WO2017043509A1 - 水溶性フィルム、薬剤包装体及び水溶性フィルムの製造方法 - Google Patents
水溶性フィルム、薬剤包装体及び水溶性フィルムの製造方法 Download PDFInfo
- Publication number
- WO2017043509A1 WO2017043509A1 PCT/JP2016/076258 JP2016076258W WO2017043509A1 WO 2017043509 A1 WO2017043509 A1 WO 2017043509A1 JP 2016076258 W JP2016076258 W JP 2016076258W WO 2017043509 A1 WO2017043509 A1 WO 2017043509A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- water
- soluble film
- film
- pva
- weight
- Prior art date
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/002—Methods
- B29B7/007—Methods for continuous mixing
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/58—Component parts, details or accessories; Auxiliary operations
- B29B7/72—Measuring, controlling or regulating
- B29B7/726—Measuring properties of mixture, e.g. temperature or density
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/80—Component parts, details or accessories; Auxiliary operations
- B29B7/88—Adding charges, i.e. additives
-
- 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
- B29C41/00—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
- B29C41/003—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor characterised by the choice of material
-
- 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
- B29C41/00—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
- B29C41/02—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor for making articles of definite length, i.e. discrete articles
- B29C41/16—Slip casting, i.e. applying a slip or slurry on a perforated or porous or absorbent surface with the liquid being drained away
-
- 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
- B29C41/00—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
- B29C41/24—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor for making articles of indefinite length
-
- 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
- B29C41/00—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
- B29C41/24—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor for making articles of indefinite length
- B29C41/28—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor for making articles of indefinite length by depositing flowable material on an endless belt
-
- 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
- B29C41/00—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
- B29C41/34—Component parts, details or accessories; Auxiliary operations
- B29C41/46—Heating or cooling
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D65/00—Wrappers or flexible covers; Packaging materials of special type or form
- B65D65/38—Packaging materials of special type or form
- B65D65/46—Applications of disintegrable, dissolvable or edible materials
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L29/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal or ketal radical; Compositions of hydrolysed polymers of esters of unsaturated alcohols with saturated carboxylic acids; Compositions of derivatives of such polymers
- C08L29/02—Homopolymers or copolymers of unsaturated alcohols
- C08L29/04—Polyvinyl alcohol; Partially hydrolysed homopolymers or copolymers of esters of unsaturated alcohols with saturated carboxylic acids
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D17/00—Detergent materials or soaps characterised by their shape or physical properties
- C11D17/04—Detergent materials or soaps characterised by their shape or physical properties combined with or containing other objects
- C11D17/041—Compositions releasably affixed on a substrate or incorporated into a dispensing means
- C11D17/042—Water soluble or water disintegrable containers or substrates containing cleaning compositions or additives for cleaning compositions
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D17/00—Detergent materials or soaps characterised by their shape or physical properties
- C11D17/04—Detergent materials or soaps characterised by their shape or physical properties combined with or containing other objects
- C11D17/041—Compositions releasably affixed on a substrate or incorporated into a dispensing means
- C11D17/042—Water soluble or water disintegrable containers or substrates containing cleaning compositions or additives for cleaning compositions
- C11D17/043—Liquid or thixotropic (gel) compositions
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
- C11D3/16—Organic compounds
- C11D3/37—Polymers
- C11D3/3746—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- C11D3/3753—Polyvinylalcohol; Ethers or esters thereof
-
- 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
- B29K2029/00—Use of polyvinylalcohols, polyvinylethers, polyvinylaldehydes, polyvinylketones or polyvinylketals or derivatives thereof as moulding material
- B29K2029/04—PVOH, i.e. polyvinyl alcohol
-
- 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
- B29K2867/00—Use of polyesters or derivatives thereof as mould material
- B29K2867/003—PET, i.e. polyethylene terephthalate
-
- 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
- B29K2995/00—Properties of moulding materials, reinforcements, fillers, preformed parts or moulds
- B29K2995/0037—Other properties
- B29K2995/0059—Degradable
- B29K2995/0062—Degradable water-soluble
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
- B29L2031/00—Other particular articles
- B29L2031/712—Containers; Packaging elements or accessories, Packages
- B29L2031/7128—Bags, sacks, sachets
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2300/00—Characterised by the use of unspecified polymers
- C08J2300/14—Water soluble or water swellable polymers, e.g. aqueous gels
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2329/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal, or ketal radical; Hydrolysed polymers of esters of unsaturated alcohols with saturated carboxylic acids; Derivatives of such polymer
- C08J2329/02—Homopolymers or copolymers of unsaturated alcohols
- C08J2329/04—Polyvinyl alcohol; Partially hydrolysed homopolymers or copolymers of esters of unsaturated alcohols with saturated carboxylic acids
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2403/00—Characterised by the use of starch, amylose or amylopectin or of their derivatives or degradation products
- C08J2403/02—Starch; Degradation products thereof, e.g. dextrin
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2429/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal, or ketal radical; Hydrolysed polymers of esters of unsaturated alcohols with saturated carboxylic acids; Derivatives of such polymer
- C08J2429/02—Homopolymers or copolymers of unsaturated alcohols
- C08J2429/04—Polyvinyl alcohol; Partially hydrolysed homopolymers or copolymers of esters of unsaturated alcohols with saturated carboxylic acids
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/0008—Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
- C08K5/0016—Plasticisers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/05—Alcohols; Metal alcoholates
- C08K5/053—Polyhydroxylic alcohols
-
- 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W90/00—Enabling technologies or technologies with a potential or indirect contribution to greenhouse gas [GHG] emissions mitigation
- Y02W90/10—Bio-packaging, e.g. packing containers made from renewable resources or bio-plastics
Definitions
- the present invention relates to a water-soluble film (hereinafter sometimes referred to as PVA film) containing a polyvinyl alcohol resin (hereinafter, polyvinyl alcohol may be abbreviated as PVA). More specifically, it is a film with excellent solubility in water-soluble film and reduced curl, and when forming a package, it shows a good sealing property, and the sealing part is not easily displaced.
- PVA film a water-soluble film, a pharmaceutical package using the same, and a method for producing a water-soluble film.
- the PVA film is a film made of a PVA resin having water solubility while being a thermoplastic resin, and a hydrophobic film usually used for packaging films such as a polyethylene terephthalate film and a polyolefin film, Various physical properties and feeling of touch are greatly different.
- water-soluble unit packaging bag used for such applications, for example, 5 to 30 parts by weight of a plasticizer, 1 to 10 parts by weight of starch, and 0.01 to 2 parts by weight of a surfactant are blended with 100 parts by weight of PVA.
- Water-soluble film see, for example, Patent Document 1
- the plasticizer (B) is 20 to 50 parts by weight
- the filler (C) is 2 to 30 parts by weight
- the surfactant (D) is 0.1 parts by weight per 100 parts by weight of the anionic group-modified PVA resin (A).
- a water-soluble film made of a resin composition containing 01 to 2.5 parts by weight is known.
- the water-soluble films disclosed in Patent Documents 1 and 2 are excellent in water solubility, and can be used as a medicine package by packaging a liquid detergent or the like. Moreover, in order to raise the tolerance with respect to detergents, such as liquid detergent, it is desirable to contain acid-modified PVA as a water-soluble film for packaging. On the other hand, in film formation, there is concern about the occurrence of curling, and in order to prevent this, heat treatment at a high temperature is required. However, when heat treatment is performed at a high temperature, in the case of a water-soluble film using an acid-modified PVA-based resin, various properties such as solubility are obtained from the point that it is easier to crystallize than a water-soluble film made of ordinary unmodified PVA. It is thought to decline. For this reason, it has been difficult to achieve both curl reduction and solubility, which are contradictory physical properties.
- the present inventors focused on conflicting physical properties such as the complete dissolution time and curl area ratio of the water-soluble film in the water-soluble film containing the PVA-based resin,
- the product of such physical property values is selectively important, and thereby the water-soluble film has excellent solubility in water-soluble film and curl is reduced. It has been found that deviation is less likely to occur, good sealing properties are exhibited, and the productivity is excellent.
- the gist of the present invention is a water-soluble film containing the PVA resin (A), and the product (T ⁇ S) of the complete dissolution time (T) and the curled area ratio (S) is represented by the following formula (
- the present invention relates to a water-soluble film characterized by satisfying 1).
- the complete dissolution time (T) is a 35 mm ⁇ 35 mm water-soluble film, left in an environment of 23 ° C. and 40% RH for 24 hours, and then immersed in water at 10 ° C. This is the time (seconds) until the adhesive film dissolves.
- the curled area ratio (S) is 100 mm ⁇ 100 mm when the water-soluble film is suspended for 24 hours in an environment of 23 ° C. and 40% RH with one side of the water-soluble film flow (MD) fixed.
- the present invention also provides a medicine package in which a liquid detergent is packaged with the water-soluble film.
- the water-soluble film is a method for producing the water-soluble film, wherein the film-forming raw material containing the PVA resin (A) is formed, dried, and then heat-treated at 95 to 135 ° C. This manufacturing method is also provided.
- the water-soluble film of the present invention is excellent in solubility of the water-soluble film, curling is reduced when forming a package, and therefore it is less likely to be misaligned and exhibits good sealing properties and excellent productivity. It can be used for various packaging applications, and is particularly useful for unit packaging applications such as drugs.
- T complete dissolution time
- curled area ratio (S) is 50% or less, excellent workability is provided.
- the water-soluble film can have good flexibility.
- the content of the plasticizer (B) is 20 parts by weight or more with respect to 100 parts by weight of the PVA resin (A), the toughness of the water-soluble film is deteriorated over time when the medicine package is formed. It becomes possible to suppress.
- the PVA resin (A) contains the anionic group-modified PVA resin (a1), solubility in water is improved.
- the water-soluble film When the water content of the water-soluble film is 3 to 15% by weight, the water-soluble film has good flexibility and can prevent blocking.
- the water-soluble film of the present invention contains a PVA resin (A), and the product (T ⁇ S) of the complete dissolution time (T) and the curled area ratio (S) satisfies the following formula (1). It is.
- the complete dissolution time (T) is a 35 mm ⁇ 35 mm water-soluble film, left in an environment of 23 ° C. and 40% RH for 24 hours, and then immersed in water at 10 ° C. This is the time (seconds) until the adhesive film dissolves.
- the curled area ratio (S) is 100 mm ⁇ 100 mm when the water-soluble film is suspended for 24 hours in an environment of 23 ° C. and 40% RH with one side of the water-soluble film flow (MD) fixed.
- a preferable range of the product (T ⁇ S) of the complete dissolution time (T) and the curl area ratio (S) is the following formula (2), more preferably the following formula (3). 1500 ⁇ complete dissolution time (T) ⁇ curl area ratio (S) ⁇ 6000 (2) 2000 ⁇ complete dissolution time (T) ⁇ curl area ratio (S) ⁇ 5000 (3)
- the complete dissolution time (T) is preferably 150 seconds or less, more preferably 10 to 145 seconds, and particularly preferably 20 to 140 seconds. If the complete dissolution time is too long, the dissolution time of the package tends to be delayed when a liquid detergent package is obtained. In addition, when too short, there exists a tendency for a package to be torn even if a water droplet adheres for a short time.
- the curled area ratio (S) is preferably 50% or less, more preferably 47% or less, and particularly preferably 45% or less. If the curled area is too large, the water-soluble film is wound when the pouch is formed, and the workability tends to be lowered.
- the complete dissolution time (T) and curl area ratio (S) are measured as follows.
- [Complete dissolution time (T)] In a 35 mm ⁇ 35 mm water-soluble film cut out from the center in the width direction (TD) of the water-soluble film, the water-soluble film is allowed to stand in an environment of 23 ° C. and 40% RH for 24 hours, and then the water-soluble film becomes parallel to the water surface. Fix it with a jig.
- 1 liter of water at 10 ° C. is put into a 1 liter beaker, and the rotation is adjusted so that the vortex is 50 mm above the water surface while stirring with a stirrer.
- a prepared water-soluble film fixed on a jig is poured in such a way that the water-soluble film is located at a depth of 50 mm from the water surface, and then the time (seconds) until the water-soluble film dissolves. ).
- Curled area ratio (%) 100 ⁇ [ ⁇ (X1) + (X2) ⁇ / 2] ⁇ 100/10000 X1: One length (mm) from the lowermost end when the curled part is extended to the center part of the curl X2: The other length (mm) from the lowest end to the center of the curl when the curled part is extended
- the water-soluble film of the present invention is produced, for example, as follows. First, the PVA resin (A) used in the present invention will be described. Examples of the PVA resin (A) used in the present invention include unmodified PVA and modified PVA resin.
- the average saponification degree of the PVA resin (A) used in the present invention is preferably 80 mol% or more, particularly 82 to 99.9 mol%, more preferably 85 to 98.5 mol%, particularly
- the average saponification degree is preferably too small, and if the average saponification degree is too small, the solubility of the water-soluble film tends to decrease over time depending on the pH of the drug to be packaged. In addition, when the average saponification degree is too large, the solubility in water tends to be greatly reduced due to the heat history during film formation.
- the average saponification degree is preferably 80 mol% or more, particularly 82 to 99 mol%, more preferably 85 mol%. It is preferably ⁇ 90 mol%.
- the average saponification degree is preferably 80 mol% or more, particularly 85 to 99.9 mol%, more preferably 90 mol%. It is preferably ⁇ 98 mol%.
- the average saponification degree is preferably 85 mol% or more, particularly 88 to 99 mol%, It is preferably 90 to 97 mol%.
- the polymerization degree of the PVA resin (A) of the present invention can be generally represented by an aqueous solution viscosity, and a 4 wt% aqueous solution viscosity at 20 ° C. is preferably 5 to 50 mPa ⁇ s, and more preferably 10 It is preferably 45 mPa ⁇ s, particularly 15 to 40 mPa ⁇ s. If the viscosity is too small, the mechanical strength of the water-soluble film as a packaging material tends to decrease. On the other hand, if the viscosity is too large, the aqueous solution viscosity during film formation tends to be high and productivity tends to decrease.
- the viscosity of the 4% by weight aqueous solution of unmodified PVA at 20 ° C. is preferably 5 to 50 mPa ⁇ s, more preferably 10 to 45 mPa ⁇ s, and particularly preferably 15 to 40 mPa ⁇ s.
- the viscosity of the 4% by weight aqueous solution of the modified PVA resin at 20 ° C. is preferably 5 to 50 mPa ⁇ s, more preferably 10 to 45 mPa ⁇ s, and particularly preferably 15 to 40 mPa ⁇ s.
- the average degree of saponification is measured according to JIS K 6726 3.5, and the viscosity of a 4% by weight aqueous solution is measured according to JIS K 6726 3.1.2.
- modified PVA resins include nonionic group-modified PVA resins, cationic group-modified PVA resins, and anionic group-modified PVA resins.
- modified PVA resin used in the present invention it is preferable to use an anionic group-modified PVA resin in terms of solubility.
- anionic group include a carboxyl group, a sulfonic acid group, and a phosphoric acid group. From the viewpoint of chemical resistance and stability over time, a carboxyl group and a sulfonic acid group, particularly a carboxyl group is preferable. .
- the modified amount of the anionic group-modified PVA resin is preferably 1 to 10 mol%, more preferably 2 to 9 mol%, particularly preferably 2 to 8 mol%, particularly preferably. If the amount of modification is too small, the solubility in water tends to decrease. If the amount is too large, the productivity of the modified PVA-based resin decreases or the biodegradability decreases. There is a tendency, and there is a tendency that blocking is likely to occur, so that practicality is lowered.
- unmodified PVA and modified PVA resin can be used alone as the PVA resin (A).
- PVA-type resin (A) contains modified PVA-type resin.
- the content ratio (weight ratio) between the modified PVA resin and the unmodified PVA is preferably 95/5 to 60/40, particularly 94/6 to 70/30, more preferably 93/7 to 80/20. It is preferable that If the content is too small, the plasticizer tends to bleed out, and if it is too large, blocking tends to occur.
- the unmodified PVA preferably has a 4% by weight aqueous solution viscosity at 20 ° C. of 5 to 50 mPa ⁇ s, more preferably 8 to 45 mPa ⁇ s. In particular, it is preferably 12 to 40 mPa ⁇ s, more preferably 15 to 35 mPa ⁇ s. If the viscosity is too small, the mechanical strength of the water-soluble film as a packaging material tends to decrease. On the other hand, if the viscosity is too large, the aqueous solution viscosity during film formation tends to be high and productivity tends to decrease.
- Unmodified PVA can be produced by saponifying a vinyl ester polymer obtained by polymerizing a vinyl ester compound.
- vinyl ester compounds examples include vinyl formate, vinyl acetate, vinyl trifluoroacetate, vinyl propionate, vinyl butyrate, vinyl caprate, vinyl laurate, vinyl versatate, vinyl palmitate, and vinyl stearate. Although it is mentioned, it is preferable to use vinyl acetate.
- the vinyl ester compounds may be used alone or in combination of two or more.
- the modified PVA resin is a method of copolymerizing the vinyl ester compound and an unsaturated monomer copolymerizable with the vinyl ester compound, and then saponifying, or post-modifying unmodified PVA. It can be manufactured by a method or the like.
- the following unsaturated monomer copolymerizable with the vinyl ester compound may be copolymerized.
- a modified PVA resin is obtained, a modified group is used as the following monomer. It is necessary to copolymerize the unsaturated monomer having.
- unsaturated monomers include olefins such as ethylene, propylene, isobutylene, ⁇ -octene, ⁇ -dodecene, ⁇ -octadecene, 3-buten-1-ol, 4-penten-1-ol, 5- Derivatives such as hydroxy group-containing ⁇ -olefins such as hexen-1-ol and acylated products thereof, unsaturated acids such as acrylic acid, methacrylic acid, crotonic acid, maleic acid, maleic anhydride, itaconic acid, undecylenic acid, Examples thereof include salts, monoesters, dialkyl esters, amides such as diacetone acrylamide, acrylamide and methacrylamide, olefin sulfonic acids such as ethylene sulfonic acid, allyl sulfonic acid and methallyl sulfonic acid, and salts thereof. These may be used alone or in combination of two or more.
- modified PVA resin examples include those having a primary hydroxyl group in the side chain.
- the number of primary hydroxyl groups is usually 1 to 5, preferably 1 to 2, and particularly preferably 1. It is done.
- examples thereof include a PVA resin having a 1,2-diol structural unit in the side chain and a PVA resin having a hydroxyalkyl group in the side chain.
- Such a PVA resin having a 1,2-diol structural unit in the side chain includes, for example, (i) a method of saponifying a copolymer of vinyl acetate and 3,4-diacetoxy-1-butene, and (ii) acetic acid.
- a copolymerization method in the preparation of the PVA resin (A) for example, a known polymerization method such as a solution polymerization method, an emulsion polymerization method, a suspension polymerization method and the like can be arbitrarily used. It is carried out by a solution polymerization method using a lower alcohol such as isopropyl alcohol as a solvent. In this solution polymerization, the monomer is charged in the case of a modified PVA resin. First, the whole amount of the vinyl ester compound and a part of the unsaturated monomer having a carboxyl group, for example, are charged, and polymerization is performed. Any method may be used, such as a method of starting and adding the remaining unsaturated monomers continuously or in portions during the polymerization period, or a method of batch-feeding the unsaturated monomers having a carboxyl group. it can.
- a known polymerization catalyst such as an azo catalyst such as azobisisobutyronitrile or a peroxide catalyst such as acetyl peroxide, benzoyl peroxide or lauroyl peroxide is appropriately selected depending on the polymerization method. be able to.
- the polymerization reaction temperature is selected from the range of about 50 ° C. to the boiling point.
- the obtained copolymer is dissolved in alcohol and carried out in the presence of a saponification catalyst.
- the alcohol include alcohols having 1 to 5 carbon atoms such as methanol, ethanol, butanol and the like.
- the concentration of the copolymer in the alcohol is selected from the range of 20 to 50% by weight.
- the saponification catalyst examples include alkali catalysts such as alkali metal hydroxides and alcoholates such as sodium hydroxide, potassium hydroxide, sodium methylate, sodium ethylate, potassium methylate, and the like. It is also possible to use a catalyst.
- the saponification catalyst is preferably used in an amount of 1 to 100 mmol equivalents relative to the vinyl ester compound. These saponification catalysts can be used alone or in combination of two or more.
- the carboxyl group-modified PVA resin can be produced by any method, for example, (I) after copolymerizing an unsaturated monomer having a carboxyl group and a vinyl ester compound.
- examples thereof include a method for saponification, and (II) a method for saponification after polymerization of a vinyl ester compound in the presence of a carboxyl group-containing alcohol, aldehyde or thiol as a chain transfer agent.
- the above-mentioned compounds can be used, but vinyl acetate is preferably used.
- Examples of the unsaturated monomer having a carboxyl group in the method (I) include ethylenically unsaturated dicarboxylic acids (maleic acid, fumaric acid, itaconic acid, etc.), or ethylenically unsaturated dicarboxylic acid monoester (maleic acid).
- monomers such as ethylenically unsaturated carboxylic acid anhydrides (maleic anhydride, itaconic anhydride, etc.) or ethylenically unsaturated monocarboxylic acids ((meth) acrylic acid, crotonic acid, etc.), and Salt.
- maleic acid maleic acid monoalkyl ester, maleic acid dialkyl ester, maleate, maleic anhydride, itaconic acid, itaconic acid monoalkyl ester, itaconic acid dialkyl ester, (meth) acrylic acid, etc.
- maleic acid, maleic acid monoalkyl ester, maleic acid dialkyl ester, maleate, maleic anhydride especially maleic acid monoalkyl ester.
- a compound derived from a thiol having a particularly large chain transfer effect is effective, and examples include compounds represented by the following general formulas (1) to (3).
- salts of the compounds represented by the above general formulas (1) to (3) include mercaptoacetate, 2-mercaptopropionate, 3-mercaptopropionate, 2-mercaptostearate and the like. These compounds can be used alone or in combination of two or more.
- alkyl esters of ethylenically unsaturated carboxylic acids allyl esters of saturated carboxylic acids, ⁇ -olefins, alkyl vinyl ethers, alkyl allyl ethers, (meth) acrylamide, (meth) acrylonitrile, styrene, vinyl chloride Etc. can be used. These may be used alone or in combination of two or more.
- the method for producing the carboxyl group-modified PVA resin is not limited to the above method.
- a PVA resin partially saponified product or completely saponified product
- a hydroxyl group such as dicarboxylic acid, aldehyde carboxylic acid, hydroxycarboxylic acid or the like.
- a method of post-reacting a carboxyl group-containing compound having a reactive functional group can also be carried out.
- a sulfonic acid-modified PVA resin modified with a sulfonic acid group for example, vinyl sulfonic acid, styrene sulfonic acid, allyl sulfonic acid, methallyl sulfonic acid, 2-acrylamido-2-methylpropane sulfonic acid, etc.
- examples of a method for post-modifying the above-mentioned unmodified PVA include a method of converting the unmodified PVA into acetoacetate ester, acetalization, urethanization, etherification, grafting, phosphoric esterification, and oxyalkylene.
- a plasticizer (B) to the PVA resin (A) from the viewpoint of imparting flexibility to the water-soluble film in the case of a medicine package.
- a plasticizer (B) Only one type of plasticizer (B) can be used, or at least two types can be used in combination.
- the toughness of the water-soluble film itself when using at least two types as a package is used.
- plasticizer (B) is a polyhydric alcohol (b1) having a melting point of 80 ° C. or higher (hereinafter sometimes abbreviated as plasticizer (b1)), and the other type has a melting point. It is polyhydric alcohol (b2) (hereinafter sometimes abbreviated as plasticizer (b2)) having a temperature of 50 ° C. or lower, toughness at the time of manufacturing a water-soluble film or a package, and packaging for liquid detergent This is preferable in terms of shape stability over time when used as a body and sealing properties at low temperatures.
- polyhydric alcohol (b1) having a melting point of 80 ° C. or higher many of sugar alcohols, monosaccharides and polysaccharides can be applied. Among them, for example, salicyl alcohol (83 ° C.), catechol (105 ° C.) ), Resorcinol (110 ° C.), hydroquinone (172 ° C.), bisphenol A (158 ° C.), bisphenol F (162 ° C.), dipentyl glycol (127 ° C.) and the like, phloroglucinol (218 ° C.), etc.
- Trihydric alcohols such as erythritol (121 ° C), threitol (88 ° C), pentaerythritol (260 ° C), xylitol (92 ° C), arabitol (103 ° C), fucitol (153 ° C), glucose (146 ), Pentahydric alcohols such as fructose (104 ° C.), mannitol (16 ° C), hexahydric alcohols such as sorbitol (95 ° C), inositol (225 ° C), octahydric alcohols such as lactitol (146 ° C), sucrose (186 ° C), trehalose (97 ° C), maltitol (145 ° C), etc.
- erythritol 121 ° C
- threitol 88 ° C
- pentaerythritol 260 ° C
- xylitol 92
- the inside of () shows melting
- those having a melting point of 85 ° C. or higher, particularly 90 ° C. or higher are preferable from the viewpoint of the tensile strength of the water-soluble film.
- the upper limit of the melting point is preferably 300 ° C., particularly 200 ° C.
- the number of hydroxyl groups in one molecule is preferably 4 or more from the viewpoint of compatibility with the PVA resin (A), and more preferably 5 to 10 Particularly preferred is 6-8, and specific examples include sorbitol, sucrose, trehalose and the like.
- the plasticizer (b1) preferably has a molecular weight of 150 or more, more preferably 160 to 500, and particularly preferably 180 to 400 in terms of toughness of the water-soluble film.
- Specific examples include sorbitol, sucrose, and the like.
- the polyhydric alcohol (b2) having a melting point of 50 ° C. or lower is an aliphatic alcohol, for example, preferably ethylene glycol ( ⁇ 13 ° C.), diethylene glycol ( ⁇ 11 ° C.), triethylene glycol ( ⁇ 7 ° C.).
- the lower limit of the melting point is usually ⁇ 80 ° C., preferably ⁇ 10 ° C., particularly preferably 0 ° C.
- the number of hydroxyl groups in one molecule is 4 or less, particularly 3 or less because flexibility at room temperature (25 ° C.) can be easily controlled.
- glycerin and the like are preferable.
- the plasticizer (b2) preferably has a molecular weight of 100 or less, more preferably 50 to 100, and particularly preferably 60 to 95, in terms of easy control of flexibility.
- glycerol etc. are suitable, for example.
- a plasticizer (b3) other than the plasticizers (b1) and (b2) may be used in combination.
- the plasticizer (b3) include trimethylolpropane (58 ° C.), diethylene glycol. Alcohols such as monomethyl ether, cyclohexanol, carbitol, polypropylene glycol, ethers such as dibutyl ether, carboxylic acids such as stearic acid, oleic acid, linoleic acid, linolenic acid, sorbic acid, citric acid, adipic acid, cyclohexanone, etc.
- Ketones such as monoethanolamine, triethanolamine, ethylenediamine and imidazole compounds, and amino acids such as alanine, glycine, aspartic acid, glutamic acid, histidine, lysine and cysteine. These may be used alone or in combination of two or more.
- the content of the plasticizer (B) is preferably 20 parts by weight or more with respect to 100 parts by weight of the PVA resin (A), particularly 25 to 70 parts by weight, more preferably 30 to 60 parts by weight. Part by weight, in particular 35 to 50 parts by weight is preferred. If the content of the plasticizer (B) is too small, the toughness of the water-soluble film tends to be deteriorated over time when a liquid such as a liquid detergent is packaged to form a package. In addition, when there is too much, it exists in the tendency for mechanical strength to fall.
- the content weight ratio (b1 / b2) is preferably 0.1 to 5, particularly 0.2 to 4.5, more preferably It is preferably 0.5 to 4, particularly 0.7 to 3. If the content is too small, the water-soluble film tends to be too soft and blocking tends to occur, and if it is too large, the water-soluble film tends to be too hard and tends to be brittle even in a low humidity environment.
- the content of the plasticizer (b1) and the plasticizer (b2) is 5 to 40 parts by weight of the plasticizer (b1), more preferably 8 to 100 parts by weight of the PVA resin (A).
- the amount is preferably 30 parts by weight, particularly 10 to 25 parts by weight, and the plasticizer (b2) is preferably 5 to 40 parts by weight, more preferably 10 to 35 parts by weight, and particularly preferably 15 to 30 parts by weight. If the amount of the plasticizer (b1) is too small, the water-soluble film tends to be too soft and blocking tends to occur. If the amount is too large, the water-soluble film tends to be too hard and tends to be brittle even in a low humidity environment. is there.
- plasticizer (b2) when there is too little plasticizer (b2), there exists a tendency for a water-soluble film to become hard too much, and there exists a tendency for it to become brittle also in a low-humidity environment, and when too much, a water-soluble film becomes too soft and tends to produce blocking. There is.
- the total amount of the plasticizer (b1) and the plasticizer (b2) is preferably 70% by weight or more, more preferably 80% by weight or more, and particularly 87% by weight or more with respect to the entire plasticizer (B). In particular, it is preferably 90% by weight or more, more preferably 95% by weight or more. Particularly preferred is the case where the entire plasticizer (B) consists solely of the plasticizer (b1) and the plasticizer (b2). If the total amount of the plasticizers (b1) and (b2) is too small, the mechanical strength tends to decrease.
- a filler (C), a surfactant (D) and the like can be further contained as necessary.
- the filler (C) used in the present invention is contained for the purpose of blocking resistance, and specific examples include inorganic fillers and organic fillers. Among them, organic fillers are preferable.
- the average particle diameter is preferably 0.1 to 20 ⁇ m, more preferably 0.5 to 15 ⁇ m. In addition, the said average particle diameter can be measured with a laser diffraction type particle size distribution measuring apparatus etc., for example.
- Such an inorganic filler preferably has an average particle size of 1 to 10 ⁇ m. If the average particle size is too small, the effect of dispersibility of the water-soluble film in water tends to be small. When the water-soluble film is formed and processed, it tends to become a pinhole when it is stretched, or the appearance may deteriorate.
- the inorganic filler include, for example, talc, clay, silicon dioxide, diatomaceous earth, kaolin, mica, asbestos, gypsum, graphite, glass balloon, glass beads, calcium sulfate, barium sulfate, ammonium sulfate, calcium sulfite, and calcium carbonate.
- the organic filler preferably has an average particle size of 0.5 to 20 ⁇ m, more preferably 0.5 to 10 ⁇ m, particularly preferably 0.5 to 7 ⁇ m, still more preferably 0.5 to 5 ⁇ m. is there. If the average particle size is too small, the cost tends to be high, and if it is too large, a pinhole tends to be formed when the water-soluble film is stretched.
- organic filler examples include starch, melamine resin, polymethyl (meth) acrylate resin, polystyrene resin, and biodegradable resins such as polylactic acid.
- biodegradable resins such as polymethyl (meth) acrylate resins, polystyrene resins and starch are preferably used. These may be used alone or in combination of two or more.
- starch examples include raw starch (corn starch, potato starch, sweet potato starch, wheat starch, kissava starch, sago starch, tapioca starch, sorghum starch, rice starch, bean starch, kudzu starch, bracken starch, lotus starch, Castor starch, etc.), physically modified starch ( ⁇ -starch, fractionated amylose, wet heat-treated starch, etc.), enzyme-modified starch (hydrolyzed dextrin, enzyme-degraded dextrin, amylose, etc.), chemically modified starch (acid-treated starch, hypochlorous acid) Chloric acid oxidized starch, dialdehyde starch, etc.), chemically modified starch derivatives (esterified starch, etherified starch, cationized starch, crosslinked starch, etc.) and the like. These may be used alone or in combination of two or more. Of these, raw starch, especially corn starch and rice starch are
- the content of the filler (C) is preferably 1 to 30 parts by weight, more preferably 2 to 25 parts by weight, particularly 2.5 to 20 parts by weight, based on 100 parts by weight of the PVA resin (A). Part.
- the content is too small, the blocking resistance tends to decrease, and when the content is too large, a pinhole tends to be formed when the water-soluble film is stretched.
- the surfactant (D) used in the present invention is contained for the purpose of improving the peelability from the cast surface during the production of a water-soluble film, and is a nonionic surfactant, a cationic surfactant, an anionic surfactant. Agents and the like.
- polyoxyethylene nonyl phenyl ether polyoxyethylene octyl nonyl ether, polyoxyethylene dodecyl phenyl ether, polyoxyethylene alkyl allyl ether, polyoxyethylene sorbitan monolaurate, polyoxyethylene sorbitan monopalmitate, polyoxyethylene sorbitan Nonionic interfaces such as monostearate, polyoxyethylene sorbitan monooleate, polyoxyalkylene alkyl ether phosphate monoethanolamine salt, polyoxyethylene lauryl amino ether, polyoxyethylene alkylamino ether such as polyoxyethylene stearyl amino ether An activator is mentioned and it is used 1 type or in combination of 2 or more types. Of these, polyoxyalkylene alkyl ether phosphate monoethanolamine salt and polyoxyethylene lauryl amino ether are preferable in terms of production stability.
- the content of the surfactant (D) is preferably 0.01 to 3 parts by weight, more preferably 0.1 to 2.5 parts by weight, based on 100 parts by weight of the PVA resin (A). In particular, the amount is preferably 0.5 to 2 parts by weight.
- the content is too small, the peelability between the cast surface of the film forming apparatus and the formed water-soluble film tends to decrease, and the productivity tends to decrease.
- the content is too large, the water-soluble film is used as a package. There is a tendency to cause inconvenience such as a decrease in adhesive strength at the time of sealing.
- water-soluble polymers for example, sodium polyacrylate, polyethylene oxide, polyvinylpyrrolidone, dextrin, chitosan, chitin, methylcellulose, hydroxyethylcellulose, etc.
- Fragrances rust inhibitors, colorants, extenders, antifoaming agents, ultraviolet absorbers, fluorescent brighteners, liquid paraffins, bitterness components (for example, denatonium benzoate, etc.) and the like can also be contained.
- these may be used alone or in combination of two or more.
- an antioxidant from the viewpoint of suppressing yellowing.
- antioxidants include sulfites such as sodium sulfite, potassium sulfite, calcium sulfite and ammonium sulfite, tartaric acid, ascorbic acid, sodium thiosulfate, catechol, Rongalite, etc.
- the blending amount is preferably 0.1 to 10 parts by weight, more preferably 0.2 to 5 parts by weight, and particularly preferably 0.3 to 3 parts by weight with respect to 100 parts by weight of the PVA resin (A).
- a composition is obtained, and such a PVA resin composition is dissolved or dispersed using water to prepare a film forming raw material, which is then formed into a water-soluble film (PVA film).
- a method such as a melt extrusion method or a casting method can be employed, and the casting method is preferable in terms of film thickness accuracy.
- the casting method is performed, for example, as follows.
- the dissolution method normal temperature dissolution, high temperature dissolution, pressure dissolution, etc. are usually employed. Among them, high temperature dissolution and pressure dissolution are preferred because there are few undissolved materials and excellent productivity.
- the dissolution temperature is usually 80 to 100 ° C., preferably 90 to 100 ° C. when dissolving at high temperature, and usually 80 to 130 ° C., preferably 90 to 120 ° C. when dissolving under pressure.
- the dissolution time is usually 1 to 20 hours, preferably 2 to 15 hours, and more preferably 3 to 10 hours. If the dissolution time is too short, undissolved products tend to remain, and if the dissolution time is too long, productivity tends to decrease.
- examples of the stirring blade include paddle, full zone, max blend, twister, anchor, ribbon, and propeller.
- defoaming treatment is performed on the obtained PVA resin aqueous solution.
- examples of the defoaming method include stationary defoaming, vacuum defoaming, and biaxial extrusion defoaming. It is done. Of these, stationary defoaming and biaxial extrusion defoaming are preferable.
- the temperature for stationary defoaming is usually 50 to 100 ° C., preferably 70 to 95 ° C., and the defoaming time is usually 2 to 30 hours, preferably 5 to 20 hours.
- water is added to the PVA resin (A) (powder) to form a PVA resin aqueous solution, preferably a plasticizer (B) and other blends are added, and the PVA resin composition An aqueous dispersion or aqueous solution is obtained.
- water is added to a PVA resin composition containing the PVA resin (A), preferably a plasticizer (B) and various blends, to obtain an aqueous dispersion or aqueous solution of the PVA resin composition.
- the solid concentration of the aqueous dispersion or aqueous solution of the PVA resin composition is preferably 10 to 50% by weight, particularly 15 to 40% by weight, and more preferably 20 to 35% by weight.
- the concentration is too low, the productivity of the water-soluble film tends to decrease. If the concentration is too high, the viscosity becomes too high, and it takes time to defoam the dope. Tend to. Furthermore, if the temperature of the metal surface of the endless belt or drum roll is too low, drying tends to take time, and if it is too high, foaming tends to occur during film formation.
- the aqueous dispersion or aqueous solution is passed through a slit such as a T-die, cast onto a cast surface such as a metal surface of an endless belt or drum roll, or a plastic substrate surface such as a polyethylene terephthalate film, dried, and dried as necessary.
- the PVA film (water-soluble film) of the present invention can be obtained by further heat treatment. For example, it can be performed under the following film forming conditions.
- the temperature of the discharge part in the aqueous dispersion or aqueous solution of the PVA-based resin composition is preferably 60 to 98 ° C, particularly 70 to 95 ° C. If the temperature is too low, the drying time tends to be long and the productivity tends to decrease. If the temperature is too high, foaming or the like tends to occur.
- the film formation speed is preferably 3 to 80 m / min, particularly 5 to 60 m / min, and more preferably 8 to 50 m / min.
- an appropriate heat treatment is performed, that is, a heat treatment at a relatively high temperature. It is important to do.
- Such heat treatment can be performed with a hot roll, but other examples include floating and far-infrared treatment. In particular, it is preferable in terms of productivity to carry out with a hot roll.
- the heat treatment temperature is preferably 95 to 135 ° C, more preferably 100 to 135 ° C, still more preferably 105 to 130 ° C, particularly preferably 110 to 125 ° C, and particularly preferably 110 to 120 ° C. If the temperature is too low, the curl improving effect tends to be low, and if it is too high, the solubility tends to decrease.
- the heat treatment time is preferably 1 to 60 seconds, particularly preferably 3 to 50 seconds, and further preferably 5 to 40 seconds. If it is too short, the curl improving effect tends to be low, and if it is too long, the curl is improved but the solubility tends to be lowered.
- an aqueous dispersion or aqueous solution of the PVA resin composition is cast on a plastic substrate or a metal substrate such as a polyethylene terephthalate film or a polyethylene film, and dried to obtain a PVA film (water-soluble film). ) Can also be obtained.
- the thickness of the PVA film is appropriately selected depending on the application and the like, but is preferably 10 to 120 ⁇ m, more preferably 15 to 110 ⁇ m, and particularly preferably 20 to 100 ⁇ m. If the thickness is too thin, the mechanical strength of the PVA-based film tends to decrease. If the thickness is too thick, the dissolution rate in water tends to be slow, and the film forming efficiency tends to decrease.
- the width of the PVA film is appropriately selected depending on the application and the like, but is preferably 300 to 5000 mm, more preferably 500 to 4000 mm, and particularly preferably 800 to 3000 mm. If the width is too narrow, the production efficiency tends to decrease, and if it is too wide, it tends to be difficult to control slackness or film thickness.
- the length of the PVA-based film is appropriately selected depending on the application and the like, but is preferably 500 to 20000 m, more preferably 800 to 15000 m, and particularly preferably 1000 to 10,000 m. If this length is too short, there is a tendency that it takes time to switch the PVA film, and if it is too long, there is a tendency that the appearance defect and weight due to winding tightening become too heavy.
- the surface of the PVA-based film may be a plane, but an embossed pattern is formed on one or both sides of the PVA-based film from the viewpoint of blocking resistance, slipperiness during processing, reduced adhesion between products, and appearance. It is also preferable to make irregularities such as fine irregular patterns and special engraving patterns.
- the processing temperature is usually 60 to 150 ° C, preferably 80 to 140 ° C.
- the processing pressure is usually 2 to 8 MPa, preferably 3 to 7 MPa.
- the processing time is usually 0.01 to 5 seconds, preferably 0.1 to 3 seconds, although it depends on the processing pressure and the film forming speed.
- the water content of the obtained PVA-based film is preferably 3 to 15% by weight, particularly 5 to 14% by weight in terms of mechanical strength and sealing properties. Further, it is preferably 6 to 13% by weight. If the water content is too low, the water-soluble film tends to be too hard, and if it is too high, blocking tends to occur. Adjustment to such a moisture content can be achieved by appropriately setting drying conditions and humidity control conditions. In addition, the said moisture content is measured based on JISK67263.4, and let the value of the obtained volatile matter be a moisture content.
- the film formation is preferably performed in an environment of 10 to 35 ° C., particularly 15 to 30 ° C., for example.
- the humidity is usually 70% RH or less.
- the obtained PVA-type film can be made into a film roll by winding up to a core pipe (S1).
- the obtained film roll can be supplied as a product as it is, it is preferably wound around a core tube (S2) having a length corresponding to the PVA film width of a desired size and supplied as a film roll.
- the core tube (S1) around which the PVA film is wound is cylindrical, and the material thereof can be appropriately selected from metals, plastics, etc., but is preferably metal in terms of fastness and strength.
- the inner diameter of the core tube (S1) is preferably 3 to 30 cm, more preferably 10 to 20 cm.
- the thickness of the core tube (S1) is preferably 1 to 30 mm, more preferably 2 to 25 mm.
- the length of the core tube (S1) needs to be longer than the width of the PVA film, and preferably protrudes from 1 to 50 cm from the end of the film roll.
- the core tube (S2) has a cylindrical shape, and the material thereof can be appropriately selected from paper, metal, plastic and the like, but is preferably paper in terms of weight reduction and handling.
- the inner diameter of the core tube (S2) is preferably 3 to 30 cm, more preferably 10 to 20 cm.
- the thickness of the core tube (S2) is preferably 1 to 30 mm, more preferably 3 to 25 mm.
- the length of the core tube (S2) may be any length that is equal to or longer than the PVA film width of the product, and preferably is equal to or longer than 50 cm.
- the PVA film When winding on the core tube (S2), the PVA film is slit to a desired width.
- a slit is slit using a shear blade or a leather blade, but it is preferable to slit with a shear blade in terms of the smoothness of the slit cross section.
- the obtained film roll is packaged with a packaging film of a water vapor barrier resin, but such a film is not particularly limited, but the moisture permeability is 10 g / m 2 ⁇ 24 hr (according to JIS Z 0208). Measurement)
- a packaging film of a water vapor barrier resin but such a film is not particularly limited, but the moisture permeability is 10 g / m 2 ⁇ 24 hr (according to JIS Z 0208). Measurement)
- the following can be used. Specific examples include, for example, single-layer films such as high-density polyethylene, low-density polyethylene, polypropylene, polyester, polyvinylidene chloride-coated polypropylene, and glass-deposited polyester, or laminated films thereof, or split cloth, paper, and non-woven fabric.
- a laminated film etc. are mentioned. Examples of the laminated film include a laminated film of glass-deposited polyester and polyethylene, a laminated film of polyvinylidene chloride-co
- Such a film is preferably subjected to an antistatic treatment from the viewpoint of preventing the introduction of foreign substances, and the antistatic agent may be kneaded into the film or coated on the surface.
- an antistatic agent of about 0.01 to 5% by weight relative to the resin is used, and in the case of surface coating, an antistatic agent of about 0.01 to 1 g / m 2 is used.
- the antistatic agent for example, alkyldiethanolamine, polyoxyethylene alkylamine, higher fatty acid alkanolamide, sorbitan fatty acid ester and the like are used.
- a packaging film made of an aluminum material after the film roll is packaged with a packaging film of a water vapor barrier resin Such films include aluminum foil, laminated film of aluminum foil and moisture-resistant plastic film (for example, laminated film of aluminum foil and polyethylene film), laminated film of aluminum-deposited film and moisture-resistant plastic film (for example, aluminum-deposited polyester film and polyethylene film) Laminating film), an alumina vapor-deposited film and a moisture-resistant plastic film laminating film (for example, laminating film of alumina vapor-deposited polyester film and polyethylene film), etc.
- Laminated film of polyolefin film and film is useful, especially stretched polypropylene film / polyethylene film / aluminum Laminated films made of configuration of Umuhaku / polyethylene film, laminated film or the like made of structure of oriented polypropylene film / low density polyethylene film / aluminum foil is useful.
- core tube through holes are formed at both ends of the film roll directly from the film roll or after being wrapped with a packaging film in order to prevent scratches at the end and adhesion of foreign matters such as dust.
- a protective pad can be attached.
- As the shape of the protective pad a disc-shaped sheet or film is practical according to the film roll.
- a cushioning function such as foam, woven fabric, and nonwoven fabric.
- a desiccant can be enclosed separately, or it can be laminated or mixed in the protective pad.
- the protective pad material is advantageously plastic, and specific examples thereof include polystyrene, polyethylene, polypropylene, polyester, polyvinyl chloride, and the like.
- the protective pad containing the desiccant examples include, for example, calcium chloride, silica gel, molecular sieves, saccharides, particularly saccharides with high osmotic pressure, desiccants or water absorbents such as water absorbent resins, natural celluloses, synthetic celluloses, Moisture absorbing layers that are dispersed, impregnated and coated and dried in moldable materials such as glass cloth and non-woven fabrics, and these moldable materials and polyester film, polyethylene film, polypropylene film, Teflon (registered) (Trademark) film and the like sandwiched between thermoplastic resin films.
- sheet-like desiccants examples include “Idie Sheet” manufactured by IDY, “Arrow Sheet” and “Zeo Sheet” manufactured by Shinagawa Kasei Co., Ltd., and “High Sheet Dry” manufactured by High Sheet Industrial Co., Ltd. .
- the film roll wrapped by such means is supported by providing brackets (support plates) at both end projections of the core tube or by placing the both end projections on a gantry, and without being grounded, so-called air Storage and transportation are preferably performed in a floating state.
- a bracket is used when the film width is relatively small, and a gantry is used when the film width is relatively large.
- the bracket is made of a veneer plate or a plastic plate, and the size of the bracket is sufficient if the four sides of the bracket are larger than the diameter of the film roll.
- a pair of brackets are arranged upright and fitted to the core tube protrusions at both ends of the film roll so as to face each other, and are provided on the film roll.
- a hollow hole slightly larger than the diameter of the core tube may be provided in the central portion of the bracket, or a U-shape may be hollowed from the upper portion of the bracket to the central portion so that the core tube can be easily inserted.
- the film roll supported by the bracket is stored and transported in a carton such as a cardboard box, but when using a rectangular bracket, the four corners should be cut off to facilitate the work during storage. preferable.
- the side of the bracket (thickness portion) is the same as the tape width so that the tape does not move or loosen. It is also practical to provide a tape misalignment prevention groove.
- the temperature should be 10-30 ° C. and humidity 40-75% RH. .
- the water-soluble film of the present invention thus obtained is useful for various packaging applications and the like, and is particularly useful for unit packaging applications for drugs and the like.
- the drug is not particularly limited and may be alkaline, neutral, or acidic, and the drug may have any shape such as granules, tablets, powders, powders, liquids, etc. Drugs that are used dissolved or dispersed are preferred and are particularly useful for packaging liquid detergents.
- the liquid detergent preferably has a pH value of 6 to 12 when dissolved or dispersed in water, particularly preferably 7 to 11.
- the water content of the liquid detergent is preferably 15% by weight or less, particularly preferably 0.1 to 10% by weight, and more preferably 0.1 to 7% by weight. It is not insolubilized and has excellent water solubility.
- the pH value is measured according to JIS K 3362 8.3.
- the water content is measured according to JIS K 3362 7.21.3.
- the liquid detergent package which is an example of the pharmaceutical package of the present invention, is one in which a liquid detergent is included in a package made of a water-soluble film.
- the size of the liquid detergent package is usually 10 to 50 mm in length, preferably 20 to 40 mm.
- the thickness of the package of the water-soluble film is usually 10 to 120 ⁇ m, preferably 15 to 110 ⁇ m, more preferably 20 to 100 ⁇ m.
- the amount of the liquid detergent to be included is usually 5 to 50 mL, preferably 10 to 40 mL.
- the surface of the liquid detergent package is smooth. Furthermore, in terms of blocking resistance, slipperiness during processing, reduced adhesion between products (packaging bodies), and appearance, an embossed pattern, fine uneven pattern, special engraving on the outer surface of the packaging body (water-soluble film) It may have been subjected to uneven processing such as a handle. Further, the liquid detergent package is held in a shape containing a liquid detergent during storage. At the time of use (during washing), the package (water-soluble film) comes into contact with water, so that the liquid detergent contained in the package is dissolved and flows out of the package.
- a known method can be employed. For example, (1) a method for heat sealing, (2) a method for water sealing, (3) a method for sealing with glue, and the like (2) a method for water sealing is versatile and advantageous.
- Example 1 90 parts of carboxyl group-modified PVA (A1) having a 4% aqueous solution viscosity of 22 mPa ⁇ s at 20 ° C., an average saponification degree of 94 mol%, and a modification amount of 2.0 mol% with maleic acid monomethyl ester as the PVA resin (A) 10 parts unmodified PVA (A2) having a 4% aqueous solution viscosity at 20 ° C.
- plasticizer (B) 20 parts of sorbitol (b1) and glycerin (b2) 20 parts, 8 parts of starch (average particle size 20 ⁇ m) as filler (C), 2 parts of polyoxyalkylene alkyl ether phosphate monoethanolamine salt as surfactant (D) and water are mixed and dissolved.
- aqueous PVA solution solid concentration 25% in which starch was dispersed was obtained.
- the obtained PVA aqueous solution was degassed at 80 ° C. and cooled to 40 ° C.
- the PVA aqueous solution was cast on a polyethylene terephthalate film (thickness: 125 ⁇ m, width: 300 mm) at a thickness of 630 ⁇ m and a width of 200 mm, and passed through a 3 m drying chamber (105 ° C.) at a speed of 0.350 m / min.
- the PVA film (water-soluble film) having a thickness of 89 ⁇ m was obtained.
- the obtained PVA film (F0) (water-soluble film) was affixed to a 300 mm ⁇ 210 mm SUS frame with four sides fixed, and heat treated by placing it in a hot air dryer set at 100 ° C. for 30 seconds.
- a PVA film (F1) (water-soluble film) was obtained.
- a prepared water-soluble film fixed on a jig is poured in such a way that the water-soluble film is located at a depth of 50 mm from the water surface, and then the time (seconds) until the water-soluble film dissolves. ) was measured.
- Curled area ratio (%) 100 ⁇ [ ⁇ (X1) + (X2) ⁇ / 2] ⁇ 100/10000 X1: One length (mm) from the lowermost end when the curled part is extended to the center part of the curl X2: The other length (mm) from the lowest end to the center of the curl when the curled part is extended
- Example 2 A PVA film (F0) (water-soluble film) was produced in the same manner as in Example 1.
- the obtained PVA film (F0) (water-soluble film) was affixed to a 300 mm ⁇ 210 mm SUS frame with four sides fixed, and heat treated by placing it in a hot air dryer set at 110 ° C. for 30 seconds.
- a PVA film (F2) (water-soluble film) was obtained.
- Example 3 A PVA film (F0) (water-soluble film) was produced in the same manner as in Example 1.
- the obtained PVA film (F0) (water-soluble film) was affixed to a 300 mm ⁇ 210 mm SUS frame with four sides fixed, and heat treated by placing it in a hot air dryer set at 120 ° C. for 30 seconds.
- a PVA film (F3) was obtained.
- Example 4 A PVA film (F0) (water-soluble film) was produced in the same manner as in Example 1.
- the obtained PVA film (F0) (water-soluble film) was affixed to a 300 mm ⁇ 210 mm SUS frame with four sides fixed, and heat treated by placing it in a hot air dryer set at 130 ° C. for 30 seconds.
- a PVA film (F4) was obtained.
- the obtained PVA-based film (F4) (water-soluble film) was measured and evaluated in the same manner as in Example 1.
- Example 5 A PVA film (F0) (water-soluble film) was produced in the same manner as in Example 1.
- the obtained PVA film (F0) (water-soluble film) was affixed to a 300 mm x 210 mm SUS frame with four sides fixed, and heat treated by placing it in a hot air dryer set at 95 ° C for 30 seconds.
- the PVA film (F5) was obtained.
- the obtained PVA film (F5) (water-soluble film) was measured and evaluated in the same manner as in Example 1.
- a PVA film (F0) (water-soluble film) was produced in the same manner as in Example 1.
- the obtained PVA-based film (F0) (water-soluble film) was affixed to a 300 mm ⁇ 210 mm SUS frame with four sides fixed, and heat treated by placing it in a hot air dryer set at 90 ° C. for 30 seconds.
- a PVA film (F6) (water-soluble film) was obtained.
- a PVA film (F0) (water-soluble film) was produced in the same manner as in Example 1.
- the obtained PVA film (F0) (water-soluble film) was affixed to a 300 mm x 210 mm SUS frame with four sides fixed, and heat treated by placing it in a hot air dryer set at 140 ° C for 30 seconds.
- a PVA film (F7) (water-soluble film) was obtained.
- the product (T ⁇ S) satisfies a predetermined range.
- the balance between the complete dissolution time and the curl area ratio is poor, and the product (T ⁇ S) does not satisfy the predetermined range. It will interfere with sex. From these results, it can be seen that when the water-soluble film of the example is used, for example, when a liquid detergent is packaged to form a package, a good package is obtained.
- a package was prepared by the following procedure using a package manufacturing machine manufactured by Engel. That is, a PVA film (F1) (bottom film) is fixed on a mold (package to be molded: length 45 mm, width 42 mm, height 30 mm) in the lower part of the above-mentioned manufacturing machine, and is placed on the upper part of the apparatus. Also fixed a PVA film (F1) (top film). The bottom film was heated for 10 seconds with a dryer generating hot air at 90 ° C., and the bottom film was vacuum-formed into a mold.
- a package manufacturing machine manufactured by Engel That is, a PVA film (F1) (bottom film) is fixed on a mold (package to be molded: length 45 mm, width 42 mm, height 30 mm) in the lower part of the above-mentioned manufacturing machine, and is placed on the upper part of the apparatus. Also fixed a PVA film (F1) (top film). The bottom film was heated for 10 seconds with a dryer generating hot air at 90 ° C
- liquid detergent (5.4% glycerin, 22.6% propylene glycol, 10.4% moisture contained in P &G's"Arière Power Gel Ball” (content ratio of polyhydric alcohol in liquid detergent) : 28%)
- P &G's"Arière Power Gel Ball content ratio of polyhydric alcohol in liquid detergent
- the water-soluble film of the present invention is excellent in solubility, curling is reduced when forming a package, and therefore, it is less likely to be misaligned, exhibits good sealing properties, and is excellent in productivity. It can be used for various packaging applications, and is particularly useful for unit packaging applications of drugs and the like, particularly liquid detergents.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Manufacturing & Machinery (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Wood Science & Technology (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- Materials Engineering (AREA)
- Dispersion Chemistry (AREA)
- Wrappers (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
一方で、フィルム製膜においては、カールの発生が懸念されるものであり、これを防止するためには、高温での熱処理が必要となってくる。
しかしながら、高温での熱処理を行うと、酸変性PVA系樹脂を用いた水溶性フィルムの場合は、通常の未変性PVAからなる水溶性フィルムよりも、結晶化しやすい点から溶解性などの諸物性が低下すると考えられている。このようなことから、相反する物性となるカールの軽減と溶解性を両立させるのは困難であった。
〔式(1)において、完溶時間(T)は、35mm×35mmの水溶性フィルムにおいて、23℃、40%RHの環境下に24時間放置した後、10℃の水に浸漬して、水溶性フィルムが溶解するまでの時間(秒)である。また、カール面積率(S)は、100mm×100mmの水溶性フィルムにおいて、水溶性フィルムの流れ(MD)方向の一辺を固定して、23℃、40%RHの環境下に24時間ぶら下げた時に、正面から見た際の水溶性フィルム全体の面積に対する、水溶性フィルムのカールしている部分の面積率(%)である。〕
本発明の水溶性フィルムは、PVA系樹脂(A)を含有してなり、完溶時間(T)とカール面積率(S)の積(T×S)が下記式(1)を満足するものである。
〔式(1)において、完溶時間(T)は、35mm×35mmの水溶性フィルムにおいて、23℃、40%RHの環境下に24時間放置した後、10℃の水に浸漬して、水溶性フィルムが溶解するまでの時間(秒)である。また、カール面積率(S)は、100mm×100mmの水溶性フィルムにおいて、水溶性フィルムの流れ(MD)方向の一辺を固定して、23℃、40%RHの環境下に24時間ぶら下げた時に、正面から見た際の水溶性フィルム全体の面積に対する、水溶性フィルムのカールしている部分の面積率(%)である。〕
1500≦完溶時間(T)×カール面積率(S)≦6000 ・・・(2)
2000≦完溶時間(T)×カール面積率(S)≦5000 ・・・(3)
[完溶時間(T)]
水溶性フィルムの幅方向(TD)における中央部から切り出した35mm×35mmの水溶性フィルムにおいて、23℃、40%RHの環境下に24時間放置した後、かかる水溶性フィルムを水面に平行になるように冶具で固定しておく。一方、1リットルビーカーに10℃の水1リットルを入れ、スターラーにより撹拌しながら、渦が水面から50mmの高さになるように回転を調整する。そこに、予め用意しておいた、冶具に固定した水溶性フィルムを、水溶性フィルムが水面から50mmの深さの位置になるように投入し、その後水溶性フィルムが溶解するまでの時間(秒)を測定する。
水溶性フィルムの幅方向(TD)における中央部から、100mm×100mmの水溶性フィルムを切り出す。つぎに、図1に示すように、上記水溶性フィルム1の流れ方向(MD)の一辺を幅15mmの粘着テープ2で固定して、23℃、40%RHの環境下に24時間ぶら下げた時の、水溶性フィルム1のカールしている部分の面積を算出する。その算出値から、水溶性フィルム1のカール面積率を下記式より求める。
カール面積率(%)
=100×[{(X1)+(X2)}/2]×100/10000
X1:カール部分を伸ばした際の最下端からカールの中心部分までの一方の長さ(mm)
X2:カール部分を伸ばした際の最下端からカールの中心部分までのもう一方の長さ(mm)
まず、本発明で用いられるPVA系樹脂(A)について説明する。
本発明で用いられるPVA系樹脂(A)としては、未変性PVAや変性PVA系樹脂が挙げられる。
これら化合物は単独でもしくは2種以上併せて用いることができる。
上記の中でも、水溶性フィルムの引張強度の点で融点が85℃以上、特には90℃以上のものが好ましい。なお、融点の上限は300℃、特には200℃が好ましい。
かかる可塑剤(b1)が少なすぎると水溶性フィルムが柔らかくなりすぎて、ブロッキングが生じやすくなる傾向があり、多すぎると水溶性フィルムが硬くなりすぎる傾向があり、低湿環境下でもろくなる傾向がある。また、可塑剤(b2)が少なすぎると水溶性フィルムが硬くなりすぎる傾向があり、低湿環境下でもろくなる傾向があり、多すぎると水溶性フィルムが柔らかくなりすぎて、ブロッキングが生じやすくなる傾向がある。
溶解方法としては、通常、常温溶解、高温溶解、加圧溶解等が採用され、中でも、未溶解物が少なく、生産性に優れる点から高温溶解、加圧溶解が好ましい。
溶解温度が、高温溶解の場合には、通常80~100℃、好ましくは90~100℃であり、加圧溶解の場合には、通常80~130℃、好ましくは90~120℃である。
溶解時間としては、通常1~20時間、好ましくは2~15時間、更に好ましくは3~10時間である。溶解時間が短すぎると未溶解物が残る傾向にあり、長すぎると生産性が低下する傾向にある。
更に、溶解した後、得られたPVA系樹脂水溶液に対して脱泡処理が行われるが、かかる脱泡方法としては、例えば、静置脱泡、真空脱泡、二軸押出脱泡等が挙げられる。中でも静置脱泡、二軸押出脱泡が好ましい。
静置脱泡の温度としては、通常50~100℃、好ましくは70~95℃であり、脱泡時間は、通常2~30時間、好ましくは5~20時間である。
例えば、下記の製膜条件にて行うことができる。
かかる凹凸加工に際しては、加工温度は、通常60~150℃であり、好ましくは80~140℃である。加工圧力は、通常2~8MPa、好ましくは3~7MPaである。加工時間は、上記加工圧力、製膜速度にもよるが、通常0.01~5秒であり、好ましくは0.1~3秒である。
また、必要に応じて、凹凸加工処理の後に、熱による水溶性フィルムの意図しない延伸を防止するために、冷却処理を施してもよい。
なお、上記含水率は、JIS K 6726 3.4に準拠して測定され、得られた揮発分の値を含水率とする。
芯管(S1)の内径は、3~30cmが好ましく、より好ましくは10~20cmである。
芯管(S1)の肉厚は、1~30mmが好ましく、より好ましくは2~25mmである。
芯管(S1)の長さは、PVA系フィルムの幅より長くすることが必要で、フィルムロールの端部から1~50cm突出するようにするのが好ましい。
芯管(S2)の内径は、3~30cmが好ましく、より好ましくは10~20cmである。
芯管(S2)の肉厚は、1~30mmが好ましく、より好ましくは3~25mmである。
芯管(S2)の長さは、製品のPVA系フィルム幅と同等或いはそれ以上の長さのものであればよく、好ましくは同等~50cm長いものである。
かかるスリットに当たっては、シェア刃やレザー刃などを用いてスリットされるが、好ましくはシェア刃でスリットすることがスリット断面の平滑性の点で好ましい。
帯電防止剤としては、例えば、アルキルジエタノールアミン、ポリオキシエチレンアルキルアミン、高級脂肪酸アルカノールアミド、ソルビタン脂肪酸エステル等が使用される。
包装に当たっては内側の水蒸気バリヤー性樹脂の包装フィルム、外側のアルミニウム素材からなる包装フィルムで順次包装を行い、幅方向に余った部分を芯管に押し込めば良い。
保護パットの形状は、フィルムロールにあわせて、円盤状のシート、フィルムが実用的である。保護効果を顕著にするため発泡体、織物状、不織布状等の緩衝機能を付加させるのが良い。又、湿気からフィルムロールを守るため乾燥剤を別途封入したり、前記保護パットに積層又は混入したりしておくこともできる。
保護パットの素材はプラスチックが有利であり、その具体例としては、例えば、ポリスチレン、ポリエチレン、ポリプロピレン、ポリエステル、ポリ塩化ビニル等が挙げられる。
市販されているシート状乾燥剤の例としては、アイディ社製の「アイディシート」や品川化成社製の「アローシート」、「ゼオシート」、ハイシート工業社製の「ハイシートドライ」等がある。
ブラケットはベニヤ板やプラスチック板からなるものであり、その大きさはブラケットの4辺がフィルムロールの直径より大きいものであればよい。
また、上記一対のブラケットがぐらつかないように、両者を結束テープで固定するのが有利であり、そのときテープの移動や弛みが起こらないようにブラケットの側面(厚さ部分)にテープ幅と同程度のテープズレ防止溝を設けて置くのも実用的である。
なお、上記pH値は、JIS K 3362 8.3に準拠して測定される。また、水分量は、JIS K 3362 7.21.3に準じて測定される。
本発明の薬剤包装体の一例である液体洗剤包装体は、水溶性フィルムからなる包装体内に液体洗剤が内包されてなるものである。液体洗剤包装体の大きさは、通常長さ10~50mm、好ましくは20~40mmである。また、水溶性フィルムからなる包装体のフィルムの厚みは、通常10~120μm、好ましくは15~110μm、より好ましくは20~100μmである。内包される液体洗剤の量は、通常5~50mL、好ましくは10~40mLである。
尚、例中「部」、「%」とあるのは、重量基準を意味する。
PVA系樹脂(A)として、20℃における4%水溶液粘度22mPa・s、平均ケン化度94モル%、マレイン酸モノメチルエステルによる変性量2.0モル%のカルボキシル基変性PVA(A1)を90部、20℃における4%水溶液粘度18mPa・s、平均ケン化度88モル%の未変性PVA(A2)を10部、可塑剤(B)として、ソルビトール(b1)を20部及びグリセリン(b2)を20部、フィラー(C)として澱粉(平均粒子径20μm)を8部、界面活性剤(D)として、ポリオキシアルキレンアルキルエーテルリン酸エステルモノエタノールアミン塩を2部及び水を混合して溶解処理し、澱粉が分散したPVA水溶液(固形分濃度25%)を得た。
得られたPVA水溶液を80℃にて脱泡し、40℃まで冷やした。そのPVA水溶液をポリエチレンテレフタレートフィルム(厚み:125μm、幅:300mm)上に、厚さ630μm、幅200mmで流延し、3mの乾燥室(105℃)の中を0.350m/minの速度で通過させ乾燥し、厚さ89μmのPVA系フィルム(水溶性フィルム)を得た。
得られたPVA系フィルム(F0)(水溶性フィルム)を300mm×210mmのSUS製の枠に4辺を固定して貼り付け、100℃に設定した熱風乾燥機に30秒入れることで熱処理を行い、PVA系フィルム(F1)(水溶性フィルム)を得た。
得られたPVA系フィルム(F1)(水溶性フィルム)について、以下の通り測定、評価を行った。
水溶性フィルムの幅方向(TD)における中央部から35mm×35mmに切り出した水溶性フィルムにおいて、23℃、40%RHの環境下に24時間放置した後、かかる水溶性フィルムを水面に平行になるように冶具で固定しておいた。一方、1リットルビーカーに10℃の水1リットルを入れ、スターラーにより撹拌しながら、渦が水面から50mmの高さになるように回転を調整した(回転子長3cm、回転数750rpm)。そこに、予め用意しておいた、冶具に固定した水溶性フィルムを、水溶性フィルムが水面から50mmの深さの位置になるように投入し、その後水溶性フィルムが溶解するまでの時間(秒)を測定した。
水溶性フィルムの幅方向(TD)における中央部から、100mm×100mmの水溶性フィルムを切り出した。つぎに、図1に示すように、上記水溶性フィルム1の流れ方向(MD)の一辺を幅15mmの粘着テープ2で固定して、23℃、40%RHの環境下に24時間ぶら下げた時の、水溶性フィルム1のカールしている部分の面積を算出した。その算出値から、水溶性フィルム1のカール面積率を下記式より求めた。
カール面積率(%)
=100×[{(X1)+(X2)}/2]×100/10000
X1:カール部分を伸ばした際の最下端からカールの中心部分までの一方の長さ(mm)
X2:カール部分を伸ばした際の最下端からカールの中心部分までのもう一方の長さ(mm)
実施例1と同様にPVA系フィルム(F0)(水溶性フィルム)を作製した。
得られたPVA系フィルム(F0)(水溶性フィルム)を300mm×210mmのSUS製の枠に4辺を固定して貼り付け、110℃に設定した熱風乾燥機に30秒入れることで熱処理を行い、PVA系フィルム(F2)(水溶性フィルム)を得た。
得られたPVA系フィルム(F2)(水溶性フィルム)について、実施例1と同様にして、測定、評価を行った。
実施例1と同様にPVA系フィルム(F0)(水溶性フィルム)を作製した。
得られたPVA系フィルム(F0)(水溶性フィルム)を300mm×210mmのSUS製の枠に4辺を固定して貼り付け、120℃に設定した熱風乾燥機に30秒入れることで熱処理を行い、PVA系フィルム(F3)を得た。
得られたPVA系フィルム(F3)(水溶性フィルム)について、実施例1と同様にして、測定、評価を行った。
実施例1と同様にPVA系フィルム(F0)(水溶性フィルム)を作製した。
得られたPVA系フィルム(F0)(水溶性フィルム)を300mm×210mmのSUS製の枠に4辺を固定して貼り付け、130℃に設定した熱風乾燥機に30秒入れることで熱処理を行い、PVA系フィルム(F4)を得た。
得られたPVA系フィルム(F4)(水溶性フィルム)について、実施例1と同様にして、測定、評価を行った。
実施例1と同様にPVA系フィルム(F0)(水溶性フィルム)を作製した。
得られたPVA系フィルム(F0)(水溶性フィルム)を300mm×210mmのSUS製の枠に4辺を固定して貼り付け、95℃に設定した熱風乾燥機に30秒入れることで熱処理を行い、PVA系フィルム(F5)を得た。
得られたPVA系フィルム(F5)(水溶性フィルム)について、実施例1と同様にして、測定、評価を行った。
実施例1と同様にPVA系フィルム(F0)(水溶性フィルム)を作製した。
得られたPVA系フィルム(F0)(水溶性フィルム)を300mm×210mmのSUS製の枠に4辺を固定して貼り付け、90℃に設定した熱風乾燥機に30秒入れることで熱処理を行い、PVA系フィルム(F6)(水溶性フィルム)を得た。
得られたPVA系フィルム(F6)(水溶性フィルム)について、実施例1と同様にして、測定、評価を行った。
実施例1と同様にPVA系フィルム(F0)(水溶性フィルム)を作製した。
得られたPVA系フィルム(F0)(水溶性フィルム)を300mm×210mmのSUS製の枠に4辺を固定して貼り付け、140℃に設定した熱風乾燥機に30秒入れることで熱処理を行い、PVA系フィルム(F7)(水溶性フィルム)を得た。
得られたPVA系フィルム(F7)(水溶性フィルム)について、実施例1と同様にして、測定、評価を行った。
上記実施例1にて得られたPVA系フィルム(F1)を用い、Engel社製包装体製造機により、下記の手順にて包装体を作製した。
即ち、上記製造機の下部にある金型(成型される包装体:縦45mm、横42mm、高さ30mm)の上に、PVA系フィルム(F1)(ボトムフィルム)を固定し、装置の上部にもPVA系フィルム(F1)(トップフィルム)を固定した。ボトムフィルムを10秒間、90℃の熱風を発生させるドライヤーで加熱し、ボトムフィルムを金型に真空成型した。その後、P&G社製の「アリエールパワージェルボール」に包装された液体洗剤(グリセリン5.4%、プロピレングリコール22.6%、水分10.4%を含有(液体洗剤中の多価アルコールの含有割合:28%))を、成型されたPVA系フィルム(F1)に20mL投入した。トップフィルムに水を1.5g塗布し、トップフィルムとボトムフィルムを圧着した。30秒間圧着した後に、真空を開放し、包装体を得た。
得られた液体洗剤包装体は、外観に関して問題のない良好なものが得られた。
Claims (11)
- ポリビニルアルコール系樹脂(A)を含有してなる水溶性フィルムであって、完溶時間(T)とカール面積率(S)の積(T×S)が下記式(1)を満足することを特徴とする水溶性フィルム。
1000≦完溶時間(T)×カール面積率(S)≦7000 ・・・(1)
〔式(1)において、完溶時間(T)は、35mm×35mmの水溶性フィルムにおいて、23℃、40%RHの環境下に24時間放置した後、10℃の水に浸漬して、水溶性フィルムが溶解するまでの時間(秒)である。また、カール面積率(S)は、100mm×100mmの水溶性フィルムにおいて、水溶性フィルムの流れ(MD)方向の一辺を固定して、23℃、40%RHの環境下に24時間ぶら下げた時の、正面から見た際の水溶性フィルム全体の面積に対する、水溶性フィルムのカールしている部分の面積率(%)である。〕 - 完溶時間(T)が、150秒以下であることを特徴とする請求項1記載の水溶性フィルム。
- カール面積率(S)が、50%以下であることを特徴とする請求項1または2記載の水溶性フィルム。
- 可塑剤(B)を含有してなることを特徴とする請求項1~3のいずれか一項に記載の水溶性フィルム。
- 可塑剤(B)の含有量が、ポリビニルアルコール系樹脂(A)100重量部に対して20重量部以上であることを特徴とする請求項4記載の水溶性フィルム。
- ポリビニルアルコール系樹脂(A)が、アニオン性基変性ポリビニルアルコール系樹脂(a1)を含有してなることを特徴とする請求項1~5のいずれか一項に記載の水溶性フィルム。
- 水溶性フィルムの含水率が3~15重量%であることを特徴とする請求項1~6のいずれか一項に記載の水溶性フィルム。
- 薬剤包装に用いることを特徴とする請求項1~7のいずれか一項に記載の水溶性フィルム。
- 請求項1~8のいずれか一項に記載の水溶性フィルムで、液体洗剤が包装されてなることを特徴とする薬剤包装体。
- 液体洗剤が、水に溶解又は分散させた時のpH値が6~12で、水分量が15重量%以下であることを特徴とする請求項9記載の薬剤包装体。
- 請求項1~8のいずれか一項に記載の水溶性フィルムの製造方法であって、ポリビニルアルコール系樹脂(A)を含有してなる製膜原料を製膜し、乾燥した後、95~135℃で熱処理することを特徴とする請求項1~8いずれか記載の水溶性フィルムの製造方法。
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2016556036A JP6805828B2 (ja) | 2015-09-11 | 2016-09-07 | 水溶性フィルム、薬剤包装体及び水溶性フィルムの製造方法 |
KR1020187003884A KR102516145B1 (ko) | 2015-09-11 | 2016-09-07 | 수용성 필름, 약제 포장체 및 수용성 필름의 제조 방법 |
CN201680046684.6A CN107922645B (zh) | 2015-09-11 | 2016-09-07 | 水溶性薄膜、药剂包装体及水溶性薄膜的制造方法 |
EP16844370.3A EP3348605A4 (en) | 2015-09-11 | 2016-09-07 | WATER-SOLUBLE FILM, CHEMICAL PACKAGING AND METHOD FOR PRODUCING A WATER-SOLUBLE FILM |
US15/753,693 US10696934B2 (en) | 2015-09-11 | 2016-09-07 | Water-soluble film, chemical agent package and water-soluble film production method |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2015-179020 | 2015-09-11 | ||
JP2015179020 | 2015-09-11 | ||
JP2015-221980 | 2015-11-12 | ||
JP2015221980 | 2015-11-12 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2017043509A1 true WO2017043509A1 (ja) | 2017-03-16 |
Family
ID=58239816
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2016/076258 WO2017043509A1 (ja) | 2015-09-11 | 2016-09-07 | 水溶性フィルム、薬剤包装体及び水溶性フィルムの製造方法 |
Country Status (6)
Country | Link |
---|---|
US (1) | US10696934B2 (ja) |
EP (1) | EP3348605A4 (ja) |
JP (1) | JP6805828B2 (ja) |
KR (1) | KR102516145B1 (ja) |
CN (1) | CN107922645B (ja) |
WO (1) | WO2017043509A1 (ja) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2019094490A (ja) * | 2017-11-20 | 2019-06-20 | 日本合成化学工業株式会社 | ポリビニルアルコール系水溶性フィルム及びその製造方法、ならびに薬剤包装体 |
WO2019189685A1 (ja) | 2018-03-29 | 2019-10-03 | 三菱ケミカル株式会社 | 水溶性フィルム及びその製造方法、並びに薬剤包装体 |
CN110603285A (zh) * | 2017-06-12 | 2019-12-20 | 三菱化学株式会社 | 水溶性薄膜和药剂包装体、以及水溶性薄膜的制造方法 |
CN110785879A (zh) * | 2017-06-07 | 2020-02-11 | 株式会社可乐丽 | 非水电解质电池用粘合剂组合物、以及使用其的非水电解质电池用粘合剂水溶液、非水电解质电池用浆料组合物、非水电解质电池用电极及非水电解质电池 |
WO2020138444A1 (ja) * | 2018-12-28 | 2020-07-02 | 株式会社クラレ | 水溶性フィルムおよび包装体 |
CN113174071A (zh) * | 2021-04-26 | 2021-07-27 | 东北林业大学 | 一种阴离子多糖膜的压封方法 |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2017043510A1 (ja) * | 2015-09-11 | 2017-03-16 | 日本合成化学工業株式会社 | 液体洗剤包装用水溶性フィルム及び液体洗剤包装体 |
EP3348604A4 (en) * | 2015-09-11 | 2019-05-15 | The Nippon Synthetic Chemical Industry Co., Ltd. | WATER-SOLUBLE FILM AND CHEMICAL PACKAGING BODY |
US20180251615A1 (en) * | 2015-09-11 | 2018-09-06 | The Nippon Synthetic Chemical Industry Co., Ltd. | Water-soluble film and chemical agent package |
JPWO2017043513A1 (ja) * | 2015-09-11 | 2018-06-21 | 日本合成化学工業株式会社 | 水溶性フィルム、薬剤包装体及び水溶性フィルムの製造方法 |
JP7204488B2 (ja) * | 2016-06-13 | 2023-01-16 | モノソル リミテッド ライアビリティ カンパニー | 水溶性パケット |
JPWO2020039988A1 (ja) * | 2018-08-22 | 2020-02-27 | ||
CN113226689B (zh) * | 2018-12-28 | 2023-04-14 | 株式会社可乐丽 | 水溶性膜、其制造方法以及包装体 |
WO2020138442A1 (ja) * | 2018-12-28 | 2020-07-02 | 株式会社クラレ | 水溶性フィルムおよび包装体 |
KR20230016192A (ko) * | 2020-05-26 | 2023-02-01 | 피터 모리스 리서치 앤드 디밸롭먼트 리미티드 | 수용성 중합체의 제조 방법, 그에 의해 제조된 수용성 중합체, 및 용융-가공가능한 수용성 중합체 조성물 |
US11718010B2 (en) | 2020-05-26 | 2023-08-08 | Peter Morris Research And Development Limited | Method of making a water-soluble polymer composition |
WO2023054721A1 (ja) * | 2021-10-01 | 2023-04-06 | 株式会社クラレ | 水溶性フィルム、製造方法及び包装体 |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002301899A (ja) * | 2001-04-04 | 2002-10-15 | Nippon Synthetic Chem Ind Co Ltd:The | 転写印刷用ベースフィルム |
JP2009051947A (ja) * | 2007-08-27 | 2009-03-12 | Nippon Synthetic Chem Ind Co Ltd:The | 農薬包装用水溶性フィルム |
JP2013518173A (ja) * | 2010-01-29 | 2013-05-20 | モノソル リミテッド ライアビリティ カンパニー | Pvohポリマーのブレンド材を有する改良された水溶性フィルムおよびそれで作られたパケット |
WO2015098979A1 (ja) * | 2013-12-25 | 2015-07-02 | 株式会社クラレ | 変性ポリビニルアルコールおよびそれを含有する水溶性フィルム |
Family Cites Families (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU2001256248A1 (en) * | 2000-04-14 | 2001-10-30 | Unilever Plc | Water soluble package and liquid contents thereof |
AU2001262160A1 (en) * | 2000-04-14 | 2001-10-30 | Hewitt, Malcolm | Water soluble package of liquid cleaning composition |
ES2236081T3 (es) * | 2000-05-02 | 2005-07-16 | Kuraray Co., Ltd. | Pelicula de polimero de poli(alcohol vinilico), metodo para producir la misma y pelicula de polarizacion. |
JP5116911B2 (ja) | 2000-05-19 | 2013-01-09 | 株式会社クラレ | 水溶性フィルムの製造法 |
GB0021113D0 (en) * | 2000-08-25 | 2000-10-11 | Reckitt & Colmann Prod Ltd | Improvements in or relating to containers |
DE60201142T2 (de) * | 2001-04-20 | 2005-10-20 | Kuraray Co., Ltd., Kurashiki | Wasserlösliche Folie und Verpackung, welche dieselbe verwendet |
WO2003055938A1 (fr) * | 2001-12-27 | 2003-07-10 | The Nippon Synthetic Chemical Industry Co., Ltd. | Film a base de poly(alcool de vinyle) |
JP4056859B2 (ja) | 2002-11-11 | 2008-03-05 | 日本合成化学工業株式会社 | 水溶性フィルム |
EP1640444A1 (en) * | 2004-09-17 | 2006-03-29 | The Procter & Gamble Company | Water-soluble, liquid-containing pouch |
CN101792535B (zh) * | 2004-11-02 | 2012-02-22 | 日本合成化学工业株式会社 | 聚乙烯醇膜及其生产方法 |
CN101091127B (zh) * | 2004-12-28 | 2010-09-08 | 日本合成化学工业株式会社 | 聚乙烯醇膜和使用它的偏振膜和偏振板 |
GB2442626A (en) * | 2005-06-16 | 2008-04-09 | Nippon Synthetic Chem Ind | Water-soluble film |
US7745517B2 (en) * | 2006-05-02 | 2010-06-29 | Sekisui Specialty Chemicals America, Llc | Polyvinyl alcohol films with improved resistance to oxidizing chemicals |
US20080110370A1 (en) | 2006-11-13 | 2008-05-15 | Verrall Andrew P | Water-soluble film |
US20080176985A1 (en) | 2006-11-13 | 2008-07-24 | Verrall Andrew P | Water-soluble film |
JP2009001009A (ja) * | 2007-05-22 | 2009-01-08 | Nippon Synthetic Chem Ind Co Ltd:The | 液圧転写印刷用ベースフィルム、液圧転写印刷用ベースフィルムの製造方法および液圧転写方法 |
TWI689547B (zh) * | 2014-10-13 | 2020-04-01 | 美商摩諾索公司 | 具有塑化劑摻合物的水溶性聚乙烯醇膜、相關方法及相關物品 |
RU2675519C2 (ru) * | 2014-10-13 | 2018-12-19 | Дзе Проктер Энд Гэмбл Компани | Изделия, содержащие водорастворимую пленку на основе смеси поливиниловых спиртов, и способы их изготовления |
EP3348604A4 (en) * | 2015-09-11 | 2019-05-15 | The Nippon Synthetic Chemical Industry Co., Ltd. | WATER-SOLUBLE FILM AND CHEMICAL PACKAGING BODY |
WO2017043510A1 (ja) * | 2015-09-11 | 2017-03-16 | 日本合成化学工業株式会社 | 液体洗剤包装用水溶性フィルム及び液体洗剤包装体 |
US20180251615A1 (en) * | 2015-09-11 | 2018-09-06 | The Nippon Synthetic Chemical Industry Co., Ltd. | Water-soluble film and chemical agent package |
JPWO2017043513A1 (ja) * | 2015-09-11 | 2018-06-21 | 日本合成化学工業株式会社 | 水溶性フィルム、薬剤包装体及び水溶性フィルムの製造方法 |
-
2016
- 2016-09-07 CN CN201680046684.6A patent/CN107922645B/zh active Active
- 2016-09-07 EP EP16844370.3A patent/EP3348605A4/en not_active Withdrawn
- 2016-09-07 JP JP2016556036A patent/JP6805828B2/ja active Active
- 2016-09-07 KR KR1020187003884A patent/KR102516145B1/ko active IP Right Grant
- 2016-09-07 US US15/753,693 patent/US10696934B2/en active Active
- 2016-09-07 WO PCT/JP2016/076258 patent/WO2017043509A1/ja active Application Filing
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002301899A (ja) * | 2001-04-04 | 2002-10-15 | Nippon Synthetic Chem Ind Co Ltd:The | 転写印刷用ベースフィルム |
JP2009051947A (ja) * | 2007-08-27 | 2009-03-12 | Nippon Synthetic Chem Ind Co Ltd:The | 農薬包装用水溶性フィルム |
JP2013518173A (ja) * | 2010-01-29 | 2013-05-20 | モノソル リミテッド ライアビリティ カンパニー | Pvohポリマーのブレンド材を有する改良された水溶性フィルムおよびそれで作られたパケット |
WO2015098979A1 (ja) * | 2013-12-25 | 2015-07-02 | 株式会社クラレ | 変性ポリビニルアルコールおよびそれを含有する水溶性フィルム |
Non-Patent Citations (1)
Title |
---|
See also references of EP3348605A4 * |
Cited By (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110785879A (zh) * | 2017-06-07 | 2020-02-11 | 株式会社可乐丽 | 非水电解质电池用粘合剂组合物、以及使用其的非水电解质电池用粘合剂水溶液、非水电解质电池用浆料组合物、非水电解质电池用电极及非水电解质电池 |
CN110785879B (zh) * | 2017-06-07 | 2023-01-17 | 株式会社可乐丽 | 非水电解质电池用粘合剂组合物 |
CN110603285B (zh) * | 2017-06-12 | 2022-08-09 | 三菱化学株式会社 | 水溶性薄膜和药剂包装体、以及水溶性薄膜的制造方法 |
EP3640285A4 (en) * | 2017-06-12 | 2020-06-03 | Mitsubishi Chemical Corporation | WATER-SOLUBLE FILM, MEDICAL PACKAGING AND METHOD FOR PRODUCING WATER-SOLUBLE FILM |
US11649420B2 (en) | 2017-06-12 | 2023-05-16 | Mitsubishi Chemical Corporation | Water-soluble film, chemical agent package, and method of producing water-soluble film |
CN110603285A (zh) * | 2017-06-12 | 2019-12-20 | 三菱化学株式会社 | 水溶性薄膜和药剂包装体、以及水溶性薄膜的制造方法 |
JP7099273B2 (ja) | 2017-11-20 | 2022-07-12 | 三菱ケミカル株式会社 | ポリビニルアルコール系水溶性フィルム及びその製造方法、ならびに薬剤包装体 |
JP2019094490A (ja) * | 2017-11-20 | 2019-06-20 | 日本合成化学工業株式会社 | ポリビニルアルコール系水溶性フィルム及びその製造方法、ならびに薬剤包装体 |
JPWO2019189685A1 (ja) * | 2018-03-29 | 2021-02-12 | 三菱ケミカル株式会社 | 水溶性フィルム及びその製造方法、並びに薬剤包装体 |
EP3778732A4 (en) * | 2018-03-29 | 2021-05-26 | Mitsubishi Chemical Corporation | WATER SOLUBLE FILM, ITS PRODUCTION PROCESS AND PHARMACEUTICAL PACKAGING |
CN111819229A (zh) * | 2018-03-29 | 2020-10-23 | 三菱化学株式会社 | 水溶性薄膜及其制造方法、以及药剂包装体 |
WO2019189685A1 (ja) | 2018-03-29 | 2019-10-03 | 三菱ケミカル株式会社 | 水溶性フィルム及びその製造方法、並びに薬剤包装体 |
JP7238769B2 (ja) | 2018-03-29 | 2023-03-14 | 三菱ケミカル株式会社 | 水溶性フィルム及びその製造方法、並びに薬剤包装体 |
US11634547B2 (en) | 2018-03-29 | 2023-04-25 | Mitsubishi Chemical Corporation | Water-soluble film, production method thereof, and chemical agent package |
JPWO2020138444A1 (ja) * | 2018-12-28 | 2021-11-04 | 株式会社クラレ | 水溶性フィルムおよび包装体 |
JP7240422B2 (ja) | 2018-12-28 | 2023-03-15 | 株式会社クラレ | 水溶性フィルムおよび包装体 |
WO2020138444A1 (ja) * | 2018-12-28 | 2020-07-02 | 株式会社クラレ | 水溶性フィルムおよび包装体 |
CN113174071A (zh) * | 2021-04-26 | 2021-07-27 | 东北林业大学 | 一种阴离子多糖膜的压封方法 |
US11970588B2 (en) | 2021-04-26 | 2024-04-30 | Northeast Forestry University | Press-sealing method of anionic polysaccharide films |
Also Published As
Publication number | Publication date |
---|---|
KR20180054567A (ko) | 2018-05-24 |
US10696934B2 (en) | 2020-06-30 |
US20180245028A1 (en) | 2018-08-30 |
JP6805828B2 (ja) | 2020-12-23 |
CN107922645A (zh) | 2018-04-17 |
KR102516145B1 (ko) | 2023-03-30 |
EP3348605A4 (en) | 2019-05-29 |
CN107922645B (zh) | 2021-08-03 |
JPWO2017043509A1 (ja) | 2018-06-28 |
EP3348605A1 (en) | 2018-07-18 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2017043509A1 (ja) | 水溶性フィルム、薬剤包装体及び水溶性フィルムの製造方法 | |
WO2017043513A1 (ja) | 水溶性フィルム、薬剤包装体及び水溶性フィルムの製造方法 | |
US10414889B2 (en) | Water-soluble film and chemical agent package | |
JP6729279B2 (ja) | 水溶性フィルム及び薬剤包装体 | |
WO2017043511A1 (ja) | 水溶性フィルム及び薬剤包装体 | |
WO2018230583A1 (ja) | 水溶性フィルム及び薬剤包装体、ならびに水溶性フィルムの製造方法 | |
WO2017043510A1 (ja) | 液体洗剤包装用水溶性フィルム及び液体洗剤包装体 | |
JPWO2018123892A1 (ja) | 水溶性フィルムおよび薬剤包装体 | |
WO2017043505A1 (ja) | 水溶性フィルム及び薬剤包装体 | |
JP2022125059A (ja) | 水溶性フィルム及び薬剤包装体 | |
JP2017119853A (ja) | 水溶性フィルム、薬剤包装体及び水溶性フィルムの製造方法 | |
JP2017095679A (ja) | 水溶性フィルム及び薬剤包装体 | |
JP2017119434A (ja) | 水溶性フィルム、薬剤包装体及び水溶性フィルムの製造方法 | |
JP2017106002A (ja) | 水溶性フィルム及び薬剤包装体 | |
JP2017115128A (ja) | 水溶性フィルム及び薬剤包装体 | |
JP2017110213A (ja) | 薬剤包装体及び薬剤包装体の製造方法 | |
WO2017043506A1 (ja) | 水溶性フィルム及び薬剤包装体 | |
JP2017119851A (ja) | 水溶性フィルム及び薬剤包装体 | |
JP2017106008A (ja) | 水溶性フィルム及び薬剤包装体 | |
WO2017043514A1 (ja) | フィルムロール及び薬剤包装体 | |
WO2017043512A1 (ja) | 水溶性フィルム及び薬剤包装体 | |
JP2018104563A (ja) | 水溶性フィルム及び薬剤包装体 | |
WO2017043507A1 (ja) | 水溶性フィルムおよびそれを用いた薬剤包装体、並びに水溶性フィルムの製造方法 | |
JP2017100806A (ja) | 水溶性フィルム及び薬剤包装体 | |
JP2017115123A (ja) | 水溶性フィルム及び薬剤包装体 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
ENP | Entry into the national phase |
Ref document number: 2016556036 Country of ref document: JP Kind code of ref document: A |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 16844370 Country of ref document: EP Kind code of ref document: A1 |
|
ENP | Entry into the national phase |
Ref document number: 20187003884 Country of ref document: KR Kind code of ref document: A |
|
WWE | Wipo information: entry into national phase |
Ref document number: 15753693 Country of ref document: US |
|
NENP | Non-entry into the national phase |
Ref country code: DE |