking, copolymers of ethylene with one or more comonamers selected from C3 to about C1o alpha olefins but especially compris-es ethylene copolymers with CQ to about C1o alpha olefins such as butane-1, pentane-1, hexane-1, octane-l, and the like, in which the polymer molecules comprise long chains with few side chains or. branches and sometimes are referred to as lin-ear polymers. These polymers are obtained by low pressure polymerization processes and the side branching which is present will be short compared to non-linear ethylenes.
Ethylene/alpha-olefin copolymers have a density in the range of fram about 0.860 g/cc to about 0.940 g/cc. The term linear low density polyethylene is generally understood to include that group of ethylene/alpha-olefin copolymers which fall into the density range of about 0.915 to about 0.940 g/cc. Some-times linear polyethylene in the density range from about 0.926 to about 0.940 is referred to a linear medium density polyethylene (LMDPE). Lower density ethylene alpha olefins may be referred to as very low density polyethylene (VLDPE, typically used to refer to the ethylene butane copolymers supplied by Union Carbide) and ultra-low density polyethylene (ULDPE,. typically used to refer to the ethylene octane copolymers supplied by Dow). It should be noted although specific density ranges is for VLDPE, ULDPE, LLDPE, and LMDPE
have been set forth herein, that no bright line can be drawn for density classification and such will vary by supplier.
5/920915.1/SPECFLDR
Heretofore, conventional ethylene alpha-olefins have been produced by Ziegler-Natta catalyst polymerization. The traditional Ziegler-Natta homogeneous system includes a metal halide activated by a metal alkyl cocatalyst. These are sys-tems in which there are various oxidation states of the metal, and a variety of ligand environments, depending upon where the site is located in the catalyst, all leading to a relatively broad molecular weight distribution and a generally heteroge-neous composition. Generally speaking, Ziegler-rT~tta cata-lysts incorporate comonomer poorly and produce some polymer chains with much comonomer and others with substantially less. Fox example, with conventional Ziegler-Natta catalysis, a linear ethylene alpha-olefin having an average of l00 comonomer may have a range of Oo to 40% comonomer in any given individual chain.
Recently a new type of ethylene based linear polymers have been introduced. These new resins are produced by metallacene catalyst polymerization and are characterized by narrow or more homogenous compositional properties, such as molecular weight distribution, than resins produced by conven-tianal Ziegler-Natta polymerization processes. Conventional Ziegler-Natta polymerization systems have discreet catalyst composition differences which axe manifested as different catalyst reaction sites with each site having different reac-tion rates and selectivities. Metallocene catalyst systems are characterized as a single identifiable chemical type which has a singular rate in selectivity. Thus the conventional systems produce resins that reflect the differential character of the different catalyst sites while resins produced by metallocene systems reflect the single catalytic site. Howev-er, it should be noted that at least some previously available ethylene based linear polymers exhibited the physical and compositional properties achieved by the present metallocene catalyzed polyolefins. Although not produced by metallocene catalysis, such copolymers were produced by non-metallocene single cite catalysts yielding resins which achieve the homoge-neity of metallocene catalyzed resins. An example of such are 5/920915.1/SPECFLDR
the resins sold under the trade-mark Tafmer(TM) by Mitsui.
Both metallocene catalyzed ethylene alpha olefins and the Tafmer-type of resins are appropriate for use in the heat seal layer of the present invention.
Thus, the ethylene alpha-olefin of the present heat sealing layer is a homogeneous metallocene catalyzed resin or, at least, a single site catalyzed resin such as a Tafmer. The density is limited to below about 0.90 g/cc in order to aid in processability of the overall film structure and for improved sealing. The homogeneous ethylene alpha-olefin employed is preferably an ethylene butene copolymer or an ethylene propylene copolymer which will exhibit excellent compatibility with the propylene-based resin. The ethylene alpha-olef in will comprise from about 5o to about 50o by weight of the heat sealing layer, most preferably between 15% and 300.
The present film structure further includes at least one polyamide or nylon-containing layer. Such layer is present to impart elastic recovery properties to the overall structure. Specifically, in a cook-in application, as noted above, the food product is literally cooked in the film pack-age. Because the present film is biaxially oriented it shrinks during cooking to closely conform to the enclosed food product. After cooking, the product is typically 'chilled which, at least in the case of a meat product, often results in product shrinkage. It is desirable that the film have good elastic recovery in order to tightly conform to the meat dur-ing such shrinkage.
It is generally known that nylons provide such elastic recovery properties to thermoplastic films. For purposes of the present invention, various combinations of polyamides, copolyamides and amorphous nylons were investigated for deter-mining a preferred combination of processability, stiffness imparting properties and elastic recovery. A layer of nylon 6/12 was found to produce the optimum combination of proper-ties for the present invention.
Thus, the invention preferably comprises the foregoing (inner sealing and food contact layer)/(nylon layer)/(outer sealing layer) and in further embodiments the structure:
(inner sealing and food contact layer)/(nylon layer)/(barrier layer)/(outer sealing layer). Each of the layers may also be optionally banded to one anothEr by a tie layer as well.
The food contact layer can optionally be subjected to an energetic radiation treatment, including, but not limited to corona discharge, plasma, flame, ultraviolet, and high energy electron treatment. For instance, the food contact layer may be selectively irradiated with high energy electrons which advantageously may be accomplished during irradiation of the overall multilayer film structure for cook-in integrity, as further discussed below. Radiation dosages are referred to herein in terms of the radiation unit "RAD," with one million RADS or a megarad being designated as "MR." A suitable radia -tion dosage of high energy electrons is in the range of up to about 12 MR, more preferably about 2 to about 9 MR.
The adhesive or tie layer will also comprise any poly mer that will have excellent adhesion to the barrier layer and the core layer or the abuse layer or both the core layer and the abuse layer. The various polyethylenes includ~,ng the polyethylene copolymers as described herein and the ethylene vinyl acetate copolymers are useful as tie layers employed according to the present invention. Preferably, the tie layer comprises an anhydride modified alpha-olef in copolymer having rubber moieties such as is contained in the core layer, dis TM
cussed above. A preferred resin is T~:ror 1203 from Morton International. Also suitable is BynelTM4107 from du Pont.
However, any of the various adhesives well known in the art of film making may be employed, such as, for example, the Plexar (TM) adhesives supplied by Chemplex Co.
The term "ethylene vinyl acetate copolymer" (EVA) as used herein for a type of polyethylene refers to a copolymer formed from ethyl:vw.:.~ and v,~njl a~~~~tate monomers wherein the ethylene derived units in the copolymer are present in major amounts and the vinyl acetate derived units in the copolymer are present in minor amounts. EVA is known not only for hav-ing structural strength, as ethylene alpha-olefin polymer does, but also for providing excellent adhesion to an adjacent layer, which. decrease or even obviate the need for an "adhe-sive." EVA copolymers can be hydrolyzed to ethylene vinyl alcohol copolymers, (EVOH), which are employed principally as a barrier layer according to the present invention. For en-hanced orientability a modifier such as an ethylene/acrylic esterfmaleic anhydride terpolymer may be blended with the present EVOH barrier layer.
The term "oriented" is also used herein interchangeably with the term "heat shrinkable," these terms designating a material which has been stretched and set by cooling while substantially retaining its stretched dimensions. An oriented (i.e. heat shrinkable) material will tend to return to its original unstretched (unextended) dimensions when heated to an appropriate elevated temperature.
The cook-in film of the present invention is preferably oriented and is formed by extrusion processes especially art-known coextrusion methods. It is initially cooled by, for example, cascading water quenching, after which it is reheated to within its orientation temperature range and oriented by stretching. The stretching to orient may be accomplished in many ways such as, for example, by "blown bubble" techniques or "tenter framing." These processes are well known to those skilled in the art and refer to orientation procedures whereby the material is stretched in the cross or transverse direction (TD) and/or in the longitudinal or machine direction (MD).
After being stretched, the film is quickly quenched while substantially retaining its stretched dimensions to cool the film rapidly and thus set or lock in the oriented molecular configuration.
~'~_~""''~
If a film having little or no orientation is desired, e.g. nonoriented or non-heat shrinkable film, the film may be formed from a nonorientable material or, if formed from an orientable material may be "hot blown." In forming a hot blown film, the film is not cooled immediately after extrusion or coextrusion but rather is first stretched shortly after extrusion while the film is still at an elevated temperature abave the orientation temperature range of the material.
Thereafter, the film is cooled, by well known methods. Those having skill in the art are familiar with this process and the fact that the resulting film has substantially unoriented characteristics. Other methods for forming unoriented films are well known such as cast extrusion or cast coextrusion methods.
As noted, the film layers may be formed by coextrusion, with additional layers thereafter being extrusion coated there-on to form multilayer films. Two multilayer tubes may also be formed with one of the tubes thereafter being extrusion coated or laminated onto the other. The extrusion coating method of film formation is preferable to coextruding the entire film when it is desired to subject one or more layers of the film to a treatment which may be harmful to one or more of the other layers. This may be done where it is desired to irradi-ate one or more layers of a film with high energy electrons where the film contains a baxrier layer of one or more copolymers of vinylidene chloride (e.g., Saran(TM)), such as vinylidene chloride and vinyl chloride or vinylidene chloride and methyl acrylate as well as vinylidene chloride with ethyl acrylate or acryl.onitrile.
Films of this type would, for example, comprise those where the barrier layer is a Saran(TM) layer in addition to or instead . of an EVOH layer . Those skilled in the art generally recognise that irradiation with high energy electrons is gener-ally harmful to such Saran(TM) barrier layer compositions, as irradiation may degrade and discolor Saran(TM), making it turn brown. Thus, if full coextrusion followed by high energy 5/920915.1/SPECFLDR
_ c~ °,'.i ~ ' .
electron irradiation of the multilayer structure is carried out on a film having a barrier layer containing a Saran(TM) layer, the irradiation should be conducted at low levels and with care. Alternatively, this may be avoided by extruding a first layer or layers, subjecting the layer or layers to high energy electron irradiation and thereafter applying the Saran(TM) barrier layer and, for that matter, other layers (which may or may not have been irradiated) sequentially onto the outer surf ace of the extruded previously irradiated tube.
This sequence allows for high energy electron irradiation of the first layer or layers without subjecting the Saran(TM) barrier layer to harmful discoloration.
Thus, as used herein the term "extrusion" or the term °'extruding" is intended to include coextrusion, extrusion coating, or combinations thereof.
The above general outline for manufacturing of films is not meant to be all inclusive since such processes are well.
known as set forth in U. S. Patent Nos. 4,274,900; 4,229,241;
4,194,039; 4,188,443; 4,048,428; 3,821,182 and 3,022,543.
5/920915.1/SPECE'LDR
.. 1 8 ~~.~~'~?j?~
EXAMPLES
An attempt was made to produce the following film struc-tures. Tt was believed that the polyamide composition of the internal layers would provide good elastic recovery properties to a conventional inner sealant / tie / barrier / tie / outer sealant structure. However, these comparative film structures proved difficult and sometimes impossible to orient. Relative percent thicknesses for each layer are also given.
manr.~ T
Layers Tnner Tie Nylon Barrier Nylon Tie Out, Sealant Seal:
Comp.
Ex. 1 EPC-1 R-AD PA(90%) EVOH PA(90%) R-AD EPC
APA (10%) APA (10%) 7.35% 8.82% 7.35% 8.82% 29.41% 29.41% 8.8 Comp.
Ex. 2 EPC-1 P-AD ~ PA(90%) EVOH PA(90%) P-AD EPC
APA ( :10 APA ( 10 % ) % ) 29.41% 8.82% 7.35% 8.82% 7.35% 8.82% 29.4 Comp.
Ex. 3 EPC-1 R=AD PA(90%) EVOH PA(90%) R°AD EPC
APA (10%) APA (10%) 31.75% 9.52%- 3.97% 9.52% 3.97% 9.52% 31.7 Comp.
Ex. 4 EPC-1 R-AD PA(90%) EVOH-2 PA(90%) R-AD EPC
APA (10%) APA (10%) 31.75% 9.52% 3.97% 9.52% 3.97% 9.52% 31.7' 5/920915.1/SPECFLDR
~~.~~~'j?.~
comp.
Ex. 5 EPC-1 R-AD PA(85%) EVOH PA(85%) R-AD EPC
APA (15%) APA (15%) 31.75% 9.52% 3.97% 9.52% 3.97% 9.52% 31.7 Comp.
Ex. 6 EPC-1 R-AD PA(85%) EVOH(85%~A(85%)R-AD EPC
APA (15%) M (15%I~PA (15%) 31.75% 9.52% 3.97% 9.52% 3.97% 9.52% 31.7 Comp.
Ex. 7 EPC-1 R-AD PA(93%) EVOH-2 PA(93%) R-AD EPC
APA (7%) APA (7%) 31.75% 9.52% 3.97% 9.52% 3.97% 9.52% 31.7 Comp.
Ex. 8 EPC-1 P-AD PA(90%) EVOH-2 PA(90%) P-AD EPC
APA (10%) APA (10%) 30.30% 11.36% 3.79% 9.09% 3.79% 11.36% 30.3 comp.
Ex. 9 EPC-1 P-AD PA(90%) EVOH-2 PA(90%) P-AD EPC
APA ( 10% APA ( 10% ) ) 31.50% 11.81% 1.97% 9.45% 1.97% 11.81% 31.5 The following film structures, all containing a blend of a propylene-based copolymer and an ethylene alpha-olefin in the sealant were readily processed with little or no difficulty in orientation. It should be noted that the structures of the present Examples include polyamide-contain-ing layers of comparable thicknesses to those of Comparative Examples 1 - 9 above. In those earlier structures the polyamide was split into twn separate layers to sandwich the barrier layer and to provide a palindromic, film structure.
It was believed that a symmetrical structure would preclude curling. However, for the present Examples it was determined that the stiffness of the barrier layer balanced that of a single polyamide-containing layer to prevent curling.
5/920915.1/SPECFLDR
,. ,. , ?_ 0 f-, p cu~
'_ ;.i ;. ~ it TABLE II
Layers Inner Tie Nylon Barrier Tie Outer Sealant Sealant EX. 1 EPC-1(75%) R-AD CPA-1(80%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA (20%) M (15%) EAO-1(25%) 25.81% 16.13% 6.45% 9.68% 16.13%25.81%
Ex. 2 EPC-1(75%) R-AD CPA-1(80%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA (20%) M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.24%
Ex. 3 EPC-1(75%) R-AD CPA-1(90%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA (10%) M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.24%
Ex. 4 EPC-1(75%) R-AD CPA-1(90%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA (10%) M (15%) EAO-1(25%) 25.81% 16.13% 6.45% 9.68% 16.13%25.81%
Ex. 5 EPC1(75%) ,R-AD CPA-2(90%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA (10%) M (15%) EAO-1(25%) 25.81% 16.13% 6.45% 9.68% 16.13%25.81%
Ex. 6' EPC-1(75%) R-AD CPA-2(90%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA (10%) M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.24%
Ex. 7 EPC-1(75%) R-AD CPA-1(60%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) CPA-2 (40%) M (15%) EAO-1(25%) 25.81% 16.13% 6.45% 9.68% 16.13%25.81%
Ex. 8 EPC-1(75%) R-AD CPA-1(60%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) CPA-2 (40%) M (115%) EAO-1(25%) 24.24% 15.'15% 12.90% 9.09% 15.15%24.24%
Ex. 9 EPC-1(75%) R-AD PA-1(60%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) CPA-1 (40%) M (15%) EAO-1(25%) 25.81% 16.13% 6.45% 9.68% 16.13%25.81%
Ex. 10 EPC-1(75%) R-AD PA-1(60%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) CPA-1 (40%) M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.24%
5/920915.1/S~ECFLDR
,e ~ !' f ' C ~ f .,? y f ~ .)_ 4,~ ~.~ ,. J .J e~
Ex. 11 EPC-1(75%) R-AD PA-1(60%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) CPA-2 (40%) M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.24%
Ex. 12 EPC-1(75%) R-AD PA-1(60%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) CPA-2 (40%) M (15%) EAO-1(25%) 25.81% 16.13% 6.45% 9.68% 16.13%25.81%
Ex. 13 EPC-1(75%) R-AD PA-1(90%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA (10%) M (15%) EAO-1(25%) 25.81% 16.13% 6.45% 9.68% 16.13%25.81%
Ex. 14 EPC-1(75%) R-AD PA-1(90%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA (10%) M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.240 Ex. 15 EPC-1(75%) R-AD CPA-1 EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) M (15%) EAO-1(25%) 25.81% 16.13% 6.45% 9.68% 16.13%25.81%
Ex. 16 EPC-1(75%) R-AD CPA-1 EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) . M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.24%
Ex. 17 EPC-1(75%) R-AD CPA-3 EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) M (15%) EAO°1(25%) 25.00% 15.63% 9.37% 9.37% 15.63%25.00%
Ex. 18 EPC-1(75%)R-AD CPA-1(70%) EVOH(85%)R-ADEPC1(75%) EAO1(25%) CPA-4(30%) M (15%) EAO1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.24%
Ex. 19 EPC1(75%) R-AD CPA-4(50%) EVOH(85%)R-ADEPC-1(75%) EAO1(25%) CPA-1(500) M (15%) EAO-1(25%) 25.00% 15.63% 9.37% 9.37% 15.63%25.00%
Ex. 20 EPC-1(750)R-AD CPA-4(70%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) CPA-1(30%) M (15%) EAO-1(25%) 25.00% 15.63% 9.37% 9.37% 15.63%25.00%
Ex. 21 EPC-1(75%) R-AD PA-2(60%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) CPA-4(40%) M (15%) EAO-1(25%) 25.81% 16.13% 6.45% 9.68% 16.13%25.81%
5/920915.1/SPECFLDR
.. .
~~ 4/
Ex. 22 EPC-1(75%)R-AD PA-2(60%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) CPA-4(40%) M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.240 Ex. 23 EPC-1(75%)R-AD CPA-3(90%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA(10%) M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.24%
Ex. 24 EPC-1(75%)R-AD CPA-2(90%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA(10%) M (15%) EAO-1(25%) 25.81% 16.13% 6.45% 9.68% 16.13%25.81%
Ex. 25 EPC-1(75%) R-AD CPA-2(90%) EVOH(85%)R-ADEPC-1(75%) EAO-1(25%) APA(10%) M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.24%
Ex. 26 EPB(75%) R-AD CPA-3(40%) EVOH(85%)R-AD EPB(75%) EAO-1(25%) GPA°1(60%) M (15%) EAO-1(25%) 24.24% 15.15% 12.90% 9.09% 15.15%24.24%
Ex. 27 EPC-2(75%) R-AD CPA-3(40%) EVOH(85%)R-ADEPC-2(75%) EAO-1 ( 25 % ) ~ CPA-1 ( 60 % ) M ( 15 % ) EAO-1 ( 25 % ) 24.24% 15.15% 22.90% 9.09% 15.15%24.24%
Ex. 28 EPC-2(75%) R-AD CPA--4 EVOH R-ADEPC-2(75%) EAO-1(25%) EAO-1(25%) 23.33% 16.66% 13.33% 6.66% 16.66%23.33%
Ex. 29 EPC-2(75%) R-AD CPA-4(70%) EVOH R-ADEPC-2(75%) EAO-1(25%) CPA-1(30%) EAO-1(25%) 23.33% 16.66% 13.33% 6.66% 16.66%23.33%
Ex: 30 EPB(75%) R-AD CPA-4(70%) EVOH R-AD EPB(75%) EAO-1(25%) CPA-1(30%) EAO-1(25%) 22.67% 17.00% 12.59% 6.17% 16.37%25.19%
Ex. 31 EPB(75%) R-AD CPA-4 EVOH R-AD EPB(75%) EAO-1(25%) EAO-1(25%) 23.12% 16.87% 12.50% 6.25% 16.25%25.00%
Ex. 32 EPB(75%) R-AD CPA-4 EVOH R-AD EPB(75%) EAO-1(25%) EAO-1(25%) 27.7$% 13.89% 11.11% 5.55% 13.89%27.78%
5/920915.1/SPECFI~DR
CA 02106889 2002-12-19 ' Ex. 33 EPC-2 ( 60 a ) R-AD CPA-1 ( '>0 a ) EVOH R-ADEPC-2 ( 60 0 ) EAO-1(40%) CPA-4(500) EAO-1(40x) 26 . 44°, 14 _ 67.° 7 . 6'p'~ 6 _ 75° __I5 . 31°
29 . 23 ~ _ Ex. 34 EPC-2 ( 60 0 ) R-AD PA-1 ( 90 0 ) EVOI3 R-ADEPC-2 ( 60 0 ) EAO-1 ( 40 0 ) CPA-1 ( 1_0 0 ) EAO-1 ( 40 ~ ) 26 . 44°-" ' 14 . 61. ~ -l . 6'-~° 6 _ 75° 1.5 .
31.° 29 . 23 0 In the Foregoing Exampl_~s ~~he following materials were employed:
EPC-1 F'inaM8473 sold by Fina, a prorylen~/ethyl~ne copolymer wit_.h 3 . I_ ~ ethylene .
EPC-Z Eltn.TMP KJ 409 sold by Solway, a pr~p~y'_~ne ethy l ene copolymer with 3 . 2~~; ethylene .
EPB w531Dr~old by Sumitomo, an ethylene propy7_ene butene copolyrner .
R-AD an ethylene alpha-olefin copolymer, Tymor('"M) 1203 sold by Morton INtl., rubber and malc~~_c anhydride grafted.
P-AD F3ynelME30Z sold by Dupont, an anhyctrl_de c; rafted polypropylFne.
PA or PA-1 8209 F'2d Sold by Al Lied, Nylon 6.
TM
PA-2 Vestamid 1,1940 Natural so~'d by Hul:~ America, Inc. contains Irc~anox 1098, an antioxidant, anti calcium stearate.
APA
Celar PA 3526 sold by DuPcnt, ' an amorphous nylon.
TM
CPA-1 Xh 3303 sold by E~mser, a Nylon 6 G/6 10.
TM
CPA-2 CF62BSE sold by Emser, a Nylon C / 0 9 .
'1'M
CPA-3 Ultra.mid C35 sold by HASF , a Nylon 666..
TM
CPA-4 Grilcn ~~'6S sold by Emser, a Nylon 6/12.
~4 EVOH Ethylene vinyl.~Mlcohol copolymer, Evai~ a~C-E105A sold by Eval of America.
EVOH-2 ECG--156B~ sold by Eval of America, an ethylene vinyl alco-hol copolymer.
M ~ an ethylene - acrylic ester -maleic anhydride copolymer modi-fier.
EAO-1 Tafmer A-4085 sold by Mitsui, a homogeneous ethylene butene copolymer, density = 0.885 g/cc.
EAO-1 Lower density ethylene alpha-olefin copolymer ATTANE(TM) 4203, sold 'ay Dow Chemical, ethylene polymerized with 1-octene having a den=pity of 0.905 g/cc EAO-2 ethylene 1-octene copolymer, Dowlex(TM) 2045 ~~old by Dow Chemical EBA EA 705-009TM so7_d by Quantum Chemical Company, e-~.hylene butyl acrvlate copolymer having a butyl acrylate content oz 50 by weight.
COLOR-1 whi~._o c~i-or concentrate, EPE
102.4-C~~:>old by Teknor Color, a 50 o TiOzI 50 o LDPE blend.
The foregoing description of preferred embodiments of the invention have been presented for purpose: of illustra-tion and description. It is not intended to be exhaustive or to limit the invention to the prec:i.se form disclosed, and modifications and variations are possible in light of the above teachings or may be acquired from practice of the inven-tion- The embodiments were chosen and described in order to explain the principles of the invention and its practical application to enable one skilled in the art to utilize the invention in various embodiments and with various modifica-tions as are suited to the particular use contemplated. I'or example, although backseamed casings are discussed herein, thermoplastic films employing the present seal layer and other strucr~ural layers are also within the scope cf the present invention. It is intended that the scope of the invention be defined by the claims appended hereto, an~vtheir equivalents.
Claims (14)
1. A heat-shrinkable multilayer film comprising an outer heat sealing layer comprising a blend of from about 50% to about 95% by weight of a propylene-based copolymer and from about 5% to about 50% by weight of a homogeneous ethylene alpha-olefin copolymer having a density below about 0.90 g/cc.
2. A heat-shrinkable multilayer film as set forth in claim 1, wherein said heat sealing layer comprises a blend of from about 70% to about 85% by weight of said propylene-based copolymer and from about 15% to about 30% by weight of said homogeneous ethylene alpha-olefin copolymer.
3. A heat-shrinkable multilayer film as set forth in claim 1 or 2, wherein said propylene-based copolymer is a copolymer of propylene and one or more other alpha-olefins.
4. A heat-shrinkable multilayer film as set forth in claim 3, wherein said propylene-based copolymer is a copolymer of propylene and ethylene.
5. A heat-shrinkable multilayer film as set forth in claim 3, wherein said propylene-based copolymer is a copolymer of propylene, ethylene and butene.
6. A heat-shrinkable multilayer film as set forth in claim 4, wherein said propylene-based copolymer comprise from about 94% to about 99% by weight of propylene and from about 1% to about 6% by weight of ethylene.
7. A heat-shrinkable multilayer film as set forth in claim 5, wherein said propylene-based copolymer comprises from about 90% to about 99% by weight of propylene, from about 1% to about 6% by weight of ethylene and from about 1%
to about 10% by weight of butene.
to about 10% by weight of butene.
8. A heat-shrinkable multilayer film as set forth in any one of claims 1 to 7, further comprising at least one internal layer comprising a polyamide, a copolyamide or blends thereof.
9. A heat-shrinkable multilayer film as set forth in claim 8, wherein said polyamide is amorphous.
10. A heat-shrinkable multilayer film as set forth in any one of claims 1 to 9, further comprising a barrier layer.
11. A heat-shrinkable multilayer film as set forth in any one of claims 1 to 10, further comprising one or more adhesive tie layers.
12. A heat-shrinkable film as set forth in any one of claims 1 to 11, wherein said film is corona treated.
13. A heat-shrinkable multilayer film comprising an inner heat sealing layer as defined in any one of claims 1 to 7, and an outer heat sealing layer as defined in any one of claims 1 to 7.
14. A heat-shrinkable multilayer film as set forth in claim 13, further comprising at least one internal layer comprising a polymeric material selected from the group consisting of polyamides, copolyamides, amorphous polyamides and blends thereof.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US95124592A | 1992-09-25 | 1992-09-25 | |
| US951,245 | 1992-09-25 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2106889A1 CA2106889A1 (en) | 1994-03-26 |
| CA2106889C true CA2106889C (en) | 2003-08-19 |
Family
ID=25491476
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA 2106889 Expired - Fee Related CA2106889C (en) | 1992-09-25 | 1993-09-24 | Multi-ply backseamable film |
Country Status (4)
| Country | Link |
|---|---|
| JP (1) | JPH06210810A (en) |
| AU (1) | AU672222B2 (en) |
| CA (1) | CA2106889C (en) |
| NZ (1) | NZ248765A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006102148A2 (en) * | 2005-03-17 | 2006-09-28 | Cryovac, Inc. | Retortable packaging film with outer layers containing blend of propylene-based polymer and homogeneous polymer |
| WO2006102156A2 (en) * | 2005-03-17 | 2006-09-28 | Cryovac, Inc. | Retortable packaging film with having seal/product-contact layer containing blend of polyethylenes and skin layer containing propylene-based polymer blended with polyethylene |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6221410B1 (en) | 1992-09-25 | 2001-04-24 | Cryovac, Inc. | Backseamed casing and packaged product incorporating same |
| EP0756931B2 (en) | 1995-07-31 | 2011-06-22 | Kureha Corporation | Multilayer film |
| US6086967A (en) * | 1996-11-06 | 2000-07-11 | The Dow Chemical Company | Modified atmosphere films useful in the packaging of perishable food |
| US6500505B2 (en) * | 1998-05-15 | 2002-12-31 | Cryovac, Inc. | Thermoplastic film with good interply adhesion |
| US20100247935A1 (en) * | 2009-03-24 | 2010-09-30 | Baxter International Inc. | Non-pvc films having barrier layer |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4608302A (en) * | 1985-01-30 | 1986-08-26 | W. R. Grace & Co., Cryovac Div. | Oriented films from propylene copolymers and unplasticized saran |
| GB2221649B (en) * | 1988-08-11 | 1992-04-29 | Okura Industrial Co Ltd | Heat shrinkable composite film and packaging method using same |
-
1993
- 1993-09-24 AU AU47567/93A patent/AU672222B2/en not_active Ceased
- 1993-09-24 JP JP25901393A patent/JPH06210810A/en not_active Withdrawn
- 1993-09-24 CA CA 2106889 patent/CA2106889C/en not_active Expired - Fee Related
- 1993-09-24 NZ NZ24876593A patent/NZ248765A/en unknown
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006102148A2 (en) * | 2005-03-17 | 2006-09-28 | Cryovac, Inc. | Retortable packaging film with outer layers containing blend of propylene-based polymer and homogeneous polymer |
| WO2006102156A2 (en) * | 2005-03-17 | 2006-09-28 | Cryovac, Inc. | Retortable packaging film with having seal/product-contact layer containing blend of polyethylenes and skin layer containing propylene-based polymer blended with polyethylene |
| WO2006102148A3 (en) * | 2005-03-17 | 2007-01-18 | Cryovac Inc | Retortable packaging film with outer layers containing blend of propylene-based polymer and homogeneous polymer |
| WO2006102156A3 (en) * | 2005-03-17 | 2007-01-25 | Cryovac Inc | Retortable packaging film with having seal/product-contact layer containing blend of polyethylenes and skin layer containing propylene-based polymer blended with polyethylene |
Also Published As
| Publication number | Publication date |
|---|---|
| AU4756793A (en) | 1994-03-31 |
| JPH06210810A (en) | 1994-08-02 |
| CA2106889A1 (en) | 1994-03-26 |
| NZ248765A (en) | 1996-08-27 |
| AU672222B2 (en) | 1996-09-26 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EEER | Examination request | ||
| MKLA | Lapsed |