CA1170159A - Laminate film - Google Patents
Laminate filmInfo
- Publication number
- CA1170159A CA1170159A CA000388676A CA388676A CA1170159A CA 1170159 A CA1170159 A CA 1170159A CA 000388676 A CA000388676 A CA 000388676A CA 388676 A CA388676 A CA 388676A CA 1170159 A CA1170159 A CA 1170159A
- Authority
- CA
- Canada
- Prior art keywords
- copolymer
- laminate film
- ethylene
- weight
- layer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000005001 laminate film Substances 0.000 title claims abstract description 44
- 239000010410 layer Substances 0.000 claims abstract description 56
- 229920001577 copolymer Polymers 0.000 claims abstract description 52
- 238000002844 melting Methods 0.000 claims abstract description 25
- 230000008018 melting Effects 0.000 claims abstract description 25
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims abstract description 23
- 239000005977 Ethylene Substances 0.000 claims abstract description 23
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000000203 mixture Substances 0.000 claims abstract description 13
- 239000004711 α-olefin Substances 0.000 claims abstract description 13
- 239000012790 adhesive layer Substances 0.000 claims abstract description 7
- 229920000642 polymer Polymers 0.000 claims description 17
- OEPOKWHJYJXUGD-UHFFFAOYSA-N 2-(3-phenylmethoxyphenyl)-1,3-thiazole-4-carbaldehyde Chemical compound O=CC1=CSC(C=2C=C(OCC=3C=CC=CC=3)C=CC=2)=N1 OEPOKWHJYJXUGD-UHFFFAOYSA-N 0.000 claims description 11
- 239000004698 Polyethylene Substances 0.000 claims description 3
- 239000000178 monomer Substances 0.000 claims description 3
- -1 polyethylene Polymers 0.000 claims description 3
- WSSSPWUEQFSQQG-UHFFFAOYSA-N 4-methyl-1-pentene Chemical compound CC(C)CC=C WSSSPWUEQFSQQG-UHFFFAOYSA-N 0.000 claims description 2
- 150000001732 carboxylic acid derivatives Chemical class 0.000 claims description 2
- 229920000573 polyethylene Polymers 0.000 claims description 2
- 238000007789 sealing Methods 0.000 abstract description 9
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 abstract 1
- 229920001328 Polyvinylidene chloride Polymers 0.000 description 15
- 239000005033 polyvinylidene chloride Substances 0.000 description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 230000000052 comparative effect Effects 0.000 description 7
- 229920000092 linear low density polyethylene Polymers 0.000 description 7
- 239000004707 linear low-density polyethylene Substances 0.000 description 7
- 238000012856 packing Methods 0.000 description 6
- 239000000463 material Substances 0.000 description 5
- 239000011347 resin Substances 0.000 description 5
- 229920005989 resin Polymers 0.000 description 5
- 230000001954 sterilising effect Effects 0.000 description 5
- 229920006257 Heat-shrinkable film Polymers 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000004659 sterilization and disinfection Methods 0.000 description 4
- 239000000654 additive Substances 0.000 description 3
- 238000010276 construction Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 230000007547 defect Effects 0.000 description 3
- 235000015255 meat loaf Nutrition 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 238000004806 packaging method and process Methods 0.000 description 3
- 230000002285 radioactive effect Effects 0.000 description 3
- 235000012424 soybean oil Nutrition 0.000 description 3
- 239000003549 soybean oil Substances 0.000 description 3
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 150000001336 alkenes Chemical class 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 235000013372 meat Nutrition 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 235000019198 oils Nutrition 0.000 description 2
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 2
- 239000005022 packaging material Substances 0.000 description 2
- 235000015277 pork Nutrition 0.000 description 2
- 239000003381 stabilizer Substances 0.000 description 2
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 101100536354 Drosophila melanogaster tant gene Proteins 0.000 description 1
- 241000588724 Escherichia coli Species 0.000 description 1
- 240000002129 Malva sylvestris Species 0.000 description 1
- 235000006770 Malva sylvestris Nutrition 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 125000005250 alkyl acrylate group Chemical group 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- 229920001400 block copolymer Polymers 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 235000013351 cheese Nutrition 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000003925 fat Substances 0.000 description 1
- 229920000554 ionomer Polymers 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 229920001684 low density polyethylene Polymers 0.000 description 1
- 239000004702 low-density polyethylene Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000000289 melt material Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 230000000171 quenching effect Effects 0.000 description 1
- 235000020995 raw meat Nutrition 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/06—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
- B32B27/08—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/30—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/30—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers
- B32B27/304—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers comprising vinyl halide (co)polymers, e.g. PVC, PVDC, PVF, PVDF
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/32—Layered products comprising a layer of synthetic resin comprising polyolefins
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/32—Layered products comprising a layer of synthetic resin comprising polyolefins
- B32B27/322—Layered products comprising a layer of synthetic resin comprising polyolefins comprising halogenated polyolefins, e.g. PTFE
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B7/00—Layered products characterised by the relation between layers; Layered products characterised by the relative orientation of features between layers, or by the relative values of a measurable parameter between layers, i.e. products comprising layers having different physical, chemical or physicochemical properties; Layered products characterised by the interconnection of layers
- B32B7/04—Interconnection of layers
- B32B7/12—Interconnection of layers using interposed adhesives or interposed materials with bonding properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2027/00—Use of polyvinylhalogenides or derivatives thereof as moulding material
- B29K2027/08—PVDC, i.e. polyvinylidene chloride
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/70—Other properties
- B32B2307/732—Dimensional properties
- B32B2307/734—Dimensional stability
- B32B2307/736—Shrinkable
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2327/00—Polyvinylhalogenides
- B32B2327/12—Polyvinylhalogenides containing fluorine
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2439/00—Containers; Receptacles
- B32B2439/70—Food packaging
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/24—Structurally defined web or sheet [e.g., overall dimension, etc.]
- Y10T428/24942—Structurally defined web or sheet [e.g., overall dimension, etc.] including components having same physical characteristic in differing degree
- Y10T428/2495—Thickness [relative or absolute]
- Y10T428/24967—Absolute thicknesses specified
- Y10T428/24975—No layer or component greater than 5 mils thick
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31855—Of addition polymer from unsaturated monomers
- Y10T428/31931—Polyene monomer-containing
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31855—Of addition polymer from unsaturated monomers
- Y10T428/31935—Ester, halide or nitrile of addition polymer
Landscapes
- Laminated Bodies (AREA)
Abstract
TITLE OF THE INVENTION:
LAMINATE FILM
ABSTRACT OF THE DISCLOSURE:
Described is a laminate film excellent in oil-resistance, heat-resistant sealing ability and gas-barriering property having a percentage of heat-shrinkage of larger than 15 % at 90°C
comprising a center layer consisting of a copolymer(I) of vi-nylidene chloride and both two outermost layers consisting of a mixture of 20 to 70 % by weight of a copolymer(II) of ethylene and alpha-olefin of density of 0.900 to 0.950 and of crystalline melting point of 110 to 125°C and 80 to 30 % by weight of a copolymer(III) of ethylene and vinyl acetate with the proviso that the content of the copolymer(II) in the total amount of copolymers in both the two outermost layers is less than 65 %
by weight and showing a structure of having an adhesive layer between the center layer and the outermost layer.
LAMINATE FILM
ABSTRACT OF THE DISCLOSURE:
Described is a laminate film excellent in oil-resistance, heat-resistant sealing ability and gas-barriering property having a percentage of heat-shrinkage of larger than 15 % at 90°C
comprising a center layer consisting of a copolymer(I) of vi-nylidene chloride and both two outermost layers consisting of a mixture of 20 to 70 % by weight of a copolymer(II) of ethylene and alpha-olefin of density of 0.900 to 0.950 and of crystalline melting point of 110 to 125°C and 80 to 30 % by weight of a copolymer(III) of ethylene and vinyl acetate with the proviso that the content of the copolymer(II) in the total amount of copolymers in both the two outermost layers is less than 65 %
by weight and showing a structure of having an adhesive layer between the center layer and the outermost layer.
Description
1 1 70 .~ 5 !~
BACKGROUND OF THE INVENTION: ;
The present invention relates to a heat-shrinkable laminate film having a center layer of a copolymer of vinylidene chloride (hereinafter referred to as PVDC), both two outermost layers of a mixture of a copolymer of ethylene and alpha-olefin of a crystalline melting point of llO to 125C and a copolymer of ethylene and vinyl acetate (hereinafter referred to as EVA) of a crystalline melting point of 85 to 103C and two adhesive layers each of which is inserted between the- center layer and the outermost layer.
~ eat-shrink packaging is industrially most convenient as packing for foodstuffs having irregular shapes such as raw meats, cooked meats, cheeses and other ~a-tty foodstuffs. In addition, since a long period of preser~atlon is required to these packed foodstuffs, gas-barrier property is necessary for such a packaging material. Moreover, since i~ is necessary to subject the packed foodstuffs to heat-treatment for a certain time period for sterilization in the case where the foodstuff is cooked meat (for instance, for at least 8 minutes at 90C
against Escherichia coli), oil-resistance and peel-resistant of the sealed parts in the heat shrinkage (hereinafter referred to as peel-resistant) are required to the packing material.
More in detail, there are problems in packing and sterilizing the fatty foodstuffs of breaking the thinly stretched outermost layer which is softened by fats and heat and of breaking the seal part or its viciDity of the packins material due t~ the : '' l ~ 01~9 . ,,' heat-shrinking stress generating at the time of thermal sterili-zation or at the time of packing, and accordingly, a packaging material (film) of excellent oil-resistance and peel-resistant is keenly demanded in such a case.
As a hea-t-shrinkable film of gas-barrier property, a film consisting solely of PVDC, a laminate film of construction of EVA/PVDC/EVA disclosed in Canadian Patent No. 982,923, and a cylindrically formed laminate film of construction of EVA/
PVDC/irradiated EVA by radioactive rays disclosed in Japanese Patent Application Laying Open No. 34565/72, etc. are enumerable.
~ owever, the film consisting solely of PVDC has defects ¦ of causing hygienically undesirable cases-where the additives such as plasticizers and stabilizers .in the f~ilm migrate into the packed foodstuff according to the kinds of the packed foodstuffs and becoming an undesirable state for preserving the foodstuffs due to the reduction of gas-barrier property owing to the relatively large amount of the additives for maintaining cold-resistant strength of the film, etc.
Since the laminate film of the construction of EVA/
PVDC/EVA has the EVA layer as the outermost layer which is high in cold-resistant strength, it is not necessary to add a large amount of the additive into PVDC and accordingly, the problem of reduction of gas-barrier property has been solved, however, EVA has a defect of being poor in oil-reslstance and peel-resistant.
, _ _ .
1 170tS9 In Japanese Patent Application Laying Open No. 34565/72, a cross-l.inked EVA by radioactive rays is used for the purpose of improving the oil-resistance, however, only as one of the outermost layers for the fear of causing decomposition of PVDC in the center layer by the raclioactive irradiation. In addition, heat-resistant seal ability is not improved by the cross-linking by radioactive irradiation on EVA.
In order to obtain the laminate film excellent in oil-resistance, it is desirable to use a polymer of alpha-olefin of, for instance, a crystalline melting point o~ higher than 110C
as the two outermost layers. However, since the polymer of alpha-olefin of the crystalline melting point of higher than 110C is poor in stretchability, it is impossible to uniformly stretch after being laminated wlth a PVDC lay-er, and accordingly, ¦
heat-shrinkable laminate film can not be available.
In addition, in cases where polyethylene of low density ¦¦ of a crystalline melting point of lower than 110C or an ionomer ¦¦ is used, there is a defect of poor heat-resistant seal ability.
According to the above-mentioned reasons, a heat-shrinkable film excellent in oil-resistance, peel-resistant : and gas-barrier property has been demanded in the field of food-packaging.
As a result of elaborated studies, the present inventors have found that the laminate film comprising a center layer of a copolymer(I) of vinylidene chloride, both the two outermost layer3 of a mixture of 20 to 70 ~ by weight o' a copolymer(II~
3 17~3~5g , . . I
of ethylene and alpha-olefln of a density of 0.900 to 0.950 and of a crystalline melting point of 110 to 125C and ~0 to 30 %
~by weight of a copolymer(III) of ethylene and vinyl acetate of la crystalline melting point of 85 to 103C and adhesive layer !between the center layer and the outermost layer and having a percentage of heat-shrinkage of larger than 15 % at 90C, with the proviso that the content of the copoly~.er(II) in the total weight of both the two outermost layers is less than 65 %, is excellent in oil-resistance, peel-resistant and gas-barrier property.
It is an object of the present inventlon to provide a new heat-shrinkable laminate film for packaging foodstuff.
It is another object of the present invention to provide a new ¦¦heat-shrinkable laminate film, having an excellent properties in oil-resistance, peel resistant and gas barrier-ing properties.
BRIEF EXPLANATION OF THE DRAWINGS:
.
¦ In the drawings, Fig. 1 shows the range of composition of l the copolymer(III) of ethylene and vinyl acetate, the ordinate showing the melt index of the copolymer (g/10 min) and the absci-ssa showing the content (% by weight) of vinyl acetate units in the copolymer, and Fig. 2 shows a general chart of the process for preparing the laminate film of the present invention.
I DETAI~ED DESCRIPTION OF THE INVENTION:
The present invention relates to a heat-shrinkable film excellent in oil-resistance and peel-resistant and uniformly stretchable without giving minute local necking.
The heat-shrinkable film according to the present invention comprises a center layer of PVDC and two outermost ` _ 4 _ 70~59 layers both of which consist of a mixture of at least 20 % by ~weight of a copolymer of ethylene and alpha-olefin having a Icrystalline melting point of 110 to 125C and EVA of a ¦crystalline melting point of 85 to 103C and relatively rich in stretchability, and the film accord:ing to the present invention is superior in oil-resistance and peel resistant as compared to the laminate film having a polymer of alpha-olefin of a crystal-line melting point equal to the mean value of the crystalline melting points of the above-mentioned polymers of alpha-olefin as the two outermost layers.
In order that EVA of a crystalline melting point of 85 to 103C plays a role of improving the stretchability, it is ¦Inecessary that such EVA is contained in each of the two outermost layers in an amount of at least 30 % by weight. Accordingly, the resin of the two outermost layers consist-s of a mixture of 20 to 70 % by weight of a copolymer(II) of ethylene and alpha-¦olefin of a crystalline melting point of 110 to 125C and 80 to ! 30 % by weight of a copolymer(III). Besides, in order to carry l~out the heat-shrinking packing conveniently in industrial scale, the film having a rate of heat-shrinkage of higher than 15 ~
at a temperature of 90C is desirable. In order to prepare a film of a rate of heat-shrinkage of higher than 15 %, it is necessary to maintain the temperature at stretching as low as possible. For that purpose, it is necessary that EVA of a crystalline melting point of 85 to 103C which is rich in stretchability at a low temperature is contained in an amount of at least 35 % to the total amount of polymers in both the two outermost layers, and the amount of copolymer(II) in the total amount of polymers in both of the two outermost layers ll i _ 5 _ Il .
' I
~:~7(~15~ ~
.
should be less than 65 % by weight.
As the copolymer(II) of ethylene and alpha-olefin of a crystalline melting point of 110 to 125C, copolymers of ethylene and a small amount (1.0 to 30 % by weight) oE alpha- !
olefin of carbon number of less than 18, for lnstance, butene-l, pentene-l, 4-methylpentene-1, hexene-l, octene-l, etc. are used.
These copolymers are those referred to as linear low-density polyethylene (L-LDPE) of a density of 0.900 to 0.950 g/cc and of a cry~talline~melting point of 110 to 125C, for instance, ULTZEX, NEOZEX (both made by Mitsul Petrochemical Co.) and DOWLEX (made by Dow Chemical Co.), and are produced by copolymerization by using a catalyst consisting mainly of a transition metal. These copolymers are r-ich in stretchability in spite of their relatively high crystalline melting point and moreover, they are tenacious and rich in a~ti-stress-l cracking property.
`~ As EVA which is mixed with the above-mentioned copoly mer(II) of ethylene and alpha-olefin, those of the content of i vinyl acetate units of 3 to 12 % by weight are used. EVA
selected from these ranges of properties is fairly compatible with the copolymer(II~ to be rich in transparency and is oil-resistant, peel resistant, and easily stretchable~
Among such EVA, those included in the pentagonal range made by connecting the five points in Eig. 1, i.e., W-I (3,0.2), W-II (3,4.0), X-II (5,4.0), Z-III (12,1.5) and Z-I (12,0.2) with linear lines are preferable because of their excellent oil-resistance after mixing with the copolymer(II) of ethylene ll ~ 1 70~
nd alpha-ole in. Moreover, those included in the heptagonal range made by connecting the seven points i.n Fig. 1, i.e , W-I (3,002), W-II (3,4.0), X-II (5,4.0), X-I (5,2.0), Y-I (9~0~5)0 Z-II (12,0.5) and Z-I (12,0.2) with linear lines are most pre-ferable because of their excellent peel-resistant plus excellent oil-resistance after mixing with -the copolymer(II).
The above-mentioned melt-.index of the polymers is measured by the method is ASTM D-1238-79 (cf. Japanese Industrial Standard K-6730-1973), and their crystalline melting point is the temperature of the highest peak in the melting curve obtained by determining the melting point of the polymer with a differ ential scanning calorimeter (Type IB, made by Perkin-Elmer CoO) at a temperature rise rate of 8C/min.
PVDC for use in the present invention is a copolymer of 65 to 95 % by weight of vinylidene chloride and 5 to 35 %
by weight of at least one of unsaturated monomers polymerizabl.e with vinylidene chloride. As the copolymerizable monomer with vinylidene chloride, for instance, vinyl chloride, acrylonit-rile and alkyl acrylate of 1 to 18 carbon atoms in the alkyl ~roup are enumerable. Into PVDC, publicly known plast:i.clzerO
stabilizer, etc. may be added if necessaryO
Since a copolymer(II) of ethylene and alpha-olefin is originally not compatible with PVDC, the :Lam:ina-te made ~y piling the layer of PVDC and that of the copolymer(II) is apt to be exfoliated. Particularly, since there are many cases according to the present invention where it is necessary to ~ ~:170:~59 soak the laminate in hot water for a long period for sterili-zation, the laminate with weak mutual adhesion is apt to be exfoliated thus spoiling the appearance with additional reduction of peel-resistance.
Accordingly, it is necessary in the present invention to provide a layer of strong adhesion between the outermost layer and the center layer to prevent the e~foliation. As the material for such a layer of strong adhesion, polyolefin modified by carboxylic acid, copolymers of ethylene and vinyl acetate, block copolymer of styrene and bu*adiene and the like are used, and particularly, a copolymer of ethylene and vinyl acetate containing 13 to 25 % by weight of vinyl acetate units or a mixture of copolymers of ethylene and vinyl acetate ¦ containing in total of 13 to 25 % by-weight of vinyl acetate units is preferable. The preferable thickness of such a ~¦ layer of 1 to 3 microns.
¦¦ It is preferable to have the thickness of e~ch of the ¦ outermost layers of more than 18 % of the total thickness of the laminate, and the kinds of the copolymer(II) and EVA, the ratio of mixing of the copolymer(II) to EVA and the thickness of one of the outermost layers may be the same to or different from those of the other of the outermost layers.
In the case where the thickness of the layer playing the role of sealing is less than 18 % of the total thickness of the lamlnate (at least one of the two outermost layers in the ca e Of clasp-sealing and o h of the two outerl~ost lay-rs -.
:
ll 1170159 in the case of envelope-sealing), there is a tendency of giving poor peel-resistant. Total thickness of the laminate is pre^
ferably about 20 to 100 microns in generalO It is necessary to have at least 2 microns of the thlckness of the center layer for granting gas-barriering property and the thickness is preferably less than 30 % of the total thickness of the laminate because of a tendency of reducing the impact strength in the case of more than 30 %.
The cylindrically formed laminate film according to the present invention is extruded by using a circular die similar to that disclosed in Japanese Patent Application Laylng Open No. 82888/78 while supplying the melt materials from the nu~ber of extruders corresponding to the number of laminate layers.
The each layer of the flat laminate film according to the present invention is extruded by using a publicly known T--die while . supplying eaçh material from each extruder, and then laminated together.
A representative process ~or preparing the cylindrically formed laminate-film will be explained as follows while refer-ring to FigO 2 The mixture of copolymer(II) and (III)~ adhesi.ve re~inand PVDC are respectively extruded from the separate extruders (1)~ (1') and (1"~ and are supplied to the co-extruding circular die (2) to be a cylindrically formed laminated film (3), which is taken by the pair of nip-rollers (5) installed in a cooling bath (6) containing ~ater maintained at a temperature of low~r 1~0~59 than 40C to be an envelope-formed folded laminate film while being immediately quenched by water in the bath (6) and having a liquid (4) enclosed within the cylindrically formed part of I the laminate film (3) squeezed by the nip-rollers ~5), the ¦ liquid having been introduced for preventing the adhesion of ¦ the both two inner walls of the envelope-formed folded laminate film.
Then, the thus quenched envelope-formed laminate film Il is continuously pulled up from the bath (6) and transferred 10ll into a heating bath (8) containing hot water ~aintained at, for instance, 80 to 110C and/or an oven maintained at the same temperature (the oven is omitted from Fig. 2) and passed 1~ through the second pair of nip-rollers installed in the bath (8) ¦i or the oven while being heated.
Thereafter, the folded laminate film was inflated I between the second pair of nip-rollers (9) and the third pair j of nip-rollers (12) rotating at a speed of a few times, for instance 1.5 to 4.0 times, of that of the rotation of`the second I¦ pair of nip-rollers (9) by the air introduced and enclosed 201 between the both two internal walls of the envelope-formed laminate film while being cooled by the ambient atmosphere at ordinary temperature. By this inflation, a biaxial stretch-ing both 1.5 to 4.0 times into longitudinal direction and diametral direction is simultaneously carried out on the laminate film to prepare a heat-shrinkable laminate film (11) of t~e present inve~tion . . .
1 J 7~59 In the case of preparing the flat laminate film, the film extruded from the T-die is once cooled by the chilling rolls right below the die, and then, after being heated to a predetermined temperature, stretched between the pair of rolls into the direction of material flow and stretched into the direction of width by a tenter in a successive biaxial stretching, or stretched simultaneously into both directions of flow-direction and width-direction by a different tenter to be a heat-shrinkable film.
The heat-shrinkable stretched laminate film according to the present invention obtained by the above-mentioned process is excellent in oil-resistance, heat-resistant seal ability and gas-barriering property and desirably used for packing fatty foodstuffs requiring sterilization at a high temperature.
The present invention will be explained more in detail while referring to non limitativ~ examples as follows:
EXAMPLES 1- ~ 15:
. ~ .
By using a plurality o extruders corresponding to each combination of resins shown in Table 2 (refer to each member of polymers in Table 1), respective resins of each combination were extruded from the xespective extruders and these extruded resins were co-extruded via the co-extruding die to be a cylindrically formed laminate with the desired combination.
The thus extruded cylindrically formed laminate was quenched in a cooling bath at about 20C to be cylinder of 120 mm in folded width and of 250 ~ 980 microns in thickness.
137V~59 In the thus extruded cylindrically formed laminate, a suitable amount of soybean oil had been enclosed in advance of quenching for the prevention of adhesion of both the inner surfaces of the laminate when it was folded. Then, the cylinder was heated for about 12 sec in a hot water bath maintained at a temperature shown in Table 2 while beillg transferred in the bath at a rate of 5 m/min and passed betwe-e.~.-the first nip-rollers of a revoluting rate of 5 m/min. Thereafter, the I heated cylinder was stretched by 3 times into the longitudinal 10l direction while being stretched into transvers directlon by inflating the cylinder with an air supplied into the cylinder 3.3 times of the original diameter until pa-ssing between the second nip-rollers of a revoluting rate of 1-5 m/min while being cooled by an ambient atmosphere at ordinary temperature.
The thus obtained biaxially stretched laminate film was about i 360 mm in folded width and about 25 ~ 98 mi-crons in thickness.
Table 1 shows the physical properties of each polymer used for preparing the laminate film with an index; Table 2 1I shows the composition and constitution of the laminate film 20,¦ prepared as above; Table 3 shows the test met-hods of physical ¦¦ properties of the laminate film and Table 4 shows the test ~esults of the 1a~in~te ~ilm.
~ 12 -,, 11 1 17~159 Table 1: Polymers and Copolymers . _~
Index of Polymers Melt index Density Content of Crystalline polymer and melt. point copolymers (g/10 min) (g/cc) VAc(wt.%) (C) A r Tr ~ ~
C L-LDPE 2.5 0.922 _ 122 D L-LDPE ~ 2.5 0.93 _ 122 E L-LDPE 0.7 0.922 _ 120 0 F L-LDPE 1.8 0.935 122 G Low-density 1.2 0.922 _ 107 pleoneye thy- . . __ .
H EVA 0.3 0.93 3 103 I EVA 3.8 0.93 3.5 101 J EVA 0.5 0.93 5 97 K EVA 2.0 0.93 5 .97 L EVA 1.1 0.93 5.5 96 M EVA 3.3 O.93 6 95 N EVA - 0.2 0.93 8 94 O EVA 0.5 0.93 9 93 _ ~
P EVA 1.5 0.93 10 91 Q EVA 3 0.93 10 90 R EVA 0.35 0.94 12 85 S EVA 0.8 0.94 12 85 .. : to be continued Table 1: (Continued) , Index of ¦ Polymers Melt index¦ Density ¦ Content of ¦ Crystalline polymer and melt. point copolymers (g/10 min) (g/cc) VAc(wt.~) (C) i _ _ .__ _ _ jl T EVA 3 O . 94 15 82 I l 1~ EVA 6 O . 9 5 2 8 _ V modif ed 15 0.97 19 _ carboxylic 0~; acid . ~ . ___ I Notes: A is a composition of 100 part-s of copolymer of vinylidene chloride and vinyl chloride of 80:20 ! and 1 part of epoxyfied soybean oiL.
Il B is a composition of 100 parts of copolymer of il vinylidene chloride and vinyl-c~l-orld-e of 85 15 and 'j 0.5 part of epoxyfied soybean oil.
C and D: Linear low-dens~y polye-thylene, commercial name of ULTOZEX. (-~ts~i- Pe-trochemical Co.) ll E and F: Linear low-density polyethylene, commercial 20', name of NEOZEX ~ (Mitsui Petrochemical Co.) ,i V lS resin for an adhesive, commercial name of ADMER.
(Mitsui Petrochemical Co.) 1~ , ll ' ,, 7{~ 1 5 9 .
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,11 117~159 Table 3: Me-thods of Determination Item Method . __ A specimen of 10 cm in length and also in width cut out from the laminate fil~
is immersed into hot water a-t 90C in a relaxed state for one minu-te. The Rate of shrinkage rate of linear shrinkage of the film in hot water into direction of length, and that into direction of width were respectively expressed by L and T in percentage as compared to the original dimensions.
. .. _____ __ _ Vacuum-packed meat loaf with the speci-men is immersed into hot water a-t 90C
on which surface an oil is intentional-ly floated for 8 min, or vacuum-packed Oil-resisiance loast pork (Chinese style) with the specimen is-immersed into the same manner for lO mini. After cooling the foodstuff, the damage of the outermost layer is observed.
Heat-sealed specimen (c~asp-type seal-~eat-resistan-t seal ing or envelope-type sealing) is abiIity stretched onto an embroidary frame with about 5% of reserve, and after pain~ing lard on the specimen, it is immersed into hot water of 85C. The time until the seal part is broken is measured in sec.
....____ i . ..
1 17~59 Table 4: Test Results of Laminate Film _ Example Stretch- Rate of Oil-resistance Heat- Gas-barrier- iability heat- of the layers resistant ing property I
. (%, L/Tl~) First Fifth ability (cc/cm2 day 1 possible 42/47 1 2 ¦ 2 ~ 42 I
BACKGROUND OF THE INVENTION: ;
The present invention relates to a heat-shrinkable laminate film having a center layer of a copolymer of vinylidene chloride (hereinafter referred to as PVDC), both two outermost layers of a mixture of a copolymer of ethylene and alpha-olefin of a crystalline melting point of llO to 125C and a copolymer of ethylene and vinyl acetate (hereinafter referred to as EVA) of a crystalline melting point of 85 to 103C and two adhesive layers each of which is inserted between the- center layer and the outermost layer.
~ eat-shrink packaging is industrially most convenient as packing for foodstuffs having irregular shapes such as raw meats, cooked meats, cheeses and other ~a-tty foodstuffs. In addition, since a long period of preser~atlon is required to these packed foodstuffs, gas-barrier property is necessary for such a packaging material. Moreover, since i~ is necessary to subject the packed foodstuffs to heat-treatment for a certain time period for sterilization in the case where the foodstuff is cooked meat (for instance, for at least 8 minutes at 90C
against Escherichia coli), oil-resistance and peel-resistant of the sealed parts in the heat shrinkage (hereinafter referred to as peel-resistant) are required to the packing material.
More in detail, there are problems in packing and sterilizing the fatty foodstuffs of breaking the thinly stretched outermost layer which is softened by fats and heat and of breaking the seal part or its viciDity of the packins material due t~ the : '' l ~ 01~9 . ,,' heat-shrinking stress generating at the time of thermal sterili-zation or at the time of packing, and accordingly, a packaging material (film) of excellent oil-resistance and peel-resistant is keenly demanded in such a case.
As a hea-t-shrinkable film of gas-barrier property, a film consisting solely of PVDC, a laminate film of construction of EVA/PVDC/EVA disclosed in Canadian Patent No. 982,923, and a cylindrically formed laminate film of construction of EVA/
PVDC/irradiated EVA by radioactive rays disclosed in Japanese Patent Application Laying Open No. 34565/72, etc. are enumerable.
~ owever, the film consisting solely of PVDC has defects ¦ of causing hygienically undesirable cases-where the additives such as plasticizers and stabilizers .in the f~ilm migrate into the packed foodstuff according to the kinds of the packed foodstuffs and becoming an undesirable state for preserving the foodstuffs due to the reduction of gas-barrier property owing to the relatively large amount of the additives for maintaining cold-resistant strength of the film, etc.
Since the laminate film of the construction of EVA/
PVDC/EVA has the EVA layer as the outermost layer which is high in cold-resistant strength, it is not necessary to add a large amount of the additive into PVDC and accordingly, the problem of reduction of gas-barrier property has been solved, however, EVA has a defect of being poor in oil-reslstance and peel-resistant.
, _ _ .
1 170tS9 In Japanese Patent Application Laying Open No. 34565/72, a cross-l.inked EVA by radioactive rays is used for the purpose of improving the oil-resistance, however, only as one of the outermost layers for the fear of causing decomposition of PVDC in the center layer by the raclioactive irradiation. In addition, heat-resistant seal ability is not improved by the cross-linking by radioactive irradiation on EVA.
In order to obtain the laminate film excellent in oil-resistance, it is desirable to use a polymer of alpha-olefin of, for instance, a crystalline melting point o~ higher than 110C
as the two outermost layers. However, since the polymer of alpha-olefin of the crystalline melting point of higher than 110C is poor in stretchability, it is impossible to uniformly stretch after being laminated wlth a PVDC lay-er, and accordingly, ¦
heat-shrinkable laminate film can not be available.
In addition, in cases where polyethylene of low density ¦¦ of a crystalline melting point of lower than 110C or an ionomer ¦¦ is used, there is a defect of poor heat-resistant seal ability.
According to the above-mentioned reasons, a heat-shrinkable film excellent in oil-resistance, peel-resistant : and gas-barrier property has been demanded in the field of food-packaging.
As a result of elaborated studies, the present inventors have found that the laminate film comprising a center layer of a copolymer(I) of vinylidene chloride, both the two outermost layer3 of a mixture of 20 to 70 ~ by weight o' a copolymer(II~
3 17~3~5g , . . I
of ethylene and alpha-olefln of a density of 0.900 to 0.950 and of a crystalline melting point of 110 to 125C and ~0 to 30 %
~by weight of a copolymer(III) of ethylene and vinyl acetate of la crystalline melting point of 85 to 103C and adhesive layer !between the center layer and the outermost layer and having a percentage of heat-shrinkage of larger than 15 % at 90C, with the proviso that the content of the copoly~.er(II) in the total weight of both the two outermost layers is less than 65 %, is excellent in oil-resistance, peel-resistant and gas-barrier property.
It is an object of the present inventlon to provide a new heat-shrinkable laminate film for packaging foodstuff.
It is another object of the present invention to provide a new ¦¦heat-shrinkable laminate film, having an excellent properties in oil-resistance, peel resistant and gas barrier-ing properties.
BRIEF EXPLANATION OF THE DRAWINGS:
.
¦ In the drawings, Fig. 1 shows the range of composition of l the copolymer(III) of ethylene and vinyl acetate, the ordinate showing the melt index of the copolymer (g/10 min) and the absci-ssa showing the content (% by weight) of vinyl acetate units in the copolymer, and Fig. 2 shows a general chart of the process for preparing the laminate film of the present invention.
I DETAI~ED DESCRIPTION OF THE INVENTION:
The present invention relates to a heat-shrinkable film excellent in oil-resistance and peel-resistant and uniformly stretchable without giving minute local necking.
The heat-shrinkable film according to the present invention comprises a center layer of PVDC and two outermost ` _ 4 _ 70~59 layers both of which consist of a mixture of at least 20 % by ~weight of a copolymer of ethylene and alpha-olefin having a Icrystalline melting point of 110 to 125C and EVA of a ¦crystalline melting point of 85 to 103C and relatively rich in stretchability, and the film accord:ing to the present invention is superior in oil-resistance and peel resistant as compared to the laminate film having a polymer of alpha-olefin of a crystal-line melting point equal to the mean value of the crystalline melting points of the above-mentioned polymers of alpha-olefin as the two outermost layers.
In order that EVA of a crystalline melting point of 85 to 103C plays a role of improving the stretchability, it is ¦Inecessary that such EVA is contained in each of the two outermost layers in an amount of at least 30 % by weight. Accordingly, the resin of the two outermost layers consist-s of a mixture of 20 to 70 % by weight of a copolymer(II) of ethylene and alpha-¦olefin of a crystalline melting point of 110 to 125C and 80 to ! 30 % by weight of a copolymer(III). Besides, in order to carry l~out the heat-shrinking packing conveniently in industrial scale, the film having a rate of heat-shrinkage of higher than 15 ~
at a temperature of 90C is desirable. In order to prepare a film of a rate of heat-shrinkage of higher than 15 %, it is necessary to maintain the temperature at stretching as low as possible. For that purpose, it is necessary that EVA of a crystalline melting point of 85 to 103C which is rich in stretchability at a low temperature is contained in an amount of at least 35 % to the total amount of polymers in both the two outermost layers, and the amount of copolymer(II) in the total amount of polymers in both of the two outermost layers ll i _ 5 _ Il .
' I
~:~7(~15~ ~
.
should be less than 65 % by weight.
As the copolymer(II) of ethylene and alpha-olefin of a crystalline melting point of 110 to 125C, copolymers of ethylene and a small amount (1.0 to 30 % by weight) oE alpha- !
olefin of carbon number of less than 18, for lnstance, butene-l, pentene-l, 4-methylpentene-1, hexene-l, octene-l, etc. are used.
These copolymers are those referred to as linear low-density polyethylene (L-LDPE) of a density of 0.900 to 0.950 g/cc and of a cry~talline~melting point of 110 to 125C, for instance, ULTZEX, NEOZEX (both made by Mitsul Petrochemical Co.) and DOWLEX (made by Dow Chemical Co.), and are produced by copolymerization by using a catalyst consisting mainly of a transition metal. These copolymers are r-ich in stretchability in spite of their relatively high crystalline melting point and moreover, they are tenacious and rich in a~ti-stress-l cracking property.
`~ As EVA which is mixed with the above-mentioned copoly mer(II) of ethylene and alpha-olefin, those of the content of i vinyl acetate units of 3 to 12 % by weight are used. EVA
selected from these ranges of properties is fairly compatible with the copolymer(II~ to be rich in transparency and is oil-resistant, peel resistant, and easily stretchable~
Among such EVA, those included in the pentagonal range made by connecting the five points in Eig. 1, i.e., W-I (3,0.2), W-II (3,4.0), X-II (5,4.0), Z-III (12,1.5) and Z-I (12,0.2) with linear lines are preferable because of their excellent oil-resistance after mixing with the copolymer(II) of ethylene ll ~ 1 70~
nd alpha-ole in. Moreover, those included in the heptagonal range made by connecting the seven points i.n Fig. 1, i.e , W-I (3,002), W-II (3,4.0), X-II (5,4.0), X-I (5,2.0), Y-I (9~0~5)0 Z-II (12,0.5) and Z-I (12,0.2) with linear lines are most pre-ferable because of their excellent peel-resistant plus excellent oil-resistance after mixing with -the copolymer(II).
The above-mentioned melt-.index of the polymers is measured by the method is ASTM D-1238-79 (cf. Japanese Industrial Standard K-6730-1973), and their crystalline melting point is the temperature of the highest peak in the melting curve obtained by determining the melting point of the polymer with a differ ential scanning calorimeter (Type IB, made by Perkin-Elmer CoO) at a temperature rise rate of 8C/min.
PVDC for use in the present invention is a copolymer of 65 to 95 % by weight of vinylidene chloride and 5 to 35 %
by weight of at least one of unsaturated monomers polymerizabl.e with vinylidene chloride. As the copolymerizable monomer with vinylidene chloride, for instance, vinyl chloride, acrylonit-rile and alkyl acrylate of 1 to 18 carbon atoms in the alkyl ~roup are enumerable. Into PVDC, publicly known plast:i.clzerO
stabilizer, etc. may be added if necessaryO
Since a copolymer(II) of ethylene and alpha-olefin is originally not compatible with PVDC, the :Lam:ina-te made ~y piling the layer of PVDC and that of the copolymer(II) is apt to be exfoliated. Particularly, since there are many cases according to the present invention where it is necessary to ~ ~:170:~59 soak the laminate in hot water for a long period for sterili-zation, the laminate with weak mutual adhesion is apt to be exfoliated thus spoiling the appearance with additional reduction of peel-resistance.
Accordingly, it is necessary in the present invention to provide a layer of strong adhesion between the outermost layer and the center layer to prevent the e~foliation. As the material for such a layer of strong adhesion, polyolefin modified by carboxylic acid, copolymers of ethylene and vinyl acetate, block copolymer of styrene and bu*adiene and the like are used, and particularly, a copolymer of ethylene and vinyl acetate containing 13 to 25 % by weight of vinyl acetate units or a mixture of copolymers of ethylene and vinyl acetate ¦ containing in total of 13 to 25 % by-weight of vinyl acetate units is preferable. The preferable thickness of such a ~¦ layer of 1 to 3 microns.
¦¦ It is preferable to have the thickness of e~ch of the ¦ outermost layers of more than 18 % of the total thickness of the laminate, and the kinds of the copolymer(II) and EVA, the ratio of mixing of the copolymer(II) to EVA and the thickness of one of the outermost layers may be the same to or different from those of the other of the outermost layers.
In the case where the thickness of the layer playing the role of sealing is less than 18 % of the total thickness of the lamlnate (at least one of the two outermost layers in the ca e Of clasp-sealing and o h of the two outerl~ost lay-rs -.
:
ll 1170159 in the case of envelope-sealing), there is a tendency of giving poor peel-resistant. Total thickness of the laminate is pre^
ferably about 20 to 100 microns in generalO It is necessary to have at least 2 microns of the thlckness of the center layer for granting gas-barriering property and the thickness is preferably less than 30 % of the total thickness of the laminate because of a tendency of reducing the impact strength in the case of more than 30 %.
The cylindrically formed laminate film according to the present invention is extruded by using a circular die similar to that disclosed in Japanese Patent Application Laylng Open No. 82888/78 while supplying the melt materials from the nu~ber of extruders corresponding to the number of laminate layers.
The each layer of the flat laminate film according to the present invention is extruded by using a publicly known T--die while . supplying eaçh material from each extruder, and then laminated together.
A representative process ~or preparing the cylindrically formed laminate-film will be explained as follows while refer-ring to FigO 2 The mixture of copolymer(II) and (III)~ adhesi.ve re~inand PVDC are respectively extruded from the separate extruders (1)~ (1') and (1"~ and are supplied to the co-extruding circular die (2) to be a cylindrically formed laminated film (3), which is taken by the pair of nip-rollers (5) installed in a cooling bath (6) containing ~ater maintained at a temperature of low~r 1~0~59 than 40C to be an envelope-formed folded laminate film while being immediately quenched by water in the bath (6) and having a liquid (4) enclosed within the cylindrically formed part of I the laminate film (3) squeezed by the nip-rollers ~5), the ¦ liquid having been introduced for preventing the adhesion of ¦ the both two inner walls of the envelope-formed folded laminate film.
Then, the thus quenched envelope-formed laminate film Il is continuously pulled up from the bath (6) and transferred 10ll into a heating bath (8) containing hot water ~aintained at, for instance, 80 to 110C and/or an oven maintained at the same temperature (the oven is omitted from Fig. 2) and passed 1~ through the second pair of nip-rollers installed in the bath (8) ¦i or the oven while being heated.
Thereafter, the folded laminate film was inflated I between the second pair of nip-rollers (9) and the third pair j of nip-rollers (12) rotating at a speed of a few times, for instance 1.5 to 4.0 times, of that of the rotation of`the second I¦ pair of nip-rollers (9) by the air introduced and enclosed 201 between the both two internal walls of the envelope-formed laminate film while being cooled by the ambient atmosphere at ordinary temperature. By this inflation, a biaxial stretch-ing both 1.5 to 4.0 times into longitudinal direction and diametral direction is simultaneously carried out on the laminate film to prepare a heat-shrinkable laminate film (11) of t~e present inve~tion . . .
1 J 7~59 In the case of preparing the flat laminate film, the film extruded from the T-die is once cooled by the chilling rolls right below the die, and then, after being heated to a predetermined temperature, stretched between the pair of rolls into the direction of material flow and stretched into the direction of width by a tenter in a successive biaxial stretching, or stretched simultaneously into both directions of flow-direction and width-direction by a different tenter to be a heat-shrinkable film.
The heat-shrinkable stretched laminate film according to the present invention obtained by the above-mentioned process is excellent in oil-resistance, heat-resistant seal ability and gas-barriering property and desirably used for packing fatty foodstuffs requiring sterilization at a high temperature.
The present invention will be explained more in detail while referring to non limitativ~ examples as follows:
EXAMPLES 1- ~ 15:
. ~ .
By using a plurality o extruders corresponding to each combination of resins shown in Table 2 (refer to each member of polymers in Table 1), respective resins of each combination were extruded from the xespective extruders and these extruded resins were co-extruded via the co-extruding die to be a cylindrically formed laminate with the desired combination.
The thus extruded cylindrically formed laminate was quenched in a cooling bath at about 20C to be cylinder of 120 mm in folded width and of 250 ~ 980 microns in thickness.
137V~59 In the thus extruded cylindrically formed laminate, a suitable amount of soybean oil had been enclosed in advance of quenching for the prevention of adhesion of both the inner surfaces of the laminate when it was folded. Then, the cylinder was heated for about 12 sec in a hot water bath maintained at a temperature shown in Table 2 while beillg transferred in the bath at a rate of 5 m/min and passed betwe-e.~.-the first nip-rollers of a revoluting rate of 5 m/min. Thereafter, the I heated cylinder was stretched by 3 times into the longitudinal 10l direction while being stretched into transvers directlon by inflating the cylinder with an air supplied into the cylinder 3.3 times of the original diameter until pa-ssing between the second nip-rollers of a revoluting rate of 1-5 m/min while being cooled by an ambient atmosphere at ordinary temperature.
The thus obtained biaxially stretched laminate film was about i 360 mm in folded width and about 25 ~ 98 mi-crons in thickness.
Table 1 shows the physical properties of each polymer used for preparing the laminate film with an index; Table 2 1I shows the composition and constitution of the laminate film 20,¦ prepared as above; Table 3 shows the test met-hods of physical ¦¦ properties of the laminate film and Table 4 shows the test ~esults of the 1a~in~te ~ilm.
~ 12 -,, 11 1 17~159 Table 1: Polymers and Copolymers . _~
Index of Polymers Melt index Density Content of Crystalline polymer and melt. point copolymers (g/10 min) (g/cc) VAc(wt.%) (C) A r Tr ~ ~
C L-LDPE 2.5 0.922 _ 122 D L-LDPE ~ 2.5 0.93 _ 122 E L-LDPE 0.7 0.922 _ 120 0 F L-LDPE 1.8 0.935 122 G Low-density 1.2 0.922 _ 107 pleoneye thy- . . __ .
H EVA 0.3 0.93 3 103 I EVA 3.8 0.93 3.5 101 J EVA 0.5 0.93 5 97 K EVA 2.0 0.93 5 .97 L EVA 1.1 0.93 5.5 96 M EVA 3.3 O.93 6 95 N EVA - 0.2 0.93 8 94 O EVA 0.5 0.93 9 93 _ ~
P EVA 1.5 0.93 10 91 Q EVA 3 0.93 10 90 R EVA 0.35 0.94 12 85 S EVA 0.8 0.94 12 85 .. : to be continued Table 1: (Continued) , Index of ¦ Polymers Melt index¦ Density ¦ Content of ¦ Crystalline polymer and melt. point copolymers (g/10 min) (g/cc) VAc(wt.~) (C) i _ _ .__ _ _ jl T EVA 3 O . 94 15 82 I l 1~ EVA 6 O . 9 5 2 8 _ V modif ed 15 0.97 19 _ carboxylic 0~; acid . ~ . ___ I Notes: A is a composition of 100 part-s of copolymer of vinylidene chloride and vinyl chloride of 80:20 ! and 1 part of epoxyfied soybean oiL.
Il B is a composition of 100 parts of copolymer of il vinylidene chloride and vinyl-c~l-orld-e of 85 15 and 'j 0.5 part of epoxyfied soybean oil.
C and D: Linear low-dens~y polye-thylene, commercial name of ULTOZEX. (-~ts~i- Pe-trochemical Co.) ll E and F: Linear low-density polyethylene, commercial 20', name of NEOZEX ~ (Mitsui Petrochemical Co.) ,i V lS resin for an adhesive, commercial name of ADMER.
(Mitsui Petrochemical Co.) 1~ , ll ' ,, 7{~ 1 5 9 .
h V ~`I ~ ~1 ~ 1_ ~D ~D 1` ~ 1` ~D CO r` ~
a~ a~
~0 ,~ ~ ~ ~ $ ,~ ~0 Q~ s ~c o ~ ~ o u~ ~ ~ D
6 ~ (~ ~ ) ( E~ Orq . O
~ ~ , ... __ .4 h ~ ~ ~ : ~
0 u 3 ~ ~ o o o ~ ~ ~ r~ ~ ~ ~ o o ~ .
o 2 ~o .~ . .
,1 .
,- ~
.~, ~ ~ ~ ~ ~ C ~ o o~ o ~ o o .~.c ~ ~
a~ ~ ~ 1- 1~ OD
Ul ~ ~ ~
U ~ o ~ ~ ~ ~ Z ~ .
.
.OS Ih N ~ ~ ^ ~ N ~ t`l ~) 1--I ~`1 ~1 ~)a) ~ _ "7 _ _ _ _ 1~, _ _ ~ _ _ .~t~~0 ^ E~ ~, E~ ~ E~ E~ 11 E~ E~ ~ E~ E~ 11 U ~ ,1 . 4-1h ~) O O O O O O ô O CO C~ 1 . O~C ~ _ _ _ _ _ _ _ _ _ _ _ _ _ . r~E~-rt ~ ~ m ~ ~ o Q V~ -rl -- _ _ . ~ o 6 _ L" _ _ ~, t~
8 c~ E~ ~ E~ E I E-f 11 E~ E~ E~ E~ E~ D
_ ~ ~ , ~
_ ~r ~r ~ ~ ~ ~ ~ ~D ~ O ~`I O O
~ _ _ _ _ _ _ ~_ _ _ _ _ _ _ C) ~ ~
.
~1 X ,1 ~ n ~ o ~1 ~
. ~
!~ 1 17~5~
V 3 ---- N~D ~ N ~) ~ O ~ ~ O O O ~ O O 5~
~ C LO ~1 o~r o o o E~
~051 (11~1 I~ a~,~ ~, ~-C O
I ~ ~ . .i. I
. ¦ i H X
ll ~ 1 ~ O l l l l l l ~ .
~ 3 ~ i ~ !
_ ~- I
.,. O N ~ ~ _ N î~ î_ ~
. I J,J t` ~ N N ~1 _ - _ _ O
. i . ~ ~ ~~1 ~ N ~1 'i ~ U ~ 1~4 U ~ 14 14 ~ O
~0-0 i ~ r~ N _ _ N N ~
.i ~ (D ~0 ~ E~ _ _ _ _ ~ ~ I
~ ~ ~ ' I! ~ a) ~ ~ ô ô ô ô o ô ô Ci ~
Il ~ ~ ~ _ ~ ~ ~ ~ ~ ~ 0 1 ~ a.) O .~ ~ ¢ r5 ~ r5 r~ r5 r5 r--I
Il ~t .,1 (1~ ~ O
Il Qi ~i s~ ~ ~ ~ ~ E~
J~ O . ~r :i N N N N N ~
U ~ ~ E~ _ _ _ _ ~.~ ~' ' ~; ô ~ ô ô ~r ~
_ _ N ~ ~ _ _ _ r~ ~ co r~) .~1 N ('~ O
_ __H :~ ~ U 1~ ., .
1~1 _1 ~ ~ ` ~ Z
. 1, -16- ' ~
,11 117~159 Table 3: Me-thods of Determination Item Method . __ A specimen of 10 cm in length and also in width cut out from the laminate fil~
is immersed into hot water a-t 90C in a relaxed state for one minu-te. The Rate of shrinkage rate of linear shrinkage of the film in hot water into direction of length, and that into direction of width were respectively expressed by L and T in percentage as compared to the original dimensions.
. .. _____ __ _ Vacuum-packed meat loaf with the speci-men is immersed into hot water a-t 90C
on which surface an oil is intentional-ly floated for 8 min, or vacuum-packed Oil-resisiance loast pork (Chinese style) with the specimen is-immersed into the same manner for lO mini. After cooling the foodstuff, the damage of the outermost layer is observed.
Heat-sealed specimen (c~asp-type seal-~eat-resistan-t seal ing or envelope-type sealing) is abiIity stretched onto an embroidary frame with about 5% of reserve, and after pain~ing lard on the specimen, it is immersed into hot water of 85C. The time until the seal part is broken is measured in sec.
....____ i . ..
1 17~59 Table 4: Test Results of Laminate Film _ Example Stretch- Rate of Oil-resistance Heat- Gas-barrier- iability heat- of the layers resistant ing property I
. (%, L/Tl~) First Fifth ability (cc/cm2 day 1 possible 42/47 1 2 ¦ 2 ~ 42 I
2 possible 37/41 1 1 ¦ 2 ~ 42 I
3 possible 39/42 1 1 ¦ 2 ¦ 42 ¦
4 possible 40/45 1 1 ¦ 2 ¦ 42 .
10 1 5 possible 30/36 1 1 ! 1 1 42 i . l l 6 possible 35/39 1 1 1 42 7 possible 33/41 1 1 1 42 il 8 possible 36/38 1 1 . 42 9 possible 32/37 1 1 1 15 ~I 10 possible 37/42 1 1 1 52 ., 11 possible 37/40 1 1 1 52 I
., 12 possible 28/35 1 1 1l) 68 ,,. 13 possible 32/35 1 1 1l) 68 il 14 poss.ible 35/39 1 1 1 34 20,¦ 15 possible 38/43 2 1 2 42 l ~ i , Comparative l .
Example l , 1 possible 43/47 3 3 ¦ 3 42 2 with minute 32/36 1 1 ¦ 2 42 necking l ll 3 possible 42/46 1 2 ¦ 3 42 ¦¦ . to be continued - 18 - :
,11 ~ 5 9 Table 4: ~Continued) Example Stretch- Rate of Oil-resistance Peel- ¦ Gas-barrier-ability heat- of the layersResis- ing property shrinkage tant(cc/cm2 day.
(%, L/Tl)) First Fi:fth ability atom.) 4 hardly _ ~ _ _ stretchable possible 44/48 3 2 2 42 6 possible 45/48 3 3 _ 0 Note: Oil-resistance is evaluated as: 1 no change found on meatloaf and pork; 2 no chanye found on meatloaf;
3 breakage found on the outermost layer.
Peel-resistant ability is evaluated as: 1 over 60 sec, 2 less than 60 sec and more -than 10 sec, and 3 less than 10 sec.
1) envelope-type sealing. The remalnder is clasp-type sealing.
In the case of clasp-type sealing, the fifth layer becomes to be the seal surface.
11 1 170~
As are seen in Examples 1 to 15 in Table 4, the laminate film according to the present invention showed excellent stretch-ability, oil-resistance, peel-resistant and gas-barrier property.
The laminate film of Comparative Example 1 showed i breaking in oil-resistance test, and showed poor peel-resistant ! because of the content of the copolymer(II) in the first layer of less than 10 ~ by weight, and of the crys-talline melting point of the low-density polyethylene of lower than 110C.
10~ The laminate film of Comparative Example 2 showed ` poor stretchability with minute neckings bec-ause of the content of EVA in the first layer of less than 30 ~ by weight.
The laminate ~ilm of Comparative ExampLe 3 showed poor peel-resistant ability because of the lac~ oE any adhesive ;
layers~
The laminate film of Comparative Example 4 was impos-sible to be obtained because both the first and the fifth layers were to be composed of low-density polyethy]ene without using any adhesive layers.
The laminate film of Comparative Example 5 was poor in oil-resistance because of the content of the copolymer(II) in the first layer of 10 ~ by weight.
The laminate film of Comparative Example 6 was poor in oil-resistance because of the crystalline melting point of EVA in the first layer and the fifth layer of as low as 82C, and poor in peel-resistant.
!
.:
10 1 5 possible 30/36 1 1 ! 1 1 42 i . l l 6 possible 35/39 1 1 1 42 7 possible 33/41 1 1 1 42 il 8 possible 36/38 1 1 . 42 9 possible 32/37 1 1 1 15 ~I 10 possible 37/42 1 1 1 52 ., 11 possible 37/40 1 1 1 52 I
., 12 possible 28/35 1 1 1l) 68 ,,. 13 possible 32/35 1 1 1l) 68 il 14 poss.ible 35/39 1 1 1 34 20,¦ 15 possible 38/43 2 1 2 42 l ~ i , Comparative l .
Example l , 1 possible 43/47 3 3 ¦ 3 42 2 with minute 32/36 1 1 ¦ 2 42 necking l ll 3 possible 42/46 1 2 ¦ 3 42 ¦¦ . to be continued - 18 - :
,11 ~ 5 9 Table 4: ~Continued) Example Stretch- Rate of Oil-resistance Peel- ¦ Gas-barrier-ability heat- of the layersResis- ing property shrinkage tant(cc/cm2 day.
(%, L/Tl)) First Fi:fth ability atom.) 4 hardly _ ~ _ _ stretchable possible 44/48 3 2 2 42 6 possible 45/48 3 3 _ 0 Note: Oil-resistance is evaluated as: 1 no change found on meatloaf and pork; 2 no chanye found on meatloaf;
3 breakage found on the outermost layer.
Peel-resistant ability is evaluated as: 1 over 60 sec, 2 less than 60 sec and more -than 10 sec, and 3 less than 10 sec.
1) envelope-type sealing. The remalnder is clasp-type sealing.
In the case of clasp-type sealing, the fifth layer becomes to be the seal surface.
11 1 170~
As are seen in Examples 1 to 15 in Table 4, the laminate film according to the present invention showed excellent stretch-ability, oil-resistance, peel-resistant and gas-barrier property.
The laminate film of Comparative Example 1 showed i breaking in oil-resistance test, and showed poor peel-resistant ! because of the content of the copolymer(II) in the first layer of less than 10 ~ by weight, and of the crys-talline melting point of the low-density polyethylene of lower than 110C.
10~ The laminate film of Comparative Example 2 showed ` poor stretchability with minute neckings bec-ause of the content of EVA in the first layer of less than 30 ~ by weight.
The laminate ~ilm of Comparative ExampLe 3 showed poor peel-resistant ability because of the lac~ oE any adhesive ;
layers~
The laminate film of Comparative Example 4 was impos-sible to be obtained because both the first and the fifth layers were to be composed of low-density polyethy]ene without using any adhesive layers.
The laminate film of Comparative Example 5 was poor in oil-resistance because of the content of the copolymer(II) in the first layer of 10 ~ by weight.
The laminate film of Comparative Example 6 was poor in oil-resistance because of the crystalline melting point of EVA in the first layer and the fifth layer of as low as 82C, and poor in peel-resistant.
!
.:
Claims (6)
1. A laminate film of the rate of heat-shrinkage at 90°C of higher than 15 % comprising the center layer consisting of a copolymer(I) of vinylidene chloride and both the outer-most layers consisting of a mixture of 20 to 70 % by weight of a copolymer(II) of ethylene and alpha-olefin of a crystalline melting point of 110 to 125°C and 80 to 30 % by weight of a copolymer(III) of ethylene and vinyl acetate of a crystalline melting point of 85 to 103°C with the proviso that the content of said copolymer(II) in the total amount of copolymers in both the outermost layers is less than 65 % by weight and having an adhesive layer between the center layer and the outermost layer.
2. A laminate film according to claim 1, wherein said copolymer(I) of vinylidene chloride comprises 65 to 95 % by weight of vinylidene chloride and 35 to 5 % by weight of at least one of unsaturated monomers copolymerizable with vinylidene chloride.
3. A laminate film according to claim 1, wherein said copolymer(II) of ethylene and alpha-olefin is a copolymer of ethylene and one or more alpha-olefins selected from the group consisting of butene-l, pentene-l, 4-methylpentene-1, hexene-l and octene-l.
4. A laminate film according to claim 1, wherein said copolymer(III) of ethylene and vinyl acetate falls in the pentagonal range defined in Fig. 1 by linear lines respectively connecting the respective points of (W-I), (W-II), (X-II), (Z-III) and (Z-I).
5. A laminate film according to claim 1, wherein said adhesive layer comprises a polymer or a mixture of polymers selected from the group consisting of polyethylene modified by a carboxylic acid, a copolymer of ethylene and vinyl acetate.
6. A laminate film according to claim 1 or claim 5 wherein the thickness of said adhesive layer is in the range of 1 to 3 microns.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55153450A JPS5775856A (en) | 1980-10-31 | 1980-10-31 | Laminated film |
| JP153450/1980 | 1980-10-31 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1170159A true CA1170159A (en) | 1984-07-03 |
Family
ID=15562812
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000388676A Expired CA1170159A (en) | 1980-10-31 | 1981-10-26 | Laminate film |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US4456646A (en) |
| EP (1) | EP0051480B2 (en) |
| JP (1) | JPS5775856A (en) |
| KR (1) | KR860000648B1 (en) |
| AU (1) | AU544001B2 (en) |
| CA (1) | CA1170159A (en) |
| DE (1) | DE3168538D1 (en) |
| ZA (1) | ZA817295B (en) |
Families Citing this family (38)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4457960A (en) * | 1982-04-26 | 1984-07-03 | American Can Company | Polymeric and film structure for use in shrink bags |
| US5209972A (en) * | 1983-05-04 | 1993-05-11 | Super Scott S | Multiple layer packaging film |
| CA1245144A (en) * | 1983-06-27 | 1988-11-22 | William Z. Snow | Polyolefin film having mineral oil resistant surface layer |
| US4615922A (en) * | 1983-10-14 | 1986-10-07 | American Can Company | Oriented polymeric film |
| JPS60120050A (en) * | 1983-12-02 | 1985-06-27 | 呉羽化学工業株式会社 | Heat-shrinkable cylindrical laminated film |
| US4997690A (en) * | 1984-12-03 | 1991-03-05 | Viskase Corporation | Irradiated multilayer film for primal meat packaging |
| US4640856A (en) * | 1985-04-29 | 1987-02-03 | W. R. Grace & Co., Cryovac Div. | Multi-layer packaging film and receptacles made therefrom |
| US4894107A (en) * | 1985-05-16 | 1990-01-16 | American National Can Company | Process for making multiple layer polymeric films |
| US7052753B1 (en) | 1985-05-16 | 2006-05-30 | Pechiney Emballage Flexible Europe | Multiple layer polymeric films and process for making them |
| US4770731A (en) * | 1985-06-03 | 1988-09-13 | W. R. Grace & Co.-Conn. | Method of making a patch for a shrinkable bag |
| US5059481A (en) * | 1985-06-17 | 1991-10-22 | Viskase Corporation | Biaxially stretched, heat shrinkable VLDPE film |
| CA1340037C (en) * | 1985-06-17 | 1998-09-08 | Stanley Lustig | Puncture resistant, heat-shrinkable films containing very low density polyethylene copolymer |
| US5256351A (en) * | 1985-06-17 | 1993-10-26 | Viskase Corporation | Process for making biaxially stretched, heat shrinkable VLDPE films |
| US4976898A (en) * | 1985-06-17 | 1990-12-11 | Viskase Corporation | Process for making puncture resistant, heat-shrinkable films containing very low density polyethylene |
| USRE35285E (en) * | 1985-09-30 | 1996-06-25 | W. R. Grace & Co.-Conn. | Thermoplastic multi-layer packaging film and bags made therefrom |
| NZ217626A (en) * | 1985-09-30 | 1989-11-28 | W R Grace & Co Conn Formerly W | Packaging film consisting of #a# olefin copolymers |
| US4910085A (en) * | 1985-11-29 | 1990-03-20 | American National Can Company | Multiple layer packaging films and packages formed thereof |
| JPS62273849A (en) * | 1986-05-23 | 1987-11-27 | 呉羽化学工業株式会社 | Heat-shrinkable composite film and manufacture thereof |
| US4755436A (en) * | 1986-06-30 | 1988-07-05 | W. R. Grace & Co., Cryovac Div. | Inter-ply adhesion between saran and linear ethylene copolymers |
| US4842952A (en) * | 1986-06-30 | 1989-06-27 | W. R. Grace & Co.-Conn. | Inter-ply adhesion between saran and linear ethylene copolymers |
| US4909881A (en) * | 1986-06-30 | 1990-03-20 | W. R. Grace And Co.-Conn. | Bonding method effecting inter-ply adhesion between saran and linear ethylene copolymers |
| US4828891A (en) * | 1987-02-02 | 1989-05-09 | Viskase Corporation | Four-layer puncture resistant film |
| US4863784C1 (en) * | 1987-05-28 | 2001-05-01 | Bt Commercial Corp | Multilayer film containing very low density polyethylene |
| US4988465A (en) * | 1987-05-28 | 1991-01-29 | Viskase Corporation | Manufacture of multilayer film containing very low density polyethylene |
| DE3814942A1 (en) * | 1988-05-03 | 1989-11-16 | Hoechst Ag | HOT-SEALANT SHRINK FILM BASED ON POLYPROPYLENE, METHOD FOR THE PRODUCTION THEREOF, AND ITS USE IN FOAM PACKAGING LABELS |
| US5075143A (en) * | 1989-09-29 | 1991-12-24 | W. R. Grace & Co.-Conn. | High barrier implosion resistant films |
| NZ242460A (en) | 1991-05-02 | 1995-05-26 | Grace W R & Co | Multilayer biaxially heat-shrinkable patch comprising two outer polymeric layers and an inner foam polymer layer |
| EP0597502B1 (en) * | 1992-11-13 | 2005-03-16 | Cryovac, Inc. | Heat shrinkable films containing single site catalyzed copolymers |
| DE69426273T3 (en) * | 1993-01-29 | 2009-03-26 | Pechiney Plastic Packaging, Inc. (n.d.Ges.d. Staates Delaware), Chicago | Tough, heat-shrinkable multilayer film |
| CA2104719C (en) * | 1993-04-21 | 2005-12-27 | Gregory Kenneth Williams | Method of making a shrinkable bag with a protective patch |
| CA2125999C (en) * | 1993-07-12 | 1998-09-22 | Paul Nick Georgelos | Puncture resistant heat shrinkable film containing narrow molecular weight ethylene alpha olefin |
| US5397613A (en) * | 1993-07-12 | 1995-03-14 | Viskase Corporation | Puncture resistant heat shrinkable film containing narrow molecular weight ethylene alpha olefin |
| US6287613B1 (en) | 1994-12-12 | 2001-09-11 | Cryovac Inc | Patch bag comprising homogeneous ethylene/alpha-olefin copolymer |
| EP0954439B1 (en) | 1997-01-21 | 2004-03-24 | Cryovac, Inc. | Packaging film and containers made therefrom |
| US6663905B1 (en) | 1998-03-16 | 2003-12-16 | Cryovac, Inc. | Patch bag having wrap-around patch |
| AU770179B2 (en) * | 1998-12-03 | 2004-02-12 | Flexopack Sa | Multilayer heat shrinkable film |
| US7147930B2 (en) * | 2003-12-16 | 2006-12-12 | Curwood, Inc. | Heat-shrinkable packaging films with improved sealing properties and articles made thereof |
| WO2025079030A1 (en) * | 2023-10-13 | 2025-04-17 | Nusens Ip, Inc. | Temporary containment barriers and related methods |
Family Cites Families (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3524795A (en) * | 1965-07-01 | 1970-08-18 | Dow Chemical Co | Packaging film |
| US3673050A (en) * | 1970-02-05 | 1972-06-27 | Dow Chemical Co | A laminate of a barrier layer enclosed in rigid high density polyolefin layers |
| GB1385196A (en) * | 1971-06-23 | 1975-02-26 | Grace W R & Co | Process for the production of laminates |
| CA982923A (en) * | 1972-09-11 | 1976-02-03 | Union Carbide Corporation | Film and bag for packaging primal meat cuts |
| US4096946A (en) * | 1974-09-16 | 1978-06-27 | E.S. & A. Robinson (Canada) Ltd. | Laminate for use in packing oil |
| JPS5267842A (en) * | 1975-12-02 | 1977-06-04 | Matsushita Electric Ind Co Ltd | High frequency heater |
| JPS5382888A (en) * | 1976-12-29 | 1978-07-21 | Kureha Chem Ind Co Ltd | Co-extruded five-layered drawn cylindrical film and its manufacture |
| JPS5391890A (en) * | 1977-01-24 | 1978-08-12 | Kureha Chemical Ind Co Ltd | Method of producing skin package |
| JPS543179A (en) * | 1977-06-10 | 1979-01-11 | Asahi Chem Ind Co Ltd | Heat-shrinkable laminate film |
| JPS5480374A (en) * | 1977-12-09 | 1979-06-27 | Mitsubishi Plastics Ind Ltd | Production of monoaxially oriented polyolefin film |
| US4178401A (en) * | 1978-01-09 | 1979-12-11 | W. R. Grace & Co. | Packaging film comprising a blended self-welding layer |
| US4278738A (en) * | 1978-03-10 | 1981-07-14 | W. R. Grace & Co. | Ethylene-vinyl acetate copolymer film laminate |
| US4228215A (en) * | 1978-06-30 | 1980-10-14 | American Can Company | Laminate including fluid compression rolled polymer |
| JPS5739957A (en) * | 1980-08-21 | 1982-03-05 | Kureha Chemical Ind Co Ltd | Thermal contractive laminated film |
| JPS56139544U (en) * | 1980-03-19 | 1981-10-22 | ||
| US4357376A (en) * | 1981-07-06 | 1982-11-02 | Union Carbide Corporation | Multilayer film for primal meat packaging |
-
1980
- 1980-10-31 JP JP55153450A patent/JPS5775856A/en active Granted
-
1981
- 1981-10-21 US US06/313,622 patent/US4456646A/en not_active Expired - Fee Related
- 1981-10-21 ZA ZA817295A patent/ZA817295B/en unknown
- 1981-10-26 CA CA000388676A patent/CA1170159A/en not_active Expired
- 1981-10-29 AU AU76947/81A patent/AU544001B2/en not_active Ceased
- 1981-10-30 EP EP81305200A patent/EP0051480B2/en not_active Expired
- 1981-10-30 DE DE8181305200T patent/DE3168538D1/en not_active Expired
- 1981-10-30 KR KR1019810004169A patent/KR860000648B1/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| KR860000648B1 (en) | 1986-05-28 |
| EP0051480B1 (en) | 1985-01-23 |
| EP0051480B2 (en) | 1988-07-13 |
| EP0051480A1 (en) | 1982-05-12 |
| JPS5775856A (en) | 1982-05-12 |
| KR830007253A (en) | 1983-10-19 |
| JPS64216B2 (en) | 1989-01-05 |
| US4456646A (en) | 1984-06-26 |
| AU7694781A (en) | 1982-05-06 |
| AU544001B2 (en) | 1985-05-16 |
| ZA817295B (en) | 1982-09-29 |
| DE3168538D1 (en) | 1985-03-07 |
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Legal Events
| Date | Code | Title | Description |
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| MKEX | Expiry |