WO2013008780A1 - プラスチックフィルム及び輸液バッグ - Google Patents
プラスチックフィルム及び輸液バッグ Download PDFInfo
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- WO2013008780A1 WO2013008780A1 PCT/JP2012/067465 JP2012067465W WO2013008780A1 WO 2013008780 A1 WO2013008780 A1 WO 2013008780A1 JP 2012067465 W JP2012067465 W JP 2012067465W WO 2013008780 A1 WO2013008780 A1 WO 2013008780A1
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- outer layer
- density polyethylene
- plastic film
- mass
- intermediate layer
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- 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
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- 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
- B32B27/302—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers comprising aromatic vinyl (co)polymers, e.g. styrenic (co)polymers
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- 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
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- 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
- B32B27/327—Layered products comprising a layer of synthetic resin comprising polyolefins comprising polyolefins obtained by a metallocene or single-site catalyst
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- B32B27/36—Layered products comprising a layer of synthetic resin comprising polyesters
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- 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
- B32B7/02—Physical, chemical or physicochemical properties
- B32B7/027—Thermal properties
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D25/00—Details of other kinds or types of rigid or semi-rigid containers
- B65D25/38—Devices for discharging contents
- B65D25/40—Nozzles or spouts
- B65D25/42—Integral or attached nozzles or spouts
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D33/00—Details of, or accessories for, sacks or bags
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- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61J—CONTAINERS SPECIALLY ADAPTED FOR MEDICAL OR PHARMACEUTICAL PURPOSES; DEVICES OR METHODS SPECIALLY ADAPTED FOR BRINGING PHARMACEUTICAL PRODUCTS INTO PARTICULAR PHYSICAL OR ADMINISTERING FORMS; DEVICES FOR ADMINISTERING FOOD OR MEDICINES ORALLY; BABY COMFORTERS; DEVICES FOR RECEIVING SPITTLE
- A61J1/00—Containers specially adapted for medical or pharmaceutical purposes
- A61J1/05—Containers specially adapted for medical or pharmaceutical purposes for collecting, storing or administering blood, plasma or medical fluids ; Infusion or perfusion containers
- A61J1/10—Bag-type containers
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61J—CONTAINERS SPECIALLY ADAPTED FOR MEDICAL OR PHARMACEUTICAL PURPOSES; DEVICES OR METHODS SPECIALLY ADAPTED FOR BRINGING PHARMACEUTICAL PRODUCTS INTO PARTICULAR PHYSICAL OR ADMINISTERING FORMS; DEVICES FOR ADMINISTERING FOOD OR MEDICINES ORALLY; BABY COMFORTERS; DEVICES FOR RECEIVING SPITTLE
- A61J1/00—Containers specially adapted for medical or pharmaceutical purposes
- A61J1/14—Details; Accessories therefor
- A61J1/1468—Containers characterised by specific material properties
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/001—Combinations of extrusion moulding with other shaping operations
- B29C48/0017—Combinations of extrusion moulding with other shaping operations combined with blow-moulding or thermoforming
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- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/07—Flat, e.g. panels
- B29C48/08—Flat, e.g. panels flexible, e.g. films
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/09—Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
- B29C48/10—Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels flexible, e.g. blown foils
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/16—Articles comprising two or more components, e.g. co-extruded layers
- B29C48/18—Articles comprising two or more components, e.g. co-extruded layers the components being layers
- B29C48/21—Articles comprising two or more components, e.g. co-extruded layers the components being layers the layers being joined at their surfaces
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
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- B29C49/00—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
- B29C49/02—Combined blow-moulding and manufacture of the preform or the parison
- B29C49/04—Extrusion blow-moulding
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
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- B29C49/00—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
- B29C49/02—Combined blow-moulding and manufacture of the preform or the parison
- B29C49/06905—Using combined techniques for making the preform
- B29C49/0691—Using combined techniques for making the preform using sheet like material, e.g. sheet blow-moulding from joined sheets
- B29C49/06914—Using combined techniques for making the preform using sheet like material, e.g. sheet blow-moulding from joined sheets using parallel sheets as a preform
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C49/00—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
- B29C49/22—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor using multilayered preforms or parisons
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- 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
- Y10T428/13—Hollow or container type article [e.g., tube, vase, etc.]
- Y10T428/1334—Nonself-supporting tubular film or bag [e.g., pouch, envelope, packet, etc.]
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- 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
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- 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
- Y10T428/24992—Density or compression of components
Definitions
- the present invention relates to a plastic film used for a medical container and an infusion bag using the same.
- the film used for soft bags is composed entirely of polyolefin materials such as polyethylene and polypropylene in order to reduce eluate during steam sterilization under high pressure and to maintain transparency and flexibility.
- polyolefin materials such as polyethylene and polypropylene
- polyolefin materials are easily melted by external heating, they are liable to cause quality deterioration such as transparency being lowered by external heating, film thickness being reduced, and wrinkles being formed.
- the bag-making process by external heating, such as heat sealing is performed by carefully melting the polyolefin material partly over time so as not to deteriorate the film.
- U.S. Patent No. 6,057,031 discloses a first outer layer comprising an ethylene / ⁇ -olefin copolymer having a density less than 0.916 g / cc and a melt peak temperature greater than 118 ° C, and a polyester, copolyester (polyester copolymer).
- Patent Document 1 describes that the film is formed by casting coextrusion, and actually describes an example in which a film is manufactured by casting coextrusion using a T die.
- an object of the present invention is to provide a plastic film and an infusion bag in which quality deterioration is suppressed and blocking resistance is excellent.
- the plastic film of one embodiment of the present invention is provided between a first outer layer made of a polyester elastomer, a second outer layer containing high-density polyethylene, and the first outer layer and the second outer layer, A first intermediate layer mainly composed of linear low density polyethylene, and provided between the first outer layer and the first intermediate layer, an ⁇ -olefin and an unsaturated carboxylic acid or unsaturated carboxylic acid; And a second intermediate layer mainly composed of a polymer with an anhydride monomer, and formed by coextrusion.
- the polyester elastomer of the first outer layer is preferably an alicyclic polyester.
- the first intermediate layer preferably contains 40% by mass or less of high-density polyethylene.
- the second outer layer is a mixture of high-density polyethylene and linear low-density polyethylene, and the content of linear low-density polyethylene is preferably 50% by mass or less.
- the second outer layer is preferably a mixture of 20 to 40% by mass of high density polyethylene, 10 to 30% by mass of linear low density polyethylene, and 70 to 30% by mass of low density polyethylene.
- the infusion bag of one embodiment of the present invention includes a bag body made of the plastic film, and a spout is provided in the bag body.
- the quality deterioration of the plastic film can be suppressed and the blocking resistance can be improved.
- plastic film A plastic film according to an embodiment of the present invention will be described below with reference to FIG.
- middle layer 14, and the 2nd outer layer 16 are laminated
- the first outer layer 10 is a layer that becomes the outermost layer of the container when the plastic film 1 is made into a bag-like container, and has the highest temperature when the plastic film 1 is subjected to external heating in the heat sealing process. It is a layer. In the heat sealing process, the plastic film 1 is welded together, or the plastic film 1 and a port or tube made of a synthetic resin molded product that is a chemical discharge outlet member are formed on the second outer layer 16 of the plastic film 1. Or welding.
- the first outer layer 10 is made of a polyester elastomer.
- the polyester elastomer is a polyester-based thermoplastic elastomer composed of a unit derived from a dibasic acid and a unit derived from a dihydric alcohol, and is a polyester ether block copolymer having a hard segment and a soft segment.
- polyester ether examples include those described in the Encyclopedia of Polymer Science and Engineering (The Encyclopedia of Polymer Science and Engineering, 2nd edition, Volume 12, pages 75 to 115, published in 1985).
- dibasic acid used in the polyester elastomer examples include aromatic or aliphatic dicarboxylic acids or dimethyl esters thereof.
- aromatic dicarboxylic acids such as terephthalic acid, isophthalic acid, naphthalene-2,6-dicarboxylic acid, anthracene dicarboxylic acid, diphenyl-4,4′-dicarboxylic acid, diphenoxyethanedicarboxylic acid and 4,4′-diphenyl ether dicarboxylic acid Acid, 1,4-cyclohexanedicarboxylic acid, cyclopentanedicarboxylic acid and alicyclic dicarboxylic acid such as 4,4′-dicyclohexyldicarboxylic acid, adipic acid, succinic acid, oxalic acid, sebacic acid, dodecanedioic acid, dimer acid, etc.
- aliphatic dicarboxylic acids such as 4,4′-dicyclohe
- dihydric alcohol used in the polyester elastomer examples include aliphatic diols such as ethylene glycol, trimethylene glycol, 1,4-butanediol, pentamethylene glycol, hexamethylene glycol, neopentyl glycol, decamethylene glycol, 1,1- Cyclohexanedimethanol, 1,4-dicyclohexanedimethanol, tricyclodecane dimethanol and other alicyclic diols, xylylene glycol, bis (p-hydroxy) diphenyl, bis (p-hydroxy) diphenylpropane and other aromatic diols , Poly (ethylene oxide), poly (propylene oxide), poly (tetramethylene oxide) and poly (alkylene glycol ethers) such as copolymers thereof.
- aliphatic diols such as ethylene glycol, trimethylene glycol, 1,4-butanediol, pentamethylene glycol, hexamethylene glycol,
- polyester elastomers containing units derived from aromatic compounds having an aromatic ring are the standards for dissolution tests in the Japanese Pharmacopoeia required when used in medical containers. In some cases, it does not satisfy the standard value of the ultraviolet absorption spectrum. For this reason, as a polyester elastomer, the polyester elastomer which does not contain an aromatic compound is preferable. Furthermore, since it does not contain an aromatic compound and has high heat resistance, it is preferably an alicyclic polyester that is a polyester elastomer containing units derived from an alicyclic compound.
- alicyclic polyesters composed of 1,4-cyclohexanedicarboxylic acid, 1,4-dicyclohexanedimethanol and poly (alkylene glycol ether) containing a large amount of alicyclic compounds are more preferable.
- polyester elastomer A conventionally well-known manufacturing method is mentioned.
- polyester elastomers include Hytrel 4767 (trade name, manufactured by Toray DuPont Co., Ltd.) containing units derived from aromatic compounds, and Ecdel 9966 (trade name, manufactured by Eastman Corp.), which is an alicyclic polyester. ) And the like.
- the thickness t1 of the first outer layer 10 is preferably 2 to 15%, more preferably 2 to 10%, and even more preferably 2 to 8% with respect to the thickness (total thickness) T of the plastic film 1. If the thickness t1 is less than the above lower limit value, the buffering effect of heat damage to the plastic film 1 due to heat transfer by external heating may be reduced, resulting in quality deterioration. If the thickness t1 is more than the upper limit, the rigidity of the plastic film 1 is remarkably increased, and flexibility as a medical container may be impaired.
- the second intermediate layer 12 is a layer adjacent to the first outer layer 10 and is an interlayer adhesive layer between the first outer layer 10 and a first intermediate layer 14 described later.
- the second intermediate layer 12 is a polymer of an ⁇ -olefin and an unsaturated carboxylic acid, or a polymer of an ⁇ -olefin and an unsaturated monomer of an unsaturated dicarboxylic acid (hereinafter sometimes referred to as a polymer A in general).
- the main component is a modified polyolefin comprising
- ⁇ -Olefin includes ethylene, propylene and the like.
- Polyolefin which is a homopolymer such as ethylene or propylene or a copolymer of ethylene and propylene, is a catalyst system (Ziegler catalyst) obtained from a transition metal compound and an organoaluminum compound, and a compound of chromium on a carrier (eg, silica). It is obtained by homopolymerizing or copolymerizing an olefin using a catalyst system (Phillips catalyst) obtained by supporting (for example, chromium oxide) or a radical initiator (for example, organic peroxide).
- the unsaturated carboxylic acid or unsaturated dicarboxylic acid anhydride monomer is an unsaturated monomer having at least one double bond, and contains at least one carboxyl group or an anhydride (group) thereof.
- anhydride monomers of unsaturated carboxylic acid or unsaturated dicarboxylic acid (meth) acrylic acid, maleic acid, itaconic acid, citraconic acid, endic acid, maleic anhydride, itaconic anhydride, endic acid anhydride, citraconic anhydride An acid etc. are mentioned.
- the polymer A used for the second intermediate layer 12 is a graft polymer obtained by graft polymerization of an unsaturated monomer to polyolefin.
- the polyolefin used for the polymer A is preferably an ethylene homopolymer or a copolymer of ethylene and propylene because of excellent adhesion. Since it is excellent in transparency in addition to adhesiveness, an olefin-based thermoplastic elastomer that is a copolymer of ethylene and propylene, particularly a copolymer of ethylene and propylene, is more preferable.
- polymer A a commercially available product may be used.
- examples of commercially available products of the polymer A include Modic (trade name, manufactured by Mitsubishi Chemical Corporation), Zelas (trade name, manufactured by Mitsubishi Chemical Corporation), Admer (trade name, manufactured by Mitsui Chemicals, Inc.), and the like. .
- the content of the polymer A in the resin constituting the second intermediate layer 12 is more than 50% by mass, preferably 75% by mass or more, and more preferably 100% by mass. The greater the content of the polymer A, the stronger the first outer layer 10 and the first intermediate layer 14 can be bonded.
- the second intermediate layer 12 can contain a resin other than the polymer A as long as the adhesive strength is not impaired.
- the resin other than the polymer A contained in the second intermediate layer 12 include polyethylene and polypropylene.
- the thickness t2 of the second intermediate layer 12 is preferably 2 to 15%, more preferably 2 to 10% with respect to the total thickness T. If the thickness t2 is less than the above lower limit value, the adhesion with the first outer layer 10 may be insufficient. If the thickness t2 exceeds the above upper limit, the strength physical properties of the plastic film 1 may be impaired, or the manufacturing cost may be unnecessarily increased.
- the first intermediate layer 14 is a layer mainly composed of linear low density polyethylene.
- the linear low density polyethylene is a polymer of ethylene and one or more ⁇ -olefins selected from ⁇ -olefins having 3 to 20 carbon atoms.
- ⁇ -olefins having 3 to 20 carbon atoms ⁇ -olefins having 3 to 12 carbon atoms are preferable, for example, propylene, 1-butene, 1-pentene, 4-methyl 1-pentene, 1-hexene, 1 -Octene, 1-decene, 1-dodecene and the like.
- propylene, 1-butene, 1-hexene and 1-octene are preferable.
- the content of ⁇ -olefin in the linear low density polyethylene is preferably 1 to 30 mol%, more preferably 3 to 20 mol%.
- the density of the linear low density polyethylene is preferably 0.890 to 0.940 g / cm 3 .
- the melt mass flow rate (hereinafter sometimes referred to as MFR) of the linear low density polyethylene is preferably 0.1 to 20 g / 10 min.
- the density is a value measured according to JIS K7112 D method
- MFR is a value measured at a load of 21.18 N and a temperature of 190 ° C. according to JIS K7210 unless otherwise specified. It is.
- the manufacturing method of linear low density polyethylene is not specifically limited, A conventionally well-known manufacturing method is mentioned.
- the linear low density polyethylene is preferably produced using a metallocene catalyst or a Ziegler-Natta catalyst.
- the metallocene linear low density polyethylene manufactured with the metallocene catalyst is more preferable in terms of excellent strength and transparency.
- Commercially available products of linear low density polyethylene include, for example, excelen GMH (trade name, manufactured by Sumitomo Chemical Co., Ltd.), Evolue (trade name, manufactured by Prime Polymer Co., Ltd.), Kernel, Harmo, which are metallocene linear low density polyethylene.
- Rex (trade name, manufactured by Nippon Polyethylene Co., Ltd.) and the like.
- the content of the linear low density polyethylene in the resin constituting the first intermediate layer 14 is more than 50% by mass, preferably 70% by mass or more, and may be 100% by mass.
- the heat resistance of the plastic film 1 can be further increased.
- the content of the high density polyethylene in this mixture is preferably 5 to 40% by mass, more preferably 5 to 30% by mass.
- heat resistance and appearance can be further improved.
- it exceeds the upper limit transparency and flexibility tend to be lowered.
- the density of the high density polyethylene used for the first intermediate layer 14 is more than 0.940 g / cm 3 .
- the MFR of this high density polyethylene is preferably 0.1 to 10 g / 10 minutes, more preferably 0.5 to 5.0 g / 10 minutes. If the MFR is less than the lower limit, the resin pressure at the time of extrusion molding may increase and the moldability may decrease. When the MFR exceeds the upper limit, bubble stability may be lowered when forming a film by the coextrusion inflation method.
- the molecular weight distribution (Mw / Mn) of the high density polyethylene is preferably 4 or less. When Mw / Mn exceeds 4, the transparency of the plastic film 1 tends to decrease.
- Mw / Mn is a ratio of the weight average molecular weight Mw and the number average molecular weight Mn, which is measured by gel permeation chromatography and calculated using a calibration curve using polystyrene as a standard sample.
- the melting peak temperature (melting point) of the high-density polyethylene is preferably 128 ° C. or higher.
- the upper limit of the melting peak temperature of a high density polyethylene can make an upper limit the melting peak temperature of the high density polyethylene marketed.
- the melting peak temperature of the high-density polyethylene is preferably 128 to 138 ° C, more preferably 130 to 135 ° C. Is done.
- the melting peak temperature was determined by using a differential scanning calorimeter, holding the sample at a temperature about 30 ° C. higher than the approximate melting peak temperature for 10 minutes, then cooling to 30 ° C. at a rate of 10 ° C./min, then 10 ° C. / This is the temperature of the melting peak that appears when the temperature is raised to 30 ° C. higher than the melting peak temperature at a rate of minutes.
- the resin constituting the first intermediate layer 14 may contain a crystal nucleating agent.
- a crystal nucleating agent By containing a crystal nucleating agent, the transparency and heat resistance of the plastic film 1 can be further enhanced.
- Preferable crystal nucleating agents include, for example, a mixture of cyclohexane dicarboxylic acid calcium salt and zinc stearate.
- the content of the crystal nucleating agent in the resin constituting the first intermediate layer 14 is preferably 0.5 to 2.5% by mass. If it is more than the said lower limit, heat resistance and transparency can further be improved. On the other hand, even if the content exceeds the upper limit, the degree of improvement in heat resistance and transparency is low.
- the thickness t3 of the first intermediate layer 14 is preferably 40 to 95%, more preferably 75 to 95%, still more preferably 80 to 95% with respect to the total thickness T. It is because it is excellent in transparency, a softness
- the second outer layer 16 is a layer containing high-density polyethylene, and is a seal layer for welding the plastic films 1 to each other by heat sealing.
- the content of the high-density polyethylene in the resin constituting the second outer layer 16 is preferably 20% by mass or more, more preferably 50% by mass or more, and still more preferably 100% by mass. If it is more than the said lower limit, it will not deform
- the resin constituting the second outer layer 16 may be a mixture of high density polyethylene and linear low density polyethylene.
- the content of the linear low density polyethylene in the resin constituting the second outer layer 16 is preferably 50% by mass or less, more preferably 45% by mass or less, and even more preferably 40% by mass or less from the viewpoint of blocking resistance. . If it exceeds the above upper limit value, heat sealing can be performed at a relatively low temperature or heat sealing can be performed in a short time, but blocking tends to occur between the inner surfaces of the plastic film 1.
- the lower limit of the content of the linear low density polyethylene in the resin constituting the second outer layer 16 is, for example, preferably 10% by mass or more, and more preferably 20% by mass or more. If it is more than the said lower limit, transparency and impact resistance of the plastic film 1 can be improved more.
- the resin constituting the second outer layer 16 is preferably a mixture of 20 to 40% by mass of high density polyethylene, 10 to 30% by mass of low density polyethylene, and 70 to 30% by mass of linear low density polyethylene.
- a mixture of 20 to 30% by mass of polyethylene, 10 to 25% by mass of low density polyethylene, and 70 to 45% by mass of linear low density polyethylene is more preferable.
- the density is preferably 0.910 to 0.930 g / cm 3
- the MFR is preferably 0.1 to 10 g / 10 minutes.
- the resin configuration of the second outer layer 16 is appropriately determined according to the application of the container using the plastic film 1 (for example, the type of contents, the capacity, etc.) and the characteristics required of the container.
- the linear low density polyethylene used for the second outer layer 16 may be the same as the linear low density polyethylene used for the first intermediate layer 14.
- the linear low density polyethylene used for the second outer layer 16 is preferably made of a metallocene catalyst or a Ziegler-Natta catalyst.
- the MFR of the linear low density polyethylene used for the second outer layer 16 is not particularly limited, but is preferably 0.1 to 10 g / 10 minutes, for example.
- the density of the linear low density polyethylene used for the 2nd outer layer 16 is not specifically limited, For example, 0.925 g / cm ⁇ 3 > or less is preferable. If a density is below the said upper limit, transparency and impact resistance of the plastic film 1 can be improved more effectively.
- the melting peak temperature of the second outer layer 16 is not more than the melting peak temperature of the first outer layer 10.
- the difference (melting peak temperature difference) between the melting peak temperature of the first outer layer 10 and the melting peak temperature of the second outer layer 16 is preferably 40 ° C. or higher, and more preferably 50 ° C. or higher.
- the upper limit of the melting peak temperature difference is not particularly limited, but is preferably 100 ° C. or lower. If the difference in melting peak temperature between the first outer layer 10 and the second outer layer 16 is too large, the second outer layer 16 is formed at a high temperature during coextrusion, and the viscosity of the second outer layer 16 is remarkably high. There is a possibility that the film cannot be stably formed.
- the thickness t4 of the second outer layer 16 is preferably 1 to 30%, more preferably 2 to 20%, still more preferably 3 to 15% with respect to the total thickness T. If the thickness t4 is less than the lower limit, the strength physical properties of the plastic film 1 may be impaired. When the thickness t4 exceeds the upper limit, transparency and flexibility may be reduced.
- the total thickness T of the plastic film 1 can be determined in consideration of the use of the plastic film 1 and the like.
- the plastic film 1 is used for an infusion bag, for example, 50 to 1000 ⁇ m is preferable, and 100 to 350 ⁇ m is more preferable. If it is less than the above lower limit, impact resistance, water vapor barrier property, heat resistance at the time of processing such as a heat sealing step and use may be insufficient. If it exceeds the upper limit, transparency and flexibility may be insufficient.
- the total thickness T is more preferably 150 to 300 ⁇ m from the viewpoint of further improving transparency and water vapor barrier properties.
- the manufacturing method of the plastic film 1 is a coextrusion method.
- the co-extrusion method include a method of forming a film into a material shape by a multilayer T-die method, and a method of forming a tube by a multilayer inflation method.
- a method of forming a film into a cylindrical shape by a multilayer inflation method is preferable. This is because by forming the film into a cylindrical shape, the surface that comes into contact with the contents such as the chemical solution when the bag is formed is not exposed to the external environment and can be manufactured more hygienically.
- a water-cooled coextrusion inflation method that can be rapidly cooled and solidified from a molten state is more preferable.
- the infusion bag 100 in FIG. 2 includes a bag body 110 made of a tubular plastic film (tube film).
- a bag body 110 made of a tubular plastic film (tube film).
- one open end of the tube film is heat-sealed in a state where a cylindrical spout 111 is provided to form a first heat-sealed portion 112, and the first heat-sealed portion 112 is
- the infusion storage part 113 is filled with the infusion solution, and the other open end of the tube film is heat sealed to form the second heat seal part 114.
- a hanging hole 115 is punched and formed at substantially the center of the second heat seal portion 114, and rectangular unsealed portions 116 are provided on both sides thereof.
- a rubber stopper 117 for inserting an injection needle is attached to the tip of the spout 111.
- the spout 111 may be a tube.
- the plastic film of the present embodiment has the first outer layer, the second intermediate layer, the first intermediate layer, and the second outer layer laminated in this order. It is difficult to cause quality deterioration due to this, and blocking can be prevented. Since the plastic film of this embodiment can be heat-sealed in a short time without causing quality deterioration due to external heating, it can be made at a high speed. Since the plastic film of this embodiment can be manufactured by a co-extrusion method, there is no fear of elution of an adhesive or the like. In the conventional plastic film, when the sealing layers are opposed to each other and wound up one after another, blocking tends to occur.
- the plastic film of this embodiment is overlapped so that the second outer layers as the seal layers face each other, blocking is unlikely to occur. For this reason, even if it shape
- the plastic film of the present invention is not limited to the above-described embodiment.
- the first outer layer, the second outer layer, the first intermediate layer, or the second intermediate layer each have a single-layer structure, but the present invention is not limited thereto, and each layer is If the function is not impaired, it may be composed of two or more layers.
- a first intermediate layer is provided between the first outer layer and the second outer layer, and a second intermediate layer is provided between the first outer layer and the first intermediate layer.
- a third intermediate layer may be provided between the first intermediate layer and the second intermediate layer.
- the third intermediate layer include a gas barrier layer mainly composed of ethylene-vinyl alcohol copolymer, MXD nylon and the like.
- Heat sealability> In order to investigate the effect of heat seal temperature, heat seal was performed at different temperatures. Using two upper and lower heat seal plates that are laminated so that the seal layers face each other so that the seal layers face each other and heated to different four temperatures (180 ° C., 200 ° C., 220 ° C., 240 ° C.), Heat sealing was performed at a pressure of 0.2 MPa. Moreover, in order to investigate the influence resulting from heat sealing time, it heat-sealed in different time. The heat sealing time was 0.1, 0.3, 0.5, 1.0, 2.0, and 3.0 seconds. The plastic film was heat-sealed at the above different temperatures, and the heat-sealing time was selected in consideration of the state of the seal part.
- the heat-sealed specimen is cut into a strip of 15 mm width and peeled off at a tensile speed of 300 mm / min using a tensile tester in accordance with JIS-K6854-3.
- the heat sealability was evaluated according to the evaluation criteria.
- A There is no quality deterioration on the outer surface of the film and the peel strength is strong. Peel strength is 50 N / 15 mm or more.
- B + There is no quality deterioration of the outer surface, but the peel strength is slightly weak. Peel strength is 30 N / 15 mm or more and less than 50 N / 15 mm.
- B- A slight decrease in thickness is observed on the outer surface, but the peel strength is strong. Peel strength is 50 N / 15 mm or more.
- C + There is no quality deterioration of the outer surface, but the peel strength is weak. Peel strength is less than 30N / 15mm.
- C- A decrease in thickness is observed on the outer surface, and the peel strength is strong.
- Peel strength is 50 N / 15 mm or more.
- D + There is no quality deterioration of the outer surface, but it is not sealed.
- D- The thickness of the outer surface is remarkably reduced and the peel strength is strong. Peel strength is 50 N / 15 mm or more.
- D-- The thickness of the outer surface is remarkably reduced, and the molten film is partially attached to the perforations and the seal plate, and the peel strength is high. Peel strength is 50 N / 15 mm or more.
- the dissolution test was conducted by the strip method and the pouch method.
- ⁇ Preparation of test solution for strip method A part having a uniform thickness of the plastic film of each example was taken so as to have a surface area of the wetted liquid of 1200 cm 2 to form a 20 cm ⁇ 30 cm strip, which was used as a test piece for the strip method.
- the obtained test piece was further cut into a size of 5 cm ⁇ 0.5 cm to obtain fine pieces.
- the fine piece was washed with distilled water and dried. All the dried fine pieces and 200 mL of distilled water were placed in a 300 mL hard glass container, and the hard glass container was sealed and heated at 121 ° C. for 1 hour in a high-pressure steam sterilizer.
- the hard glass container was taken out from the high-pressure steam sterilizer and allowed to stand at room temperature, and this liquid content was used as a test liquid for the strip method.
- foaming, pH, potassium permanganate reducing substance, ultraviolet absorption spectrum, and evaporation residue were measured.
- test solution for pouch method A four-sided seal pouch (30 cm ⁇ 40 cm, seal width: 5 mm) containing 200 mL of distilled water was prepared using the plastic film of each example so that the surface area of the liquid contact was 1200 cm 2 .
- the four-sided seal pouch was heated at 121 ° C. for 1 hour in a high-pressure steam sterilizer. After heating, the four-sided seal pouch was taken out from the high-pressure steam sterilizer and allowed to stand at room temperature, and the content solution was used as a test solution for the pouch method.
- foaming, pH, potassium permanganate reducing substance, ultraviolet absorption spectrum, and evaporation residue were measured.
- UV absorption spectrum With respect to the test solution for the strip method or the pouch method, the maximum absorbance was measured in each of a wavelength range of 220 to 240 nm and a wavelength range of 241 to 350 nm by ultraviolet visible absorbance measurement using distilled water as a control.
- the plastic film of each example was cut into a size of 20 cm ⁇ 15 cm, and two sheets were stacked so that the second outer layers faced each other, and heat sealed with a seal width of 5 mm to prepare a three-side sealed bag.
- the three-side sealed bag was filled with 500 mL of distilled water, and the opening was heat sealed.
- the sealed bag was autoclaved at 121 ° C. for 30 minutes. Thereafter, it was quickly opened and distilled water was discharged, and the condition was adjusted for 24 hours in an environment of 23 ° C. and 50% RH.
- haze was measured according to JIS-K6714.
- This post-sterilization blocking test 1 is a normal blocking test in which the ratio between the bag capacity and the amount of contents is in a quantitative relationship under normal use conditions.
- Blocking test 2 after sterilization> The plastic film of each example was cut out to 10 cm ⁇ 10 cm, and two sheets were stacked so that the second outer layers face each other, and heat-sealed with a seal width of 5 mm to prepare a three-side sealed bag.
- This three-side sealed bag was filled with 50 mL of distilled water, and the opening was heat sealed.
- the sealed bag was sterilized under high pressure steam under conditions of 121 ° C. and 30 minutes so that part of the inner surface of the bag was in close contact. Thereafter, the degree of blocking when quickly opened was determined based on the same criteria as the blocking test 1 after sterilization.
- Blocking test 2 after sterilization is a harsh condition in which blocking is likely to occur in that the amount of contents is smaller than that of blocking test 1 after sterilization and high-pressure steam sterilization is performed so that the bag inner surface is partially adhered. .
- each type of tubular plastic film was formed using a four-kind, four-layer, water-cooled coextrusion inflation film forming machine.
- the obtained plastic film was evaluated for heat sealability, pharmacopoeia dissolution test, haze, wrinkle presence, blocking presence, and bag drop strength by bag drop test.
- the plastic film has a first outer layer thickness of 10 ⁇ m, a second intermediate layer thickness of 10 ⁇ m, a first intermediate layer thickness of 130 ⁇ m, and a second outer layer thickness of 10 ⁇ m.
- Examples 1 to 8 to which the present invention is applied all have a heat seal temperature of 200 ° C. or higher, the heat sealability is “A”, and normal use conditions (blocking test 1 after sterilization) ) Did not cause blocking. Further, Examples 1 to 7 showed no blocking even under severe conditions (blocking test 2 after sterilization) in which blocking was likely to occur, and were extremely excellent in blocking resistance. In Examples 1 to 7, although 1 to 2 bags were broken in the bag drop test, there is no problem in normal use.
- Example 1 in which PET1 was used for the first outer layer and Example 2 in which PET2 was used for the first outer layer were both compatible with the dissolution test by the pouch method in the Japanese Pharmacopoeia dissolution test. However, Example 2 could not be adapted to the dissolution test by the strip method with higher load.
- Example 3 and Example 4 in which LLD1 was added to the second outer layer it was found that as the amount of LLD1 added increased, the peel strength became stronger even at low temperature for a short time.
- Example 6 using Ziegler-based linear low density polyethylene for the first intermediate layer was found to have higher haze and lower transparency than Example 1 using metallocene-based linear low density polyethylene. It was.
- Example 8 using modified polyethylene for the second intermediate layer was found to have higher haze and lower transparency than Example 1 using modified olefin elastomer. In Example 8, no blocking was observed in the blocking test 1 after sterilization, but partial adhesion between the bag inner surfaces was observed in the blocking test 2 after sterilization. However, there was no broken bag in the bag drop test, and the bag drop strength was excellent and the impact resistance was excellent.
- Comparative Example 1 using HD for the first outer layer and the second outer layer was remarkably inferior in haze and heat sealability.
- Comparative Example 2 which did not contain HD in the second outer layer and used LLD2 was in the state of a tube-shaped plastic film before heat sterilization and there was no blocking, but it was broken during heat sterilization at 121 ° C. could not withstand sterilization.
- Comparative Example 3 using LLD1 without HD in the second outer layer is in the state of a tube-shaped plastic film before heat sterilization, has blocking, and is broken during heat sterilization at 121 ° C. I could't stand it. From the above results, it was found that by applying the present invention, quality deterioration can be suppressed and blocking resistance can be improved.
- the quality deterioration of the plastic film can be suppressed and the blocking resistance can be improved.
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Abstract
Description
本願は、2011年7月12日に、日本に出願された特願2011-154050号に基づき優先権を主張し、その内容をここに援用する。
例えば、特許文献1には、0.916g/ccより小さい密度及び118℃より高い溶融ピーク温度を有するエチレン/α-オレフィンコポリマーを含む第1の外部層と、ポリエステル、コポリエステル(ポリエステル共重合体)、ポリアミド及びポリオレフィンから選択されるポリマー材料を含む第2の外部層と、第1の外部層及び/又は第2の外部層の間に設けられたα-オレフィン/不飽和モノマーコポリマーを含む層とを備えるフィルムが開示されている。また、特許文献1には、前記フィルムを流延共押出によって成形することが記載され、実際、Tダイを用いた流延共押出成形によりフィルムを製造した例が記載されている。
ブロッキングしたチューブ状フィルムの内面同士を引き離すと、内面が白化しやすい。
加えて、上記のチューブ状フィルムを製袋し、袋内に内容物を充填しようとすると、袋が開口せず、内容物を充填できないことがある。
さらに、内容物を袋内に充填した後、熱滅菌すると、袋の内面同士が部分的に溶着し、剥がせないことがある。
このように、特許文献1に開示される技術は、外部加熱による品質劣化の軽減対策がなされているものの、耐ブロッキング性に劣るという問題があった。
そこで、本発明は、品質劣化が抑制され、かつ耐ブロッキング性に優れるプラスチックフィルム及び輸液バッグを提供することを目的とする。
前記第一の外層のポリエステルエラストマーは、脂環式ポリエステルであることが好ましい。前記第一の中間層は、高密度ポリエチレンを40質量%以下含有することが好ましい。前記第二の外層は、高密度ポリエチレンと線状低密度ポリエチレンとの混合物であり、線状低密度ポリエチレンの含有量が50質量%以下であることが好ましい。前記第二の外層は、高密度ポリエチレン20~40質量%と、線状低密度ポリエチレン10~30質量%と、低密度ポリエチレン70~30質量%との混合物であることが好ましい。
本発明の一実施形態にかかるプラスチックフィルムについて、以下に図1を参照して説明する。図1のプラスチックフィルム1においては、第一の外層10と、第二の中間層12と、第一の中間層14と、第二の外層16とがこの順で積層される。
第一の外層10は、プラスチックフィルム1を袋状の容器にした際に、容器の最外層となる層であり、プラスチックフィルム1がヒートシール工程での外部加熱を施された際に最も高温となる層である。なお、ヒートシール工程では、プラスチックフィルム1同士を溶着したり、プラスチックフィルム1と、薬液の排出注入口部材である合成樹脂成形品からなるポートやチューブとをプラスチックフィルム1の第二の外層16に溶着したりする。
ポリエステルエラストマーの市販品としては、例えば、芳香族系化合物に由来する単位を含むハイトレル4767(商品名、東レ・デュポン株式会社製)、脂環式ポリエステルであるエクデル9966(商品名、イーストマン社製)等が挙げられる。
第二の中間層12は、第一の外層10に隣接する層であり、第一の外層10と後述の第一の中間層14との層間接着層である。
第二の中間層12は、α-オレフィンと不飽和カルボン酸との重合体、又はα-オレフィンと不飽和ジカルボン酸の無水物モノマーとの重合体(以下、総じて重合体Aということがある)からなる変性ポリオレフィンを主成分とする。
重合体Aに用いられるポリオレフィンとしては、接着性に優れることから、エチレンの単独重合体、又はエチレンとプロピレンとの共重合体が好ましい。接着性に加え透明性に優れることから、エチレンとプロピレンとの共重合体、特にエチレンとプロピレンとの共重合体であるオレフィン系熱可塑性エラストマーがより好ましい。
第一の中間層14は、線状低密度ポリエチレンを主成分とする層である。第一の中間層14を設けることで、プラスチックフィルム1の柔軟性を高め、透明性を高く維持できる。
線状低密度ポリエチレンは、エチレンと炭素数3~20のα-オレフィンから選択された1種以上のα-オレフィンとの重合体である。
線状低密度ポリエチレン中のα-オレフィンの含有量は、1~30モル%が好ましく、3~20モル%がより好ましい。
線状低密度ポリエチレンは、メタロセン系触媒又はチーグラー・ナッタ触媒等を用いて製造されたものが好ましい。この中でも、強度、透明性に優れる点で、メタロセン触媒で製造されたメタロセン系線状低密度ポリエチレンが、より好ましい。
線状低密度ポリエチレンの市販品としては、例えば、メタロセン系線状低密度ポリエチレンであるエクセレンGMH(商品名、住友化学株式会社製)、エボリュー(商品名、株式会社プライムポリマー製)、カーネル、ハーモレックス(商品名、日本ポリエチレン株式会社製)等が挙げられる。
この高密度ポリエチレンのMFRは0.1~10g/10分が好ましく、より好ましくは0.5~5.0g/10分である。MFRが上記下限値未満であると、押出成形時の樹脂圧力が上昇し成形性が低下する可能性がある。MFRが上記上限値超であると、共押出インフレーション法で製膜する際、バブル安定性が低下する可能性がある。
融解ピーク温度は、示差走査熱量計を用い、試料をおよその融解ピーク温度より約30℃高い温度で10分間保持した後、10℃/分の速度で30℃まで冷却し、次いで、10℃/分の速度で融解ピーク温度より30℃高い温度まで昇温した際に、現れた融解ピークの温度である。
第一の中間層14を構成する樹脂中の結晶造核剤の含有量は、0.5~2.5質量%が好ましい。上記下限値以上であれば、耐熱性、透明性をさらに高められる。一方、含有量が上記上限値を超えたとしても、耐熱性、透明性の向上の程度は低い。
第二の外層16は、高密度ポリエチレンを含有する層であり、ヒートシールによりプラスチックフィルム1同士を溶着するためのシール層である。
第二の外層16を構成する樹脂中の高密度ポリエチレンの含有量は、20質量%以上が好ましく、50質量%以上がより好ましく、実質的に100質量%がさらに好ましい。上記下限値以上であれば、加熱条件121℃の高圧蒸気殺菌で変形することがない。加えて、高密度ポリエチレンの含有量が多いほど、耐熱性に優れ、耐ブロッキング性に優れる。
なお、本発明における低密度ポリエチレンとは、いわゆる高圧法ポリエチレンである。
密度は0.910~0.930g/cm3が好ましく、MFRは0.1~10g/10分が好ましい。
第二の外層16の樹脂構成は、プラスチックフィルム1を用いた容器の用途(例えば、内容物の種類、容量等)、容器に求められる特性に応じて、適宜決定される。
第二の外層16に用いられる線状低密度ポリエチレンは、メタロセン系触媒又はチーグラー・ナッタ触媒で製造されたものが好ましい。
第二の外層16に用いられる線状低密度ポリエチレンのMFRは、特に限定されないが、例えば、0.1~10g/10分であることが好ましい。
第二の外層16に用いられる線状低密度ポリエチレンの密度は、特に限定されないが、例えば、0.925g/cm3以下が好ましい。密度が上記上限値以下であれば、プラスチックフィルム1の透明性、耐衝撃性をより効果的に高められる。
融解ピーク温度差の上限は、特に限定されないが、100℃以下が好ましい。第一の外層10と第二の外層16との融解ピーク温度差が大きすぎると、共押出時に第二の外層16が高温で製膜されることになり、第二の外層16の粘度が著しく低下して、安定的に製膜できない可能性がある。
プラスチックフィルム1の製造方法は、共押出法である。共押出法としては、例えば、多層Tダイ法により反物状に製膜する方法、多層インフレーション法により筒状に製膜する方法が挙げられる。これらの中でも多層インフレーション法により筒状に製膜する方法が好ましい。筒状に製膜することで、製袋した際に薬液等の内容物と接触する面が、外部環境に露出せず、より衛生的に製造できるためである。プラスチックフィルム1の透明性をさらに高める観点から、溶融状態から急冷固化できる水冷式の共押出インフレーション法がより好ましい。
本発明の一実施形態にかかる輸液バッグについて、以下に図2を参照して説明する。
図2の輸液バッグ100は、チューブ状のプラスチックフィルム(チューブフィルム)からなるバッグ本体110を備える。この輸液バッグ100は、チューブフィルムの一方の開口端を筒状の注出口111を設けた状態でヒートシールして第一のヒートシール部112を形成し、この第一のヒートシール部112を底にして輸液を輸液収納部113に充填し、チューブフィルムの他方の開口端をヒートシールして第二のヒートシール部114を形成することにより、形成される。第二のヒートシール部114の略中央には、吊下孔115が打抜き形成されており、その両側には長方形の未シール部116が設けられている。注出口111の先端には注射針を挿入するゴム栓117が取り付けられている。なお、注出口111はチューブであってもよい。
本実施形態のプラスチックフィルムは、外部加熱による品質劣化を生じることなく、高温かつ短時間でヒートシールできるため、高速で製袋できる。
本実施形態のプラスチックフィルムは、共押出法により製造できるため、接着剤等の溶出の懸念がない。
従来のプラスチックフィルムは、シール層同士を対向させ、重ねて巻き取ると、ブロッキングを生じやすかった。本実施形態のプラスチックフィルムは、シール層である第二の外層同士が対向するように重ねられても、ブロッキングを生じにくい。このため、共押出インフレーション法でチューブ状に成形しても、ブロッキングを生じることのない巻回体として巻き取れる。即ち、本実施形態のプラスチックフィルムは、共押出インフレーション法で製造される場合に、顕著な効果を発揮する。そして、共押出インフレーション法で製造されたプラスチックフィルムは、内容物と接触する面をより衛生的に保てるので、輸液バッグや薬液を収容する容器等に特に好適である。
上述の実施形態では、第一の外層、第二の外層、第一の中間層又は第二の中間層が、それぞれ一層構造とされているが、本発明はこれに限定されず、各層は、その機能が損なわなければ二層以上で構成されていてもよい。
各例の第一の外層、第二の中間層、第一の中間層、第二の外層に用いた樹脂は以下の通りである。
PET1:ポリエステルエラストマー(脂環式ポリエステル)、エクデル 9966(商品名)、融解ピーク温度=205℃、イーストマン社製
PET2:ポリエステルエラストマー(芳香族系化合物に由来する単位を含むポリエステル)、ハイトレル 4767(商品名)、融解ピーク温度=199℃、東レ・デュポン株式会社製
AD1:変性オレフィン系熱可塑性エラストマー、ゼラス MC721AP(商品名)、密度=0.89g/cm3、MFR(JIS K7210に準拠し、加重21.18N、温度230℃で測定した値)=3.5g/10分、融解ピーク温度=155℃、三菱化学株式会社製
AD2:変性ポリエチレン、アドマー NF308(商品名)、密度=0.932g/cm3、MFR=1.7g/10分、融解ピーク温度=125℃、三井化学株式会社製
LLD1:メタロセン系線状低密度ポリエチレン、エボリュー SP0511(商品名)、密度=0.910g/cm3、MFR=1.2g/10分、融解ピーク温度=110℃、株式会社プライムポリマー製
LLD2:チーグラー系線状低密度ポリエチレン、モアテック 3500Z(商品名)、密度=0.921g/cm3、MFR=2g/10分、融解ピーク温度=121℃、株式会社プライムポリマー製
HD:高密度ポリエチレン、密度=0.955g/cm3、MFR=3.5g/10分、融解ピーク温度=132℃、Mw/Mn=3.5
LD:高圧法低密度ポリエチレン、密度=0.927g/cm3、MFR=1g/10分、融解ピーク温度=115℃
LLD1(80質量%)とHD(20質量%)との混合物:融解ピーク温度=125℃
LLD1(20質量%)とHD(80質量%)との混合物:融解ピーク温度=130℃
LLD1(40質量%)とHD(60質量%)との混合物:融解ピーク温度=128℃
LLD2(80質量%)とHD(20質量%)との混合物:融解ピーク温度=127℃
LLD1(60質量%)とHD(20質量%)とLD(20%)との混合物:融解ピーク温度=126℃
<ヒートシール性>
ヒートシール温度による影響を調べるため、異なる温度でヒートシールした。各例のプラスチックフィルム2枚をシール層同士が対向するように重ね合わせ、異なる4点の温度(180℃、200℃、220℃、240℃)に昇温した上下のヒートシール板を用いて、圧力0.2MPaでヒートシールした。また、ヒートシール時間に因る影響を調べるため、異なる時間でヒートシールした。ヒートシール時間を0.1、0.3、0.5、1.0、2.0、3.0秒間とした。
上記の異なる温度でプラスチックフィルムをヒートシールし、シール部の状態を勘案してヒートシール時間を選択した。
A:フィルム外面の品質劣化がなく剥離強度も強い。剥離強度は50N/15mm以上。
B+:外面の品質劣化はないが、剥離強度がやや弱い。剥離強度は30N/15mm以上50N/15mm未満。
B-:外面に厚み減少がわずかにみられるが、剥離強度は強い。剥離強度は50N/15mm以上。
C+:外面の品質劣化はないが、剥離強度が弱い。剥離強度は30N/15mm未満。
C-:外面に厚み減少がみられ、剥離強度が強い。剥離強度は50N/15mm以上。
D+:外面の品質劣化はないが、シールされていない。
D-:外面の厚み減少が著しく、剥離強度が強い。剥離強度は50N/15mm以上。
D--:外面の厚み減少が著しく部分的に穴あきやシール板に溶融フィムが付着しており、剥離強度が強い。剥離強度は50N/15mm以上。
各例のプラスチックフィルムについて、「第十五改正日本薬局方」の一般試験法・プラスチック製医薬品容器試験法に定める溶出試験を行なった。溶出試験の実測値が、表1のポリエチレン製又はポリプロピレン製の水性注射剤容器の規格内であるか否かを判定した。
≪短冊法用の試験液の調製≫
接液の表面積が1200cm2になるように、各例のプラスチックフィルムの厚さが均一な部分を取って20cm×30cmの短冊とし、これを短冊法用の試験片とした。得られた試験片をさらに5cm×0.5cmの大きさに細断して、細断片とした。細断片を蒸留水で洗浄し、乾燥した。乾燥した全ての細断片と蒸留水200mLとを300mLの硬質ガラス製容器に入れ、この硬質ガラス製容器を密栓した後、高圧蒸気滅菌器にて、121℃で1時間加熱した。加熱後、高圧蒸気滅菌器から硬質ガラス製容器を取り出し、室温になるまで放置し、この内容液を短冊法用の試験液とした。短冊法用の試験液を用い、泡立ち、pH、過マンガン酸カリウム還元性物質、紫外線吸収スペクトル、蒸発残留物を測定した。
接液の表面積が1200cm2になるように、各例のプラスチックフィルムを用い、200mLの蒸留水を収容した四方シールパウチ(30cm×40cm、シール幅:5mm)を作製した。この四方シールパウチを高圧蒸気滅菌器にて、121℃で1時間加熱した。加熱後、高圧蒸気滅菌器から四方シールパウチを取り出し、室温になるまで放置し、内容液をパウチ法用の試験液とした。パウチ法用の試験液を用い、泡立ち、pH、過マンガン酸カリウム還元性物質、紫外線吸収スペクトル、蒸発残留物を測定した。
短冊法用又はパウチ法用の試験液、及び蒸留水をそれぞれ20mL採取し、これに1g/L塩化カリウム水溶液を1mL加え、pHを測定した。試験液のpHと蒸留水のpHとの差を算出した。
短冊法用又はパウチ法用の試験液5mLを内径15mm、長さ200mmの共栓試験管に入れ、3分間激しく振り混ぜ、生じた泡が消失するまでの時間を測定した。
短冊法用又はパウチ法用の試験液20mLに、0.002mol/L過マンガン酸カリウム液20mL及び希硫酸1mLを加え、3分間煮沸した後冷却した。冷却後、ヨウ化カリウム0.1gを加えて混合し、10分間放置した。放置後、0.001mol/Lチオ硫酸ナトリウム液で滴定した(指示薬:デンプン試薬)。試験液を蒸留水に換えた以外は同様にして、空試験を行った。試験液と蒸留水(空試験)とに対する0.002mol/L過マンガン酸カリウム液の消費量の差を算出した。
短冊法用又はパウチ法用の試験液について、蒸留水を対照とし、紫外可視吸光度測定法により、波長220~240nmの区間、及び241~350nmの区間のそれぞれで最大吸光度を測定した。
短冊法用又はパウチ法用の試験液をそれぞれ20mL採取し、これを水浴上で蒸発乾固し、残留物を105℃で1時間乾燥し、その質量を測定した。
各例のプラスチックフィルムを20cm×15cmに切り出し、これを第二の外層同士が対向するように2枚重ね合わせ、シール幅5mmでヒートシールして三方シール袋を作製した。この三方シール袋に蒸留水500mLを充填し、開口部をヒートシールして密封した。
密封した袋を、121℃、30分の条件下で、高圧蒸気滅菌をした。その後、速やかに開封して蒸留水を排出し、23℃、50%RHの環境下で、24時間の状態調節を行った。状態調節した袋について、JIS-K6714に準拠してヘイズを測定した。
ヘイズの評価で用いた高圧蒸気滅菌後の三方シール袋の外面上の皺の有無を目視で評価した。
評価は、外面上の皺が全く見られないものを皺が「無」とし、許容範囲ではあるが、若干の皺が見られるものを皺が「有」と判定した。
高圧蒸気滅菌前のブロッキング1種類と、滅菌後のブロッキング2種類との全3種の方法で評価した。
水冷式の共押出インフレーション製膜機で製造された後、押し潰されたチューブ状のプラスチックフィルムの内面部同士が密着している状態から、剥がした時に白化した場合をブロッキング「有」とし、剥がした時に白化しない場合をブロッキング「無」と判定した。
ヘイズの評価で用いた高圧蒸気滅菌後の三方シール袋を開封した際、袋内面同士を完全に離間させることはできるが、少なくとも一部が密着していると見られた場合をブロッキング「有」とし、密着している箇所が全く見られない場合をブロッキング「無」と判定した。この滅菌後ブロッキング試験1は、袋容量と内容物量との比が、通常の使用条件における量的関係にある通常のブロッキング試験である。
各例のプラスチックフィルムを10cm×10cmに切り出し、これを第二の外層同士が対向するように2枚重ね合わせ、シール幅5mmでヒートシールして三方シール袋を作製した。この三方シール袋に蒸留水50mLを充填し、開口部をヒートシールして密封した。
密封した袋を、121℃、30分の条件下で、袋内面の一部が密着するようにして高圧蒸気滅菌をした。その後、速やかに開封した際のブロッキングの程度を、前記滅菌後ブロッキング試験1と同様の基準で判定した。滅菌後ブロッキング試験2は、滅菌後ブロッキング試験1に比べ、内容物量が少量であり、袋内面が一部密着するようにして高圧蒸気滅菌をした点で、ブロッキングが発生しやすい過酷な条件である。
ヘイズの評価用に作製し、高圧蒸気滅菌した袋、10袋を4℃で1日保管した後、2mの高さから、各袋について1回落下させて、破袋した袋の数を数えた。
表2~5の構成に従い、4種4層の水冷式の共押出インフレーション製膜機で、各例のチューブ状のプラスチックフィルムを製膜した。得られたプラスチックフィルムについて、ヒートシール性、薬局方の溶出試験、ヘイズ、皺の有無、ブロッキングの有無及び落袋試験による落袋強度を評価した。各例のプラスチックフィルムは、いずれも第一の外層の厚みが10μm、第二の中間層の厚みが10μm、第一の中間層の厚みが130μm、第二の外層の厚みが10μmである。
なお、比較例2及び3については、高圧蒸気滅菌時に袋が破れ、内容物の蒸留水が流失したため、薬局方に定める溶出試験、ヘイズの評価、皺の有無、滅菌後のブロッキング試験及び落袋試験を行わなかった。
さらに、実施例1~7は、ブロッキングが発生し易い過酷な条件下(滅菌後ブロッキング試験2)でもブロッキングが見られず、耐ブロッキング性に極めて優れていた。なお、実施例1~7は落袋試験で1~2袋の破袋がみられるものの通常の使用において問題となるものではない。
第一の中間層にLLD1とHDとの混合物又はLLD2とHDとの混合物を用いた実施例1~4及び6~8は、高圧蒸気滅菌後に皺が生じなかったのに対し、第一の中間層をLLD1のみで構成した実施例5は、高圧蒸気滅菌後に皺が生じていた。この結果から、第一の中間層を線状低密度ポリエチレンと高密度ポリエチレンとの混合物で構成すると、皺の発生を防止できることが判った。
第一の外層にPET1を用いた実施例1と、第一の外層にPET2を用いた実施例2とは、日本薬局方の溶出試験において、パウチ法での溶出試験に両実施例とも適合したが、より負荷の高い短冊法での溶出試験に実施例2が適合できなかった。
第二の外層にLLD1を添加した実施例3及び実施例4では、LLD1の添加量が増すほど、低温、短時間のヒートシールでも剥離強度が強くなることが判った。
チーグラー系線状低密度ポリエチレンを第一の中間層に用いた実施例6は、メタロセン系線状低密度ポリエチレンを使用した実施例1と比較して、ヘイズが高く、透明性が低いことが判った。
第二の中間層に、変性ポリエチレンを用いた実施例8は、変性オレフィン系エラストマーを用いた実施例1と比較して、ヘイズが高く、透明性が低いことが判った。また、実施例8は、滅菌後ブロッキング試験1でブロッキングが見られなかったが、滅菌後ブロッキング試験2で袋内面同士の一部密着が観察された。ただし、落袋試験で破袋はなく、落袋強度に優れ、耐衝撃性に優れていた。
第二外層にHDを含有せず、LLD2を用いた比較例2は熱滅菌前のチューブ状のプラスチックフィルムの状態で、ブロッキングは無かったが、121℃の熱滅菌時に破袋してしまい、熱滅菌に耐えることができなかった。
第二外層にHDを含有せず、LLD1を用いた比較例3は熱滅菌前のチューブ状のプラスチックフィルムの状態で、ブロッキングが有り、121℃の熱滅菌時に破袋してしまい、熱滅菌に耐えることができなかった。
以上の結果から、本発明を適用することで、品質劣化を抑制し、かつ耐ブロッキング性を向上できることが判った。
10第一の外層
12第二の中間層
14第一の中間層
16第二の外層
100 輸液バッグ
110 バッグ本体
111 注出口
Claims (6)
- ポリエステルエラストマーからなる第一の外層と、
高密度ポリエチレンを含有する第二の外層と、
前記第一の外層と前記第二の外層との間に設けられ、線状低密度ポリエチレンを主成分とする第一の中間層と、
前記第一の外層と前記第一の中間層との間に設けられ、α-オレフィンと、不飽和カルボン酸又は不飽和カルボン酸の無水物モノマーとの重合体を主成分とする第二の中間層とを備え、
共押出法により製膜されるプラスチックフィルム。 - 前記第一の外層のポリエステルエラストマーは、脂環式ポリエステルである請求項1に記載のプラスチックフィルム。
- 前記第一の中間層は、高密度ポリエチレンを40質量%以下含有する請求項1に記載のプラスチックフィルム。
- 前記第二の外層は、高密度ポリエチレンと線状低密度ポリエチレンとの混合物であり、線状低密度ポリエチレンの含有量が50質量%以下である請求項1に記載のプラスチックフィルム。
- 前記第二の外層は、高密度ポリエチレン20~40質量%と、線状低密度ポリエチレン10~30質量%と、低密度ポリエチレン70~30質量%との混合物である請求項1に記載のプラスチックフィルム。
- 請求項1に記載のプラスチックフィルムからなるバッグ本体を備え、前記バック本体に注出口が設けられる輸液バッグ。
Priority Applications (7)
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BR112013033164A BR112013033164A2 (pt) | 2011-07-12 | 2012-07-09 | película de plástico, e, saco para solução de infusão |
KR20137034743A KR20140022439A (ko) | 2011-07-12 | 2012-07-09 | 플라스틱 필름 및 수액 백 |
RU2013158719/05A RU2013158719A (ru) | 2011-07-12 | 2012-07-09 | Полимерная пленка и пакет для инфузионных растворов |
AU2012281624A AU2012281624A1 (en) | 2011-07-12 | 2012-07-09 | Plastic film and infusion solution bag |
US14/127,171 US20140120281A1 (en) | 2011-07-12 | 2012-07-09 | Plastic Film And Infusion Solution Bag |
EP12811379.2A EP2732972A1 (en) | 2011-07-12 | 2012-07-09 | Plastic film and infusion solution bag |
CN201280033472.6A CN103635318A (zh) | 2011-07-12 | 2012-07-09 | 塑料膜及输液袋 |
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JP2011154050A JP5707260B2 (ja) | 2011-07-12 | 2011-07-12 | プラスチックフィルム及び輸液バッグ |
JP2011-154050 | 2011-07-12 |
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JP (1) | JP5707260B2 (ja) |
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CN (1) | CN103635318A (ja) |
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JP6403999B2 (ja) | 2014-06-05 | 2018-10-10 | 株式会社細川洋行 | レトルト包装用積層体及び容器 |
US11905093B2 (en) | 2015-12-02 | 2024-02-20 | Berry Plastics Corporation | Peelable film for container lid |
JP7059648B2 (ja) * | 2018-01-24 | 2022-04-26 | 住友ベークライト株式会社 | 多層シート、トレイ及び包装体 |
JP7274918B2 (ja) * | 2019-04-10 | 2023-05-17 | 株式会社細川洋行 | 容器用多層フィルム及びそれを含む容器 |
WO2024030398A1 (en) * | 2022-08-02 | 2024-02-08 | Repligen Corporation | Enhanced bioprocessing film for single use biocontainers |
CN115556448B (zh) * | 2022-09-08 | 2024-05-24 | 上海乐纯生物技术股份有限公司 | 生物工艺袋用多层膜及其应用 |
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JPH06190990A (ja) * | 1992-10-09 | 1994-07-12 | Otsuka Pharmaceut Factory Inc | 多層フィルム及び容器 |
JP2002524308A (ja) | 1998-09-09 | 2002-08-06 | イーストマン ケミカル カンパニー | エチレンコポリマーの層を含む多層ポリマー構造体 |
JP2010201648A (ja) * | 2009-02-27 | 2010-09-16 | C I Kasei Co Ltd | 多層フィルム及び容器 |
WO2011049031A1 (ja) * | 2009-10-20 | 2011-04-28 | 株式会社細川洋行 | プラスチックフィルム及び輸液バッグ |
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DE60231964D1 (de) * | 2001-01-15 | 2009-05-28 | Hosokawa Yoko Kk | Laminat und behälter |
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2012
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- 2012-07-09 EP EP12811379.2A patent/EP2732972A1/en not_active Withdrawn
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JPH06190990A (ja) * | 1992-10-09 | 1994-07-12 | Otsuka Pharmaceut Factory Inc | 多層フィルム及び容器 |
JP2002524308A (ja) | 1998-09-09 | 2002-08-06 | イーストマン ケミカル カンパニー | エチレンコポリマーの層を含む多層ポリマー構造体 |
JP2010201648A (ja) * | 2009-02-27 | 2010-09-16 | C I Kasei Co Ltd | 多層フィルム及び容器 |
WO2011049031A1 (ja) * | 2009-10-20 | 2011-04-28 | 株式会社細川洋行 | プラスチックフィルム及び輸液バッグ |
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US20140120281A1 (en) | 2014-05-01 |
AU2012281624A1 (en) | 2014-01-09 |
BR112013033164A2 (pt) | 2017-01-31 |
JP2013018211A (ja) | 2013-01-31 |
KR20140022439A (ko) | 2014-02-24 |
JP5707260B2 (ja) | 2015-04-22 |
EP2732972A1 (en) | 2014-05-21 |
RU2013158719A (ru) | 2015-08-20 |
CN103635318A (zh) | 2014-03-12 |
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