WO2012114810A1 - ポリ乳酸系フィルム - Google Patents
ポリ乳酸系フィルム Download PDFInfo
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- WO2012114810A1 WO2012114810A1 PCT/JP2012/051421 JP2012051421W WO2012114810A1 WO 2012114810 A1 WO2012114810 A1 WO 2012114810A1 JP 2012051421 W JP2012051421 W JP 2012051421W WO 2012114810 A1 WO2012114810 A1 WO 2012114810A1
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- resin
- polylactic acid
- mass
- film
- filler
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
- C08L67/04—Polyesters derived from hydroxycarboxylic acids, e.g. lactones
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- 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
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L101/00—Compositions of unspecified macromolecular compounds
- C08L101/16—Compositions of unspecified macromolecular compounds the macromolecular compounds being biodegradable
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
- C08L67/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
-
- 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
- C08J2367/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
- C08J2367/04—Polyesters derived from hydroxy carboxylic acids, e.g. lactones
-
- 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
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
- C08K3/24—Acids; Salts thereof
- C08K3/26—Carbonates; Bicarbonates
- C08K2003/265—Calcium, strontium or barium carbonate
-
- 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
- C08K9/00—Use of pretreated ingredients
- C08K9/04—Ingredients treated with organic substances
Definitions
- the present invention relates to a polylactic acid film excellent in flexibility, heat resistance, bleed-out resistance and durability, and excellent in workability such as stretching and embossing for expressing good moisture permeability.
- Patent Document 1 discloses a porous sheet obtained by stretching at least uniaxially a sheet containing a polylactic acid resin, a filler, and a general polyester plasticizer.
- Patent Document 2 discloses a polylactic acid polymer, an aliphatic aromatic copolymer polyester, an aliphatic polycarboxylic acid ester, an aliphatic polyhydric alcohol ester, an aliphatic polyhydric alcohol ether, and an oxyester.
- a porous film is disclosed in which fine powder fillers are blended with general plasticizers selected to form pores. JP 2007-112867 A JP 2004-149679 A
- Patent Document 1 and Patent Document 2 described above were inferior in processability although a flexible film having biodegradation and a high biomass degree was obtained.
- the present invention is excellent in flexibility, heat resistance, bleed-out resistance, durability, and excellent workability such as stretching and embossing for expressing good moisture permeability, It is intended to provide a polylactic acid film.
- the first aspect of the present invention is as follows. 1) A film comprising a composition comprising a polylactic acid resin as the resin (A), a thermoplastic resin other than the polylactic acid resin as the resin (B), and a compound treated with a surface treating agent as the filler (C).
- the polylactic acid resin includes a crystalline polylactic acid resin and an amorphous polylactic acid resin, In a total of 100% by mass of the resin (A) and the resin (B), the resin (A) is contained in an amount of 10 to 95% by mass, the resin (B) is contained in an amount of 5 to 90% by mass, and the resin (A) and the resin (B) A polylactic acid film comprising a composition containing 10 to 400 parts by mass of filler (C) with respect to 100 parts by mass in total. 2) The polylactic acid film according to 1), wherein the surface treatment agent is a phosphate ester compound and / or a fatty acid.
- the filler (C) is obtained by treating the inorganic filler and / or organic filler with a surface treatment agent, and the ratio of the inorganic filler and / or organic filler.
- the surface area S (m 2 / g) and the mass ratio T (mass%) of the portion derived from the surface treating agent in the filler (C) satisfy the following conditions: 1) to 3)
- the resin (B) is a block copolymer having a polyether segment and a polylactic acid segment, a block copolymer having a polyester segment and a polylactic acid segment, an aliphatic polyester resin, and an aliphatic fragrance
- the resin (B) is at least one resin selected from the group consisting of a block copolymer having a polyether segment and a polylactic acid segment and a block copolymer having a polyester segment and a polylactic acid segment
- the polylactic acid film according to 5 which comprises at least one resin selected from the group consisting of aliphatic polyester resins and aliphatic aromatic polyester resins.
- the polylactic acid system according to any one of 1) to 6 which is obtained using a composition obtained by reacting a reactive compound with the resin (A) and / or the resin (B). the film.
- the second aspect of the present invention is as follows. 10) A film comprising a polylactic acid resin as the resin (A) and a composition containing 10 to 400 parts by mass of the filler (C) and / or the filler (D) with respect to 100 parts by mass in total of the resin.
- the filler (C) is a compound treated with a surface treatment agent
- the filler (D) is an inorganic filler and / or an organic filler that has not been treated with a surface treatment agent
- a polylactic acid-based film having excellent flexibility, heat resistance, bleed-out resistance, durability, and excellent workability such as stretching and embossing for expressing good moisture permeability.
- the polylactic acid-based film of the present invention is mainly used for medical / hygienic materials such as bed sheets, pillow covers, sanitary napkins, and back sheets of absorbent articles such as disposable diapers, which require flexibility, moisture permeability, and heat resistance.
- Film for processing such as stretching and embossing to obtain clothing materials such as clothing, gloves, clothing materials, garbage bags and compost bags, food bags such as vegetables and fruits, bags for various industrial products, etc. Can be preferably used.
- the present invention relates to a polylactic acid film having the above-mentioned problems, that is, excellent flexibility, heat resistance, bleed-out resistance, durability, and excellent workability such as stretching and embossing for expressing good moisture permeability.
- the present inventors have succeeded in solving such a problem for the first time by using a compound having a specific resin and a filler and further using a compound treated with a surface treatment agent as a filler. That is, in the first aspect of the present invention, a compound treated with a polylactic acid resin as the resin (A), a thermoplastic resin other than the polylactic acid resin as the resin (B), and a surface treatment agent as the filler (C) is used.
- the polylactic acid resin includes a crystalline polylactic acid resin and an amorphous polylactic acid resin, and the resin (A) and the resin (B) are 100% by mass in total. 10 to 95% by mass of (A), 5 to 90% by mass of resin (B), and 10 to 400% of filler (C) with respect to 100 parts by mass in total of resin (A) and resin (B).
- a polylactic acid film comprising a composition containing parts by mass.
- the polylactic acid film according to the first aspect of the present invention will be described below.
- the resin (A) means a polylactic acid resin.
- the polylactic acid-based resin is a polymer having an L-lactic acid unit and / or a D-lactic acid unit as main constituent components.
- the main component means that the mass ratio of the lactic acid unit is the maximum in 100% by mass of the polymer.
- the mass ratio of the lactic acid unit is preferably 70% by mass to 100% by mass of the lactic acid unit in 100% by mass of the polymer.
- poly-L-lactic acid as used in the present invention refers to those in which the content of L-lactic acid units is more than 50 mol% and not more than 100 mol% in 100 mol% of all lactic acid units in the polylactic acid polymer.
- poly-D-lactic acid as used in the present invention refers to those having a D-lactic acid unit content of more than 50 mol% and not more than 100 mol% in 100 mol% of all lactic acid units in the polylactic acid polymer.
- Poly L-lactic acid changes in the crystallinity of the resin itself depending on the content ratio of the D-lactic acid unit. That is, if the content ratio of D-lactic acid units in poly-L-lactic acid increases, the crystallinity of poly-L-lactic acid decreases and approaches amorphous, and conversely the content ratio of D-lactic acid units in poly-L-lactic acid. As the amount decreases, the crystallinity of poly-L-lactic acid increases. Similarly, the crystallinity of the resin itself of poly D-lactic acid varies depending on the content ratio of L-lactic acid units.
- the content ratio of the L-lactic acid unit in the poly L-lactic acid used in the present invention, or the content ratio of the D-lactic acid unit in the poly D-lactic acid used in the present invention is a viewpoint for maintaining the mechanical strength of the composition. From 80 to 100 mol% is preferable in 100 mol% of all lactic acid units, and more preferably 85 to 100 mol%.
- the crystalline polylactic acid resin referred to in the present invention is a case where the polylactic acid resin is sufficiently crystallized under heating and then measured with a differential scanning calorimeter (DSC) in an appropriate temperature range.
- DSC differential scanning calorimeter
- the amorphous polylactic acid resin referred to in the present invention refers to a polylactic acid resin that does not exhibit a clear melting point when measured in the same manner.
- the composition constituting the polylactic acid film according to the first aspect of the present invention includes a crystalline polylactic acid resin and an amorphous polylactic acid resin as the polylactic acid resin of the resin (A). It is important that it be a mixture.
- the polylactic acid resin used in the present invention may be copolymerized with other monomer units other than lactic acid.
- Other monomers include ethylene glycol, propylene glycol, butanediol, heptanediol, hexanediol, octanediol, nonanediol, decanediol, 1,4-cyclohexanedimethanol, neopentyl glycol, glycerin, pentane Glycol compounds such as erythritol, bisphenol A, polyethylene glycol, polypropylene glycol and polytetramethylene glycol, oxalic acid, adipic acid, sebacic acid, azelaic acid, dodecanedioic acid, malonic acid, glutaric acid, cyclohexanedicarboxylic acid, terephthalic acid , Isophthalic acid, phthalic acid, naphthal
- the copolymerization amount of the other monomer units is preferably 0 to 30 mol%, and preferably 0 to 10 mol%, based on 100 mol% of the whole monomer units in the polymer of the polylactic acid resin. More preferably. In addition, it is preferable to select the component which has biodegradability among the above-mentioned monomer units according to a use.
- the polylactic acid resin used in the present invention is mixed with a small amount of poly D-lactic acid when the main component is poly L-lactic acid, and a small amount of poly L-lactic acid when the main component is poly D-lactic acid. It is also preferable. This is because the stereocomplex crystal formed thereby has a higher melting point than a normal polylactic acid crystal ( ⁇ crystal), so that the heat resistance of the film is improved.
- the mass average molecular weight of the polylactic acid mixed in a small amount is preferably smaller than the mass average molecular weight of the main component polylactic acid from the viewpoint of efficiently forming a stereocomplex crystal.
- the mass average molecular weight of the polylactic acid mixed in a small amount is preferably 0.5 to 50%, more preferably 1 to 40%, more preferably 2 to 30% of the mass average molecular weight of the main component polylactic acid. More preferably it is.
- the mass average molecular weight of the polylactic acid resin used in the present invention is preferably 50,000 to 500,000, more preferably 80,000 to 400,000 in order to satisfy practical mechanical properties. More preferably, it is ⁇ 300,000.
- the mass average molecular weight as used herein refers to a molecular weight calculated by a polymethyl methacrylate conversion method after measurement with a chloroform solvent by gel permeation chromatography (GPC).
- polylactic acid-based resin As a method for producing the polylactic acid-based resin, details will be described later, but a known polymerization method can be used, and examples thereof include a direct polymerization method from lactic acid and a ring-opening polymerization method via lactide.
- the content of the resin (A) contained in the composition constituting the polylactic acid film of the present invention is 10 to 95% by mass in a total of 100% by mass of the resin (A) and the resin (B) described later. is important. When the resin (A) is less than 10% by mass in a total of 100% by mass of the resin (A) and the resin (B), heat resistance and bleed-out resistance are insufficient, and when it exceeds 95% by mass, flexibility is insufficient. .
- the content of the resin (A) is preferably 20 to 90% by mass, more preferably 30 to 85% by mass, based on a total of 100% by mass of the resin (A) and the resin (B) described later. It is particularly preferably 40 to 80% by mass.
- the content of the resin (A) in the entire composition constituting the polylactic acid film of the present invention is preferably 5 to 80% by mass, more preferably 15 to 70% by mass, and 25 to The amount is more preferably 60% by mass, and particularly preferably 35 to 50% by mass.
- Resin (B) thermoplastic resin other than polylactic acid resin
- the polylactic acid film of the present invention is composed of a composition containing the resin (B).
- the resin (B) is a thermoplastic resin other than the polylactic acid resin.
- Thermoplastic resins other than polylactic acid resins include polyacetal, polyethylene, polypropylene, polyamide, poly (meth) acrylate, polyphenylene sulfide, polyetheretherketone, polyester, polyurethane, polyisoprene, polysulfone, polyphenylene oxide, polyimide, polyether Imide, ethylene / glycidyl methacrylate copolymer, polyester elastomer, polyamide elastomer, ethylene / propylene terpolymer, ethylene / butene-1 copolymer, thermoplastic starch, starch-containing polymer, various resin plasticizers, etc. can be used .
- polyester as the resin (B) include aromatic polyester resins such as polyethylene terephthalate, polypropylene terephthalate and polybutylene terephthalate, poly (ethylene succinate / terephthalate), poly (butylene succinate / terephthalate), poly ( Aliphatic aromatic polyester resins such as butylene adipate and terephthalate), polyglycolic acid, poly (3-hydroxybutyrate), poly (3-hydroxybutyrate ⁇ 3-hydroxyhexanoate), poly (3-hydroxybutyrate) (Rate 3-hydroxyvalerate), polycaprolactone, polybutylene succinate, poly (butylene succinate adipate), and other aliphatic polyester resins can be used.
- the thermoplastic resin other than the polylactic acid resin as the resin (B) includes aliphatic aromatic polyester resins and aliphatic polyester resins. Is preferred.
- resin plasticizers include polyesters such as polypropylene glycol and sebacic acid esters, polyalkylene ethers, ether esters, and acrylate plasticizers.
- the solubility parameter SP of the resin plasticizer that is the resin (B) contained in the composition constituting the polylactic acid film is (16 to 23) 1/2 MJ / m 3 is preferable, and (17 to 21) 1/2 MJ / m 3 is more preferable.
- the method for calculating the solubility parameter is described in P.A. Small, J.M. Appl. Chem. 3, 71 (1953).
- the resin-based plasticizer as the resin (B) preferably has biodegradability from the viewpoint of maintaining the biodegradability of the entire film.
- resin plasticizer As a resin plasticizer as resin (B) It is preferably a plasticizer approved by the US Food and Sanitation Administration (FDA), the Sanitation Council for Polyolefins, and the like.
- the resin-based plasticizer as the resin (B) used in the present invention has, for example, a number average molecular weight of 1,000 or more.
- Polyethylene glycol or the like is preferably solid at room temperature (20 ° C. ⁇ 15 ° C.), that is, the melting point exceeds 35 ° C.
- 150 degreeC is an upper limit at the point which matches melt processing temperature with thermoplastic resins other than polylactic acid-type resin and polylactic acid-type resin.
- the resin plasticizer as the resin (B) used in the present invention is a block copolymer having a polyether segment and a polylactic acid segment, or a polyester segment and a polylactic acid segment. More preferably, it is a block copolymer.
- the plasticizing component is a polyether segment or a polyester segment.
- a polyester-type segment means the segment which consists of polyesters other than polylactic acid.
- the mass ratio of the polylactic acid segment contained in the block copolymer plasticizer is preferably 45% by mass or less of the entire block copolymer plasticizer, because a desired flexibility can be imparted with a smaller amount of addition, preferably 5 mass. % Or more is preferable from the viewpoint of suppressing bleed-out.
- the number average molecular weight of the polylactic acid segment in one molecule of the block copolymer plasticizer is preferably 1,200 to 10,000.
- the block copolymer plasticizer that is the resin (B) is 1,200 or more
- the block copolymer plasticizer that is the resin (B) and the resin (A) (polylactic acid resin) A sufficient affinity is produced between the polylactic acid segment and a part of the polylactic acid segment is taken into a crystal formed from the resin (A) (polylactic acid resin) to form a so-called eutectic
- the block copolymer plasticizer, which is the resin (B) is bonded to the resin (A), and the block copolymer plasticizer exhibits a great effect in suppressing bleed-out. As a result, the blocking resistance of the film is also excellent.
- this block copolymer plasticizer is greatly superior in moisture permeability after processing of the film, compared with a plasticizer that is liquid at room temperature and a plasticizer that does not form a eutectic even when in solid form at room temperature. This is because the eutectic formed improves the hole formation efficiency by processing (stretching, embossing, etc.) described later.
- the number average molecular weight of the polylactic acid segment in the block copolymer plasticizer is more preferably 1,500 to 6,000, and further preferably 2,000 to 5,000.
- the polylactic acid segment contained in the block copolymer plasticizer is such that L-lactic acid is 95 to 100% by mass or D-lactic acid is 95 to 100% by mass, and bleeding out is particularly suppressed. Therefore, it is preferable.
- the resin (A) is a polylactic acid resin
- the polylactic acid resin is a polymer having an L-lactic acid unit and / or a D-lactic acid unit as main constituent components.
- the mass ratio of the lactic acid unit is 5% by mass to 45% by mass, and the mass ratio of the polyether segment or the polyester segment is 55%. % By mass to 95% by mass.
- the plasticizing component of the block copolymer plasticizer which is the resin (B) is a polyether segment or a polyester segment.
- the polyether segment is more flexible with a small amount of addition. It is preferable from a viewpoint which can provide. Furthermore, from the same viewpoint, it is more preferable to have a segment made of polyalkylene ether as the polyether segment.
- examples of the polyether-based segment include a segment made of polyethylene glycol, polypropylene glycol, polytetramethylene glycol, polyethylene glycol / polypropylene glycol copolymer, and the like.
- a segment made of polyethylene glycol is a resin (A ) (Polylactic acid resin) has high affinity and is excellent in reforming efficiency, and is particularly preferable because desired flexibility can be imparted by adding a small amount of plasticizer.
- the block copolymer plasticizer has a segment composed of a polyalkylene ether
- the polyalkylene ether segment tends to be easily oxidized or thermally decomposed when heated at the time of molding, etc. It is preferable to use a hindered amine-based antioxidant or a phosphorus-based heat stabilizer in combination.
- polyester-based segment polyglycolic acid, poly (3-hydroxybutyrate), poly (3-hydroxybutyrate-3hydroxyvalerate), polycaprolactone, or ethylene glycol
- Polyesters composed of aliphatic diols such as propanediol, butanediol, polyethylene glycol, and polypropylene glycol, and aliphatic dicarboxylic acids such as succinic acid, sebacic acid, and adipic acid are preferably used as the polyester-based segment.
- the block copolymer plasticizer may contain both the polyether segment and the polyester segment in one molecule, or may be either one of the components. From the viewpoint of plasticizer productivity, cost, and the like, when using any one component, it is preferable to use a polyether-based segment from the viewpoint that desired flexibility can be imparted by adding a smaller amount of the plasticizer. That is, a preferred embodiment as a block copolymer plasticizer is a block copolymer of a polyether segment and a polylactic acid segment.
- the number average molecular weight of the polyether segment or the polyester segment in one molecule of the block copolymer plasticizer is preferably 7,000 to 20,000.
- the composition constituting the polylactic acid film has sufficient flexibility, and the melt viscosity is moderate when the composition containing the resin (A) (polylactic acid resin) is used. It is possible to stabilize the film forming processability such as the inflation film forming method.
- each segment block of the polyether-based and / or polyester-based segment and the polylactic acid segment is blocked from the viewpoint of more effectively suppressing bleed out. It is preferably at the end of the copolymer plasticizer molecule. Most preferably, the block of polylactic acid segment is at both ends of the block copolymer plasticizer molecule.
- polyethylene glycol having a hydroxyl terminal at both ends (hereinafter, polyethylene glycol is referred to as PEG) is employed as the polyether segment will be specifically described.
- the number average molecular weight of PEG having hydroxyl ends at both ends (hereinafter, the number average molecular weight of PEG is referred to as MPEG ) is usually calculated from the hydroxyl value determined by a neutralization method or the like in the case of a commercially available product.
- MPEG number average molecular weight of PEG having hydroxyl ends at both ends
- lactide w L parts by mass are added to w E parts by mass of PEG having hydroxyl groups at both ends
- lactide is subjected to ring-opening addition polymerization at both hydroxyl groups of PEG and sufficiently reacted, so that PLA is substantially obtained.
- a block copolymer of the -PEG-PLA type can be obtained (where PLA stands for polylactic acid).
- the number average molecular weight of one polylactic acid segment of this block copolymer plasticizer can be substantially determined as (1/2) ⁇ (w L / w E ) ⁇ M PEG .
- the mass percentage of the total block copolymer plasticizer of the polylactic acid segment component can be substantially determined as 100 ⁇ w L / (w L + w E)%.
- the mass ratio of the plasticizer component excluding the polylactic acid segment component to the entire block copolymer plasticizer can be determined to be substantially 100 ⁇ w E / (w L + w E )%.
- the content of the resin (B) in the composition constituting the polylactic acid-based film of the present invention is 5 to 90% by mass in a total of 100% by mass of the resin (A) and the resin (B). is there. When it is less than 5% by mass, the flexibility is insufficient, and when it exceeds 90% by mass, the heat resistance and bleed-out resistance are insufficient.
- the content of the resin (B) is preferably 10 to 80% by mass, more preferably 15 to 70% by mass, based on a total of 100% by mass of the resin (A) and the resin (B). It is especially preferable that it is 60 mass%.
- the polylactic acid film of the present invention may contain only one kind of these resins (B), or may contain two or more kinds in combination.
- Thermoplastic resin groups other than the polylactic acid-type resin mentioned above as resin (B) can be combined, respectively.
- a combination of various resin-based plasticizers and a thermoplastic resin other than the resin-based plasticizer is preferable from the viewpoint of achieving both flexibility and moisture permeability after processing.
- the resin (B) is combined with various resin plasticizers and a thermoplastic resin other than the resin plasticizer, the moisture permeability after processing is dramatically improved. It was.
- the block copolymer plasticizer described above that is, a block having a polyether-based segment and a polylactic acid segment. It is preferably a copolymer or a block copolymer having a polyester-based segment and a polylactic acid segment. More preferably, it is a block copolymer having a polyether segment and a polylactic acid segment.
- thermoplastic resins other than resin plasticizers aliphatic polyester resins and aliphatic aromatic polyester resins are preferred from the viewpoint of biodegradability.
- Aliphatic polyester resins include polyglycolic acid, poly (3-hydroxybutyrate), poly (3-hydroxybutyrate-3hydroxyvalerate), poly (3-hydroxybutyrate-3hydroxyhexanoate) ), Polycaprolactone, polybutylene succinate, and poly (butylene succinate adipate) are more preferable.
- examples of aliphatic aromatic polyester resins include poly (ethylene succinate terephthalate), poly (butylene succinate terephthalate), Poly (butylene adipate terephthalate) is more preferred.
- poly (3-hydroxybutyrate ⁇ 3-hydroxyhexanoate), poly (butylene succinate adipate), and poly (butylene adipate terephthalate) are more preferable.
- the resin (B) is a block copolymer having a polyether segment and a polylactic acid segment, a block copolymer having a polyester segment and a polylactic acid segment, an aliphatic polyester resin, and an aliphatic group.
- a block copolymer having a polyether segment and a polylactic acid segment and a block copolymer having a polyester segment and a polylactic acid segment are preferable, although at least one resin selected from the group consisting of aromatic polyester resins is preferable.
- resin-based plasticizer selected from the group consisting of polymers
- resin-based plastics selected from the group consisting of aliphatic polyester-based resins and aliphatic aromatic polyester-based resins.
- the resin (A) (polylactic acid resin) includes a crystalline polylactic acid resin and an amorphous polylactic acid resin.
- the crystalline polylactic acid resin was measured with a differential scanning calorimeter (DSC) in an appropriate temperature range after the polylactic acid resin was sufficiently crystallized under heating.
- DSC differential scanning calorimeter
- it refers to a polylactic acid resin in which a melting point derived from a polylactic acid component is observed.
- the amorphous polylactic acid resin refers to a polylactic acid resin that does not exhibit a clear melting point when the same measurement is performed.
- the heat resistance of the film is insufficient.
- a block copolymer plasticizer is used as the above-mentioned various plasticizers, a co-crystal can be formed with the polylactic acid segment of the block copolymer plasticizer unless it contains a crystalline polylactic acid resin. Therefore, the bleed-out resistance is insufficient.
- the polylactic acid resin as the resin (A) does not contain an amorphous polylactic acid resin, the flexibility and bleed-out resistance of the film is insufficient. This has the effect of not providing an amorphous portion in which the plasticizer can be dispersed.
- the crystalline polylactic acid-based resin used in the polylactic acid-based film of the present invention has a content ratio of L-lactic acid units in poly-L-lactic acid or poly-D-lactic acid from the viewpoint of improving heat resistance and blocking resistance.
- the content ratio of D-lactic acid units is preferably 96 to 100 mol%, more preferably 98 to 100 mol% in 100 mol% of all lactic acid units.
- the amount of the resin (A) in the composition constituting the polylactic acid film of the present invention is 100% by mass (the total of the crystalline polylactic acid resin and the amorphous polylactic acid resin is 100% by mass) ),
- the ratio of the crystalline polylactic acid-based resin is preferably 5 to 60% by mass, more preferably 10 to 50% by mass, and still more preferably 20 to 40% by mass.
- Fill (C) In order to improve the moisture permeability after processing, it is important that the polylactic acid film of the present invention comprises a composition containing a compound treated with a surface treatment agent as a filler (C).
- An inorganic filler and / or an organic filler can be used as the compound which is a precursor of the filler (C) and before being treated with the surface treatment agent.
- an inorganic filler and / or an organic filler is a substance added as a base material in order to develop various properties, or an inert substance (inactive substance added for the purpose of increasing the volume, increasing the volume, reducing the cost of the product, etc.). Active inorganic compounds and organic compounds).
- inorganic fillers include various carbonates such as calcium carbonate, magnesium carbonate and barium carbonate, various sulfates such as magnesium sulfate, barium sulfate and calcium sulfate, zinc oxide, silicon oxide (silica), zirconium oxide and magnesium oxide.
- oxides such as calcium oxide, titanium oxide, magnesium oxide, iron oxide, alumina, hydroxide such as aluminum hydroxide, magnesium hydroxide, silicate mineral, hydroxyapatite, mica, talc, kaolin, clay, montmorillonite, Zeolite, metal ion-carrying zeolite, wollastonite, potassium titanate, boroaluminum, zepiolite and other complex oxides, lithium phosphate, calcium phosphate, magnesium phosphate and other phosphates, lithium chloride, lithium fluoride, etc.
- organic fillers examples include oxalates such as calcium oxalate, terephthalates such as calcium, barium, zinc, manganese and magnesium, vinyl monomers such as divinylbenzene, styrene, acrylic acid and methacrylic acid alone or Copolymer fine particles, polytetrafluoroethylene, benzoguanamine resin, thermosetting epoxy resin, unsaturated polyester resin, thermosetting urea resin, thermosetting phenol resin and other organic fine particles, wood powder and pulp powder Plants such as powder, rice husk, wood chip, okara, waste paper ground material, clothing ground material, cotton fiber, hemp fiber, bamboo fiber, wood fiber, kenaf fiber, jute fiber, banana fiber, coconut fiber, etc. Fiber, silk, wool, angora, cashmere, camel and other animal fibers, polyester fiber, Niro Fibers, and the like can be used synthetic fibers such as acrylic fibers.
- oxalates such as calcium oxalate
- terephthalates such as
- various properties other than moisture permeability after processing are expressed.
- silicon oxide (silica), talc, calcium carbonate, etc. as a filler that expresses flame retardancy, aluminum hydroxide, magnesium hydroxide, etc., express UV absorption Zinc oxide, titanium oxide and other fillers that exhibit antibacterial properties such as zeolite, metal ion (silver ion, etc.)-Supported zeolite, zinc oxide, titanium oxide, metal phthalocyanine, and other fillers that exhibit deodorizing properties
- Zeolite, metal ion (eg, silver ion) -supported zeolite, activated carbon, bamboo charcoal, and zepiolite can be used.
- the filler (C) of the present invention can be obtained by treating the aforementioned inorganic filler and / or organic filler with a surface treatment agent.
- Surface treatment agents used to obtain the filler (C) include phosphate ester compounds, fatty acids, resin acids, surfactants, fats and oils, waxes, carboxylic acid coupling agents, silane coupling agents, and titanate cups. Ring agents, polymer surface treatment agents, and the like can be used.
- the affinity with the matrix resin is improved, and it is effective in suppressing the aggregation of the filler and improving the dispersibility. It becomes possible to uniformly disperse the filler. As a result, it becomes possible to obtain a film excellent in processability such as stretching and embossing for expressing good moisture permeability.
- the surface treatment method is not particularly limited, but a method of physically mixing the surface treatment agent and the compound (inorganic filler and / or organic filler) before being treated with the surface treatment agent, toluene A method of mixing in a solvent such as can be employed. Among these, the method of physically mixing from a practical side is preferable.
- the physical mixing method is not particularly limited, and various pulverizers such as a roll rolling mill, a high-speed rotary pulverizer, a ball mill, a jet mill, etc.
- a method of surface treatment with a surface treatment agent while pulverizing a compound before treatment, or a container rotating mixer in which the container itself rotates, a container having rotating blades in a fixed container, or a container fixed mixer in which an air current is blown The method of surface-treating using etc. can be mentioned.
- a mixer such as a nauta mixer, a ribbon mixer, or a Henschel mixer is preferable.
- the treatment conditions at that time are not particularly limited, and when the filler (C) is added to and blended with the matrix resin (resin (A) and resin (B)), the matrix resin (resin (A) and resin)
- the treatment temperature is preferably 30 ° C. or higher. Further, it is preferably 50 ° C. or higher, particularly 90 ° C. or higher.
- the treatment time is preferably within 5 hours, more preferably within 3 hours, particularly preferably within 2 hours.
- the filler (C) of the present invention is obtained by treating the inorganic filler and / or organic filler with a surface treatment agent, and the ratio of the inorganic filler and / or organic filler. It is preferable that the surface area S (m 2 / g) and the mass ratio T (mass%) of the portion derived from the surface treatment agent in the filler (C) satisfy the following conditions.
- T / S is 0.15 or more, the effect of the surface treatment agent described above can be maximized.
- T / S is more preferably 0.20 or more, and further preferably 0.25 or more.
- T / S is 0.45 or less, it becomes possible to suppress degradation of the matrix resin (resin (A) and resin (B)) due to excessive surface treatment agent such as hydrolysis and oxidative degradation. That is, it is preferable because durability is improved.
- T / S is more preferably 0.40 or less.
- phosphate ester compound When a phosphate ester compound is used as the surface treatment agent, phosphate ester, phosphite ester, pyrophosphate ester or the like can be used as the phosphate ester compound.
- phosphate ester, phosphite ester, pyrophosphate ester or the like There may be two or more phosphorus atoms in one molecule, and it may be preferable to have an unsaturated bond in the molecule, and the unsaturated bond is a terminal double bond. May be preferred.
- a saturated fatty acid such as stearic acid, an unsaturated fatty acid such as oleic acid, linoleic acid, and the like can be used as the fatty acid.
- a resin having a carboxyl group at the terminal or main chain such as maleic acid-modified polyolefin, can be used.
- an anionic surfactant such as fatty acid soap such as stearic acid soap or sulfonic acid soap, or a nonionic surfactant such as polyethylene glycol derivative should be used as the surfactant.
- fatty acid soap such as stearic acid soap or sulfonic acid soap
- nonionic surfactant such as polyethylene glycol derivative
- soybean oil, linseed oil, etc. can be used as fats and oils.
- carnauba wax, long chain ester wax, polyethylene wax, polypropylene wax, oxides thereof, acid-modified products, and the like can be used as the wax.
- carboxylic acid coupling agent When a carboxylic acid coupling agent is used as the surface treatment agent, carboxylated polybutadiene, carboxylated polyisoprene, or the like can be used as the carboxylic acid coupling agent.
- silane coupling agent vinyl trimethoxysilane, ⁇ -glycidoxypropyltrimethoxysilane, ⁇ -methacryloxypropyltrimethoxysilane, ⁇ -aminopropyltrimethoxysilane are used as the silane coupling agent.
- N- ⁇ (aminoethyl) ⁇ -aminopropyltrimethoxysilane, N-phenyl? ⁇ -aminopropyltrimethoxysilane, ⁇ -mercaptopropyltrimethoxysilane, and the like can be used.
- titanate coupling agent an organic functional group of alkyl group + amino group type, phosphite type, pyrophosphate type, carboxylic acid type, etc. is used as the titanate coupling agent. can do.
- a polymer surface treatment agent When a polymer surface treatment agent is used as the surface treatment agent, a random or graft copolymer such as a maleic anhydride-modified polyolefin or a maleic anhydride-modified styrene-ethylene-butadiene-styrene copolymer is used as the polymer surface treatment agent.
- a polymer, a block copolymer such as propylene-acrylate, and a hydrophobic group-hydrophilic group copolymer can be used.
- the surface treatment agent used in the filler (C) of the present invention is at least selected from a phosphate ester compound, a fatty acid, a resin acid, a surfactant, a silane coupling agent, and a titanate coupling agent.
- a phosphate ester compound is at least selected from a phosphate ester compound, a fatty acid, a resin acid, a surfactant, a silane coupling agent, and a titanate coupling agent.
- One compound is preferred.
- the surface treatment agent used for the filler (C) is more preferably a phosphate ester compound and / or a fatty acid.
- thermoplastic resin other than the polylactic acid resin of the resin (B) a matrix resin (resin (A) + resin (B From the viewpoint of improving the affinity with))
- a phosphate ester compound as the surface treatment agent used in the filler (C) of the present invention.
- the surface treatment agent used when obtaining the filler (C) of the present invention preferably contains a methacrylic acid ester group.
- the methacrylic acid ester group has a high affinity with polylactic acid in the matrix resin, so it has a higher effect on suppressing the aggregation of the filler and improving the dispersibility, and more uniformly disperses the filler in the resin composition. It is because it becomes possible to do. As a result, it becomes possible to obtain a film with more excellent processability.
- the methacrylic acid ester group is more preferably at the end in the surface treatment agent molecule.
- the surface treatment agent used in obtaining the filler (C) of the present invention is at least selected from a phosphate ester compound, a fatty acid, a resin acid, a surfactant, a silane coupling agent, and a titanate coupling agent. It is preferable that it is one and further contains a methacrylic ester group. Among these, it is more preferable that they are the phosphate ester type compound containing a methacrylic ester group, and / or the fatty acid containing a methacrylic ester group.
- the average particle size of the filler (C) of the present invention is not particularly limited, but is preferably 0.01 to 10 ⁇ m.
- the film can be highly filled with the filler (C).
- the film has a high potential for improving the moisture permeability of the film, and the average particle size is 10 ⁇ m.
- processability such as extending
- the average particle diameter of the filler (C) is more preferably 0.1 to 8 ⁇ m, still more preferably 0.5 to 5 ⁇ m, and most preferably 1 to 3 ⁇ m.
- the average particle diameter means D50 (median diameter of particle diameter distribution) measured by a laser diffraction method.
- the content of the filler (C) in the composition constituting the film is 10 to 400 parts by mass with respect to 100 parts by mass in total of the resin (A) and the resin (B).
- the content of the filler (C) in the composition constituting the film is preferably 20 to 300 parts by mass, and preferably 30 to 200 parts by mass with respect to 100 parts by mass in total of the resin (A) and the resin (B).
- the polylactic acid film of the present invention may contain a crystal nucleating agent in order to improve the heat resistance and tear resistance of the film.
- organic crystal nucleating agent aliphatic amide compounds, melamine compounds, phenylphosphonic acid metal salts, benzenecarboxamide derivatives, aliphatic / aromatic carboxylic acid hydrazides, sorbitol compounds, amino acids, polypeptides, etc. are preferably used. be able to.
- carbon black, talc or the like can be preferably used as the inorganic crystal nucleating agent.
- the content of the crystal nucleating agent in the composition constituting the film is preferably 0.1 to 10 parts by mass, and 0.5 to 5 parts by mass with respect to 100 parts by mass in total of the resin (A) and the resin (B). Is more preferable.
- the polylactic acid film of the present invention preferably has a tensile elongation of 50% or more and 500% or less. When the tensile elongation is 50% or more, film breakage and defects (holes) are unlikely to occur during film formation, and the film forming property is improved. Therefore, the tensile elongation is preferably 50% or more.
- the tensile elongation is 150% or more, workability such as stretching and embossing is further improved. Therefore, the tensile elongation is more preferably 150% or more.
- the tensile elongation is more preferably 200% or more.
- the tensile elongation is 500% or less, it is difficult for tarmi and wrinkles to occur during roll-to-roll travel and winding, and the roll winding shape and unwinding property are improved. Therefore, the tensile elongation is 500% or less. preferable.
- the contents of the resin (A), the resin (B) and the filler (C) in the composition constituting the film are within the preferred ranges described above.
- the method and the method of making the relationship of the kind and mass ratio of the surface treating agent of a filler (C) and the specific surface area of a filler into the preferable content mentioned above are mentioned.
- the polylactic acid-based film of the present invention preferably has a tensile modulus in the length direction and the width direction of 100 to 1,500 MPa in order to impart sufficient flexibility.
- the tensile modulus is more preferably 150 to 1,200 MPa, and further preferably 200 to 1,000 MPa.
- the polylactic acid film of the present invention preferably has a film thickness of 5 to 300 ⁇ m. By setting the film thickness to 5 ⁇ m or more, processability such as stretching and embossing of the film is improved, and the firmness of the film is enhanced, the handling property is excellent, and the roll winding shape and unwinding property are further improved. Becomes better.
- the film thickness is more preferably 7 to 200 ⁇ m, further preferably 10 to 100 ⁇ m, and still more preferably 12 to 50 ⁇ m.
- the film thickness is more preferably 7 to 200 ⁇ m, further preferably 10 to 100 ⁇ m, and still more preferably 12 to 50 ⁇ m.
- the thermal shrinkage in the length direction and the width direction is preferably ⁇ 5 to 5%. By making it 5% or less, it is possible to suppress deterioration of the winding shape due to shrinkage with time of the film after winding, so-called winding tightening.
- the composition constituting the polylactic acid film of the present invention preferably contains 0.1 to 5% by mass of an organic lubricant in 100% by mass of the whole composition. In this case, blocking of the film after winding can be favorably suppressed.
- the polylactic acid film of the present invention when the polylactic acid film of the present invention is produced, when the composition is once pelletized, dried, melt-kneaded again, and extruded / formed, blocking between the pellets can be prevented. This is preferable in terms of handleability.
- organic lubricants include liquid paraffins, natural paraffins, synthetic paraffins, aliphatic hydrocarbons such as polyethylene, stearic acid, lauric acid, hydroxystearic acid, fatty castors such as hard castor oil, stearic acid amide, oleic acid amide, Fatty acid amides such as erucic acid amide, lauric acid amide, ethylene bis stearic acid amide, ethylene bis oleic acid amide, ethylene bis lauric acid amide, fatty acid metal salts such as aluminum stearate, lead stearate, calcium stearate, magnesium stearate , Fatty acid (partial) esters of polyhydric alcohols such as glycerin fatty acid esters and rubitan fatty acid esters, long chain fatty acid esters such as long chain ester waxes such as butyl stearate and montan wax And the like.
- liquid paraffins such as polyethylene, stearic acid, la
- fatty acid amide organic lubricants that are easy to obtain an effect in a small amount due to moderate compatibility with polylactic acid are preferred.
- organic lubricants having a relatively high melting point such as ethylene bis stearic acid amide, ethylene bis oleic acid amide, and ethylene bis lauric acid amide are preferable from the viewpoint of expressing better blocking resistance.
- additives In the composition which comprises the polylactic acid-type film of this invention, you may contain additives other than having mentioned above in the range which does not impair the effect of this invention.
- plasticizers for example, known plasticizers, antioxidants, dispersants, UV stabilizers, anti-coloring agents, matting agents, antibacterial agents, deodorants, flame retardants, weathering agents, antistatic agents, antioxidants, ion exchange Agents, tackifiers, antifoaming agents, color pigments, dyes and the like.
- Plasticizers include acetyl citrate ester, phthalate ester, aliphatic dibasic acid ester, phosphate ester, hydroxy polycarboxylic acid ester, fatty acid ester, polyhydric alcohol ester, epoxy, Polyester, polyalkylene ether, ether ester and acrylate plasticizers can be used.
- antioxidant examples include hindered phenols and hindered amines.
- the polylactic acid-based film of the present invention is a resin (A) (polylactic acid-based resin) or a case where biodegradability is not particularly required, such as packaging for various industrial products, or in applications where storage durability is preferred.
- the carboxyl group terminal concentration of the film is preferably 30 equivalents / 10 3 kg or less, More preferably, it is 20 equivalent / 10 ⁇ 3 > kg or less, More preferably, it is 10 equivalent / 10 ⁇ 3 > kg or less.
- the carboxyl group terminal concentration of the film is 30 equivalents / 10 3 kg or less, the carboxyl group terminal concentration that also serves as a hydrolysis autocatalyst is sufficiently low. There are many cases where this is possible.
- Examples of a method for setting the carboxyl group terminal concentration of the film to 30 equivalents / 10 3 kg or less include, for example, a catalyst or heat during synthesis of a resin (A) (polylactic acid resin) or a polyester resin as the resin (B). Control method by history, oligomer removal, etc., reduction of moisture content of resin used during film formation, reduction of extrusion temperature or retention time during film formation, reduction of thermal history, oligomer removal method, reaction type The method etc. which block the carboxyl group terminal using a compound are mentioned. Among these, a method using a reactive compound is preferable. That is, the polylactic acid film of the present invention is preferably a film obtained by using a composition obtained by reacting a reactive compound with the resin (A) and / or the resin (B).
- the method of blocking the carboxyl group terminal using a reactive compound it is preferable that at least a part of the carboxyl group terminal in the film is blocked, and it is more preferable that the whole amount is blocked.
- reactive compounds include condensation reactive compounds such as aliphatic alcohols and amide compounds, and addition reactive compounds such as carbodiimide compounds, epoxy compounds, and oxazoline compounds, but extra by-products are generated during the reaction.
- An addition reaction type compound is preferable in terms of difficulty, and among them, a carbodiimide compound and an epoxy compound are preferable from the viewpoint of reaction efficiency.
- a carbodiimide compound is a compound having at least one carbodiimide group represented by (—N ⁇ C ⁇ N—) in the molecule, and commercially available products include Nisshinbo's “Carbodilite” series, Rhein Chemie. The company's “Stabaxol” series and the like.
- Examples of the epoxy compound include glycidyl ether compounds, glycidyl ester compounds, glycidyl amine compounds, glycidyl imide compounds, glycidyl (meth) acrylate compounds, alicyclic epoxy compounds, and the like.
- Commercially available products include BASF's “Joncry” series of glycidyl group-containing acrylic / styrene copolymers, “Reseda” series, “Alfon” series of glycidyl group-containing acrylic resins. Examples include the “Tepic” series of Nissan Chemical Co., Ltd., which are epoxy compounds with a triazine skeleton.
- the compounding amount of the reactive compound in the polylactic acid film of the present invention is preferably 0.01 to 10 parts by mass, and 0.05 to 5 parts by mass with respect to 100 parts by mass in total of the resin (A) and the resin (B). Part is more preferable, 0.1 to 3 parts by weight is further preferable, and 0.5 to 2 parts by weight is particularly preferable.
- the specific surface area S (m 2 / g) of the inorganic filler and / or the organic filler and the mass ratio T (%) of the portion derived from the surface treatment agent in the filler (C) are preferable.
- the processability of the film And found that durability is compatible at a high level.
- the amount of lactic acid oligomer component contained in the film is preferably 0.3% by mass or less.
- lactic acid oligomer component refers to lactic acid, a linear oligomer of lactic acid, a cyclic oligomer of lactic acid, and the like.
- Lactide and DD-lactide, DL (meso) -lactide A method for setting the amount of the lactic acid oligomer component to 0.3% by mass or less will be described later. (Production method) Next, the method for producing the polylactic acid film of the present invention will be specifically described, but the present invention is not limited thereto.
- the polylactic acid resin which is the resin (A) in the present invention can be obtained, for example, by the following method.
- a lactic acid component of L-lactic acid or D-lactic acid is mainly used, and a hydroxycarboxylic acid other than the lactic acid component described above can be used in combination.
- a cyclic ester intermediate of hydroxycarboxylic acid for example, lactide, glycolide, etc. can be used as a raw material.
- dicarboxylic acids and glycols can also be used.
- the polylactic acid resin can be obtained by a method of directly dehydrating and condensing the raw materials or a method of ring-opening polymerization of the cyclic ester intermediate.
- lactic acid or lactic acid and hydroxycarboxylic acid are preferably subjected to azeotropic dehydration condensation in the presence of an organic solvent, particularly a phenyl ether solvent, and particularly preferably a solvent distilled by azeotropic distillation.
- a polymer having a high molecular weight can be obtained by polymerizing by a method in which water is removed from the solvent and the solvent is brought into a substantially anhydrous state and returned to the reaction system.
- a high molecular weight polymer can be obtained by subjecting a cyclic ester intermediate such as lactide to ring-opening polymerization under reduced pressure using a catalyst such as tin octylate.
- a method for adjusting the conditions for removing moisture and low molecular weight compounds during heating and refluxing in an organic solvent, a method for suppressing the depolymerization reaction by deactivating the catalyst after completion of the polymerization reaction, and a method for heat treating the produced polymer Can be used to obtain a polymer with a small amount of lactide.
- composition constituting the polylactic acid film of the present invention that is, resin (A) (polylactic acid resin), resin (B) (thermoplastic resin other than polylactic acid resin), filler (C), or organic
- resin (A) polylactic acid resin
- resin (B) thermoplastic resin other than polylactic acid resin
- filler (C) filler
- organic In obtaining a composition containing other components such as a lubricant, it is possible to produce a composition by uniformly mixing a solution in which each component is dissolved in a solvent and then removing the solvent. It is preferable to employ a melt-kneading method in which a composition is produced by melt-kneading each component, which is a practical production method that does not require steps such as dissolution and solvent removal.
- the melt kneading method is not particularly limited, and a commonly used known mixer such as a kneader, roll mill, Banbury mixer, single-screw or twin-screw extruder can be used. Among these, from the viewpoint of dispersibility of the resin (A), the resin (B), and the filler (C), it is preferable to use a twin screw extruder.
- the temperature at the time of melt kneading is preferably in the range of 150 ° C. to 240 ° C., and more preferably in the range of 190 ° C. to 210 ° C. from the viewpoint of preventing deterioration of the polylactic acid resin.
- the polylactic acid-based film of the present invention can be obtained by a known film production method such as a known inflation method, a tubular method, or a T-die cast method using, for example, the composition obtained by the above-described method.
- the pellet is heated at 60 to 100 ° C. It is preferable that the moisture content is 500 ppm or less, preferably 200 ppm or less by drying for 6 hours or more. Furthermore, it is preferable to reduce the amount of lactic acid oligomer components in the composition containing a polylactic acid-based resin or the like by vacuum drying under a high vacuum with a degree of vacuum of 10 Torr or less.
- melt viscosity can be adjusted to an appropriate level and the film forming process can be stabilized.
- a twin-screw extruder with a vacuum vent hole is used and melt extrusion is performed while removing volatiles such as moisture and low molecular weight substances. It is preferable to do.
- the following method is used. Pellets of the composition prepared by the method as described above are melt-extruded in a twin-screw extruder with a vent hole and led to an annular die, extruded from the annular die and supplied with dry air into a balloon shape (bubble). And then air-cooled and solidified uniformly with an air ring, taken up at a specified take-up speed while folded flat with a nip roll, and then cut off both ends or one end as necessary to wind it up. Can be obtained. *
- the cylinder temperature at the time of melt extrusion of the composition constituting the polylactic acid film of the present invention is usually in the range of 150 to 240 ° C., and the temperature of the annular die is preferably 150 to 190 ° C., more preferably 150 to 180 ° C. It is in the range of ° C.
- the spiral die is preferably a spiral type in terms of thickness accuracy and uniformity.
- various surface treatments may be applied for the purpose of improving printability, laminate suitability, coating suitability, and the like.
- the surface treatment include corona discharge treatment, plasma treatment, flame treatment, acid treatment, etc., and any method can be used, but continuous treatment is possible and equipment for existing film forming equipment is used. Corona discharge treatment can be exemplified as the most preferable one because of easy installation and simple processing.
- the polylactic acid film of the present invention is excellent in bleed resistance and blocking resistance, it can be smoothly unwound without problems when the film is unwound from the film roll after being wound.
- the blow ratio is a ratio R L / R O of the final radius R L of the bubble and the radius R O of the annular die
- the draw ratio is the winding speed V L of the molded film and melted from the die lip.
- a preferable range of the blow ratio is 1.5 to 4.0, more preferably 1.7 to 3.5, and still more preferably 2.0 to 3.0.
- a preferable range of the draw ratio is 2 to 80, more preferably 4 to 70, still more preferably 5 to 60, and particularly preferably 6 to 50.
- Processing methods such as stretching and embossing for making the polylactic acid-based film of the present invention a film that exhibits good moisture permeability will be specifically described, but the present invention is not limited thereto.
- the polylactic acid film of the present invention is heated by being conveyed on a roll at 50 to 90 ° C., and stretched in the longitudinal direction of the film using a difference in peripheral speed between the rolls.
- the film uniaxially stretched in this way is once cooled, and then both ends of the film are held by clips and guided to a tenter at 55 to 95 ° C., and stretched in the width direction.
- the stretched film is heat-treated at 90 to 150 ° C. for 0.2 to 30 seconds while being relaxed under tension or in the width direction.
- the relaxation rate is 1 to 10% from the viewpoint of reducing the thermal contraction rate in the width direction.
- Stretching may be longitudinal or lateral uniaxial stretching, or longitudinal and lateral biaxial stretching.
- the polylactic acid film of the present invention is heated between 20 to 80 ° C. and passed between an embossing roll having irregularities on the surface and a rubber nip roll.
- the second aspect of the present invention includes a polylactic acid resin as the resin (A), and 10 to 400 parts by mass of the filler (C) and / or the filler (D) with respect to 100 parts by mass in total of the resin.
- the filler (C) is a compound treated with a surface treatment agent
- the filler (D) is an inorganic filler and / or an organic filler not treated with a surface treatment agent
- tensile A polylactic acid film characterized by having an elongation of 150 to 500%.
- the polylactic acid film of the second aspect of the present invention is the same as the polylactic acid film of the first aspect except for the points described below. That is, the description of the second aspect including the resin (A) (polylactic acid resin), the filler (C), and the tensile elongation is as described in the first aspect.
- the filler (D) in the polylactic acid film of the second aspect of the present invention is the precursor of the filler (C) described in the section (Filler (C)), that is, the filler (C).
- An inorganic filler and / or an organic filler which is a compound before being treated with a surface treatment agent.
- the content of the filler (C) and / or filler (D) in the composition constituting the film is 10 to 400 parts by mass with respect to 100 parts by mass in total of the whole resin. .
- the content of the filler (C) and / or the filler (D) in the composition constituting the film is preferably 20 to 300 parts by mass with respect to 100 parts by mass in total of the whole resin, and preferably 30 to 200 parts.
- the average tensile elongation in the length direction and the width direction is more preferably from 200% to 500%, and further preferably from 250% to 500%.
- the content of the filler (C) and / or filler (D) with respect to the entire resin constituting the film And a method of setting the blow ratio and the draw ratio to the above-described preferable ranges when manufacturing by the inflation method.
- Resin (A) In the polylactic acid film of the second aspect of the present invention, it is not necessary to be a mixture of a crystalline polylactic acid resin and an amorphous polylactic acid resin, as long as the above-described tensile elongation conditions are satisfied. That is, the crystalline polylactic acid resin alone or the amorphous polylactic acid resin alone can be used.
- a sample is cut out in a strip shape having a length of 150 mm and a width of 10 mm in the measurement direction, and according to the method defined in JIS K-7127 (1999) at an initial tensile chuck distance of 50 mm and a tensile speed of 200 mm / min.
- the measurement was performed 10 times for each of the length direction and the width direction, and the average value was taken as the tensile elastic modulus in the length direction and the width direction.
- (2) Heat resistance A film for evaluation is affixed to an aluminum frame having a size of 150 mm square in a tensioned state without wrinkles, and the film is fixed to the frame using a plurality of double clips for stationery.
- the film was left in a hot air oven maintained at a constant temperature for 5 minutes and then taken out to observe the state of the film.
- the test was repeated by increasing the set temperature of the hot air oven from 120 ° C in increments of 5 ° C, and the highest temperature at which no change was observed such as holes in the film or fusion of the film to the frame was observed. (° C).
- the evaluation was made according to the following criteria. ⁇ (excellent): 160 ° C. or more ⁇ (good): 140 ° C. or more and less than 160 ° C. ⁇ (possible): 120 ° C. or more and less than 140 ° C. x (impossible): less than 120 ° C. (3) Bleed-out resistance As described below, the mass reduction rate (%) after the hot water treatment was determined and used as an index of bleed-out resistance. The smaller the mass reduction rate, the better the bleed out resistance.
- the mass (g) before processing was measured on about 0.5 g of a film sample that had been conditioned for 1 day or more in an atmosphere of a temperature of 23 ° C. and a humidity of 65% RH.
- the moisture (g) (to the third decimal place) was measured after humidity was adjusted again under the same conditions as before the treatment.
- decrease rate was computed by calculating
- a sample is cut out in a strip shape having a length of 150 mm and a width of 10 mm in the measurement direction, and according to the method specified in JIS K-7127 (1999) at an initial tensile chuck distance of 50 mm and a tensile speed of 200 mm / min.
- the measurement was performed 10 times for each of the length direction and the width direction, and the average value was taken as the tensile elongation in the length direction and the width direction, respectively.
- the stretching conditions at that time were preheating at a temperature of 80 ° C. and a time of 10 seconds in a stretching chamber, followed by 3.5 times stretching in the longitudinal direction at a temperature of 80 ° C. and a speed of 30% / second. Thereafter, the film was stretched 3.5 times in the width direction, and then heat treated in a heat treatment chamber at a temperature of 100 ° C. for 10 seconds to obtain a biaxially stretched film. From the state of the sequentially biaxially stretched film, the following criteria were evaluated.
- the upper embossing roll is a pinpoint pattern with a pitch of 1.8 mm, a repeat of 1.8 mm, a depth of 0.78 mm, a roll diameter of 100 mm, and the lower rubber roll uses a super hard rubber roll with a hardness of D-90.
- An embossed film was obtained at a roll temperature of 50 ° C., a nip pressure of 100 kg / cm, and a roll rotation speed of 1 m / min. From the state of the film after embossing, the following criteria were used for evaluation.
- Moisture permeability after processing In a constant temperature and humidity device set at 25 ° C. and 90% RH, processing was performed by the method described in (5) or (6) according to the method defined in JIS Z0208 (1976). The water vapor transmission rate (g / (m 2 ⁇ day)) of the subsequent film was measured.
- the film after being processed by the method described in (5) or (6) is affixed to an aluminum frame having a frame size of 150 mm square in a tensioned state so as not to be wrinkled. Fix the film to the frame using a plurality of double clips, and take it out for 30 days in a constant temperature and humidity oven maintained at 40 ° C. and 75% RH. Then, take it out and measure the tensile elongation as in (4). The tensile elongation Ea after forced deterioration was defined.
- the tensile elongation was measured in the same manner as in (4) to obtain the tensile elongation Eb before forced deterioration.
- the above melting point was determined by heating a polylactic acid resin in a hot air oven at 100 ° C. for 24 hours, using a differential scanning calorimeter RDC220 manufactured by Seiko Instruments Inc., and setting 5 mg of a sample in an aluminum tray. It was determined as the peak temperature of the crystal melting peak when the temperature was raised from 250C to 250C at a heating rate of 20C / min.
- the pellets of this composition were vacuum-dried at a temperature of 60 ° C. for 12 hours using a rotary drum type vacuum dryer.
- the dried composition pellets were supplied to a single screw extruder having a cylinder temperature of 180 ° C., and bubble-shaped at a blow ratio of 2.4 from a spiral annular die having a diameter of 250 mm, a lip clearance of 1.3 mm, and a temperature of 160 ° C. , Rolled up with a nip roll above the die, taken up while being folded, cut at both ends with an edge cutter and cut into two pieces, each wound with a winder to obtain a film with a final thickness of 100 ⁇ m It was. At this time, the draw ratio was 6. Table 1 shows the physical properties of the obtained film.
- Examples 2 to 8, 17 to 29, Comparative Examples 1 to 3 A film was obtained in the same manner as in Example 1 except that the composition of the film was changed as shown in the table. Table 1 shows the physical properties of the obtained film.
- Example 9 15 parts by mass of polylactic acid resin (A1), 45 parts by mass of polylactic acid resin (A3), 20 parts by mass of polybutylene adipate / terephthalate resin (B1), 20 parts by mass of block copolymer plasticizer (B4), filler (C1 ) 70 parts by mass of the mixture was subjected to a twin screw extruder with a vacuum vent of 44 mm and a cylinder diameter of 190 ° C., melted and kneaded while degassing the vacuum vent, homogenized and pelletized to obtain a composition. .
- the pellets of this composition were vacuum-dried at a temperature of 60 ° C. for 12 hours using a rotary drum type vacuum dryer.
- the dried composition pellets were supplied to a single screw extruder having a cylinder temperature of 180 ° C., and bubble-shaped at a blow ratio of 2.4 from a spiral annular die having a diameter of 250 mm, a lip clearance of 1.3 mm, and a temperature of 160 ° C. , Rolled up with a nip roll above the die, taken up while being folded, cut at both ends with an edge cutter and cut into two pieces, each wound with a winder to obtain a film with a final thickness of 15 ⁇ m It was. At this time, the draw ratio was 36.
- Table 2 The physical properties of the obtained film are shown in Table 2.
- Example 10 to 16, 30 to 42, Comparative Examples 4 to 6 A film was obtained in the same manner as in Example 9 except that the composition of the film was changed as shown in Table 2. The physical properties of the obtained film are shown in Table 2.
- “mass%” of resin (A) and resin (B) is a value (mass%) at a total of 100 mass% of resin (A) and resin (B). Further, the “part by mass” of the filler (C) is a value (part by mass) when the total of the resin (A) and the resin (B) is 100 parts by mass.
- the porous film of the present invention is excellent in flexibility, heat resistance, bleed-out resistance, durability, and excellent in workability such as stretching and embossing to express good moisture permeability. It is a film, medical / hygienic materials such as bed sheets, pillow covers, sanitary napkins, back sheets for absorbent articles such as paper diapers, clothing materials such as rainy clothes, gloves, garbage bags and compost bags, vegetables and fruits, etc. It can be used for films for processing such as stretching and embossing to obtain packaging materials such as food bags and bags for various industrial products.
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Abstract
Description
1)樹脂(A)としてポリ乳酸系樹脂、樹脂(B)としてポリ乳酸系樹脂以外の熱可塑性樹脂、充填剤(C)として表面処理剤により処理された化合物を含む組成物からなるフィルムであり、
前記ポリ乳酸系樹脂が、結晶性ポリ乳酸系樹脂及び非晶性ポリ乳酸系樹脂を含み、
樹脂(A)と樹脂(B)の合計100質量%において、樹脂(A)を10~95質量%、樹脂(B)を5~90質量%含有し、樹脂(A)と樹脂(B)の合計100質量部に対して、充填剤(C)を10~400質量部含有する組成物からなることを特徴とする、ポリ乳酸系フィルム。
2)前記表面処理剤が、リン酸エステル系化合物及び/又は脂肪酸であることを特徴とする、1)に記載のポリ乳酸系フィルム。
3)前記表面処理剤が、メタクリル酸エステル基を含むことを特徴とする、1)または2)に記載のポリ乳酸系フィルム。
4)前記充填剤(C)が、無機充填剤および/または有機充填剤に対して、表面処理剤で処理することで得られたものであり、該無機充填剤および/または有機充填剤の比表面積S(m2/g)と、前記充填剤(C)中の表面処理剤に由来する部分の質量割合T(質量%)が以下の条件を満たすことを特徴とする、1)~3)のいずれかに記載のポリ乳酸系フィルム。
5)前記樹脂(B)が、ポリエーテル系セグメントとポリ乳酸セグメントとを有するブロック共重合体、ポリエステル系セグメントとポリ乳酸セグメントとを有するブロック共重合体、脂肪族ポリエステル系樹脂、及び脂肪族芳香族ポリエステル系樹脂からなる群より選ばれる少なくとも1つの樹脂であることを特徴とする、1)から4)のいずれかに記載のポリ乳酸系フィルム。
6)前記樹脂(B)が、ポリエーテル系セグメントとポリ乳酸セグメントとを有するブロック共重合体及びポリエステル系セグメントとポリ乳酸セグメントとを有するブロック共重合体からなる群より選ばれる少なくとも1つの樹脂、並びに、脂肪族ポリエステル系樹脂及び脂肪族芳香族ポリエステル系樹脂からなる群より選ばれる少なくとも1つの樹脂からなること特徴とする、5)に記載のポリ乳酸系フィルム。
7)樹脂(A)及び/又は樹脂(B)に対して反応型化合物を反応させた組成物を用いて得られることを特徴とする、1)~6)のいずれかに記載のポリ乳酸系フィルム。
8)引張伸度が150~500%であることを特徴とする、1)~7)のいずれかに記載のポリ乳酸系フィルム。
9)引張弾性率が100~1,500MPaであることを特徴とする1)~8)のいずれかに記載のポリ乳酸系フィルム。
10)樹脂(A)としてポリ乳酸系樹脂、並びに、樹脂全体の合計100質量部に対し、充填剤(C)及び/又は充填剤(D)を10~400質量部含む組成物からなるフィルムであり、
前記充填剤(C)が、表面処理剤により処理された化合物であり、
前記充填剤(D)が、表面処理剤により処理されていない無機充填剤及び/又は有機充填剤であり、
引張伸度が150~500%であることを特徴とする、ポリ乳酸系フィルム。
(第1の態様のポリ乳酸系フィルム)
(樹脂(A)(ポリ乳酸系樹脂))
本発明のポリ乳酸系フィルムは、樹脂(A)を含む組成物からなることが重要である。ここで樹脂(A)とは、ポリ乳酸系樹脂を意味する。またポリ乳酸系樹脂とは、L-乳酸ユニットおよび/またはD-乳酸ユニットを主たる構成成分とする重合体である。ここで主たる構成成分とは、重合体100質量%中において乳酸ユニットの質量割合が最大であることを意味する。乳酸ユニットの質量割合は、好ましくは重合体100質量%中において、乳酸ユニットが70質量%~100質量%である。
(樹脂(B)(ポリ乳酸系樹脂以外の熱可塑性樹脂))
本発明のポリ乳酸系フィルムは、柔軟性と、加工後の透湿性を向上させるために、樹脂(B)を含む組成物からなることが重要である。ここで樹脂(B)とは、ポリ乳酸系樹脂以外の熱可塑性樹脂である。ポリ乳酸系樹脂以外の熱可塑性樹脂としては、ポリアセタール、ポリエチレン、ポリプロピレン、ポリアミド、ポリ(メタ)アクリレート、ポリフェニレンサルファイド、ポリエーテルエーテルケトン、ポリエステル、ポリウレタン、ポリイソプレン、ポリスルホン、ポリフェニレンオキサイド、ポリイミド、ポリエーテルイミド、エチレン/グリシジルメタクリレート共重合体、ポリエステルエラストマー、ポリアミドエラストマー、エチレン/プロピレンターポリマー、エチレン/ブテン-1共重合体、熱可塑性デンプン、デンプンを含むポリマー、各種樹脂系の可塑剤などが使用できる。
(樹脂(B)の組み合わせ)
本発明のポリ乳酸系フィルムには、これらの樹脂(B)を1種のみ含んでもよいし、2種以上を組み合わせて含んでもよい。組み合わせる樹脂には特に制限はなく、樹脂(B)として前述したポリ乳酸系樹脂以外の熱可塑性樹脂群をそれぞれ組み合わせることができる。その中でも、柔軟性と、加工後の透湿性を両立させる点から、各種樹脂系の可塑剤と、樹脂系の可塑剤以外の熱可塑性樹脂との組み合わせが好ましい。特に本発明では、樹脂(B)として、各種樹脂系の可塑剤と、樹脂系の可塑剤以外の熱可塑性樹脂とを組み合わせた際に、加工後の透湿性が飛躍的に向上することを見出した。
(結晶性ポリ乳酸系樹脂と非晶性ポリ乳酸系樹脂の混合)
本発明のポリ乳酸系フィルムを構成する組成物に含有される樹脂(A)(ポリ乳酸系樹脂)は、結晶性ポリ乳酸系樹脂と非晶性ポリ乳酸系樹脂の混合物であることが重要である。つまり、樹脂(A)(ポリ乳酸系樹脂)が、結晶性ポリ乳酸系樹脂及び非晶性ポリ乳酸系樹脂を含むことが重要である。樹脂(A)(ポリ乳酸系樹脂)を、結晶性ポリ乳酸系樹脂と非晶性ポリ乳酸系樹脂との混合物とすることにより、結晶性、非晶性、それぞれのポリ乳酸系樹脂の利点を両立できるからである。
(充填剤(C))
本発明のポリ乳酸系フィルムは、加工後の透湿性を向上させるために、充填剤(C)として表面処理剤により処理された化合物を含む組成物からなることが重要である。充填剤(C)の前駆体である、表面処理剤により処理を施す前の化合物としては、無機充填剤および/または有機充填剤が使用できる。
本発明の充填剤(C)が、無機充填剤および/または有機充填剤に対して、表面処理剤で処理することで得られたものであり、該無機充填剤および/または有機充填剤の比表面積S(m2/g)と、前記充填剤(C)中の表面処理剤に由来する部分の質量割合T(質量%)は以下の条件を満たすことが好ましい。
T/Sが0.15以上であることは、前記した表面処理剤の効果を最大限に発揮させることが可能となる。T/Sは0.20以上であることがより好ましく、0.25以上であることが更に好ましい。また、T/Sが0.45以下であることは、過剰な表面処理剤によるマトリックス樹脂(樹脂(A)と樹脂(B))の加水分解、酸化分解等の劣化を抑制することが可能となり、すなわち耐久性が向上するので好ましい。T/Sは、0.40以下がより好ましい。
本発明の充填剤(C)の平均粒径は、特に限定されないが、0.01~10μmが好ましい。平均粒径が0.01μm以上とすることで、充填剤(C)をフィルム中に高充填することが可能となり、その結果、フィルムの透湿性向上のポテンシャルが高いフィルムとなり、平均粒径を10μm以下とすることで、フィルムの延伸、エンボスなどの加工性が良好となり、その結果、フィルムの透湿性向上のポテンシャルが高いフィルムとなる。充填剤(C)の平均粒径は、より好ましくは0.1~8μm、さらに好ましくは0.5~5μm、最も好ましくは1~3μmである。なお、ここでいう平均粒径とは、レーザー回折法により測定されたD50(粒子径分布のメジアン径)をいう。
(結晶核剤)
本発明のポリ乳酸系フィルムは、フィルムの耐熱性、耐引き裂き性を向上させるために、結晶核剤を含んでもよい。
(引張伸度)
本発明のポリ乳酸系フィルムは、引張伸度が、50%以上500%以下であることが好ましい。引張伸度が50%以上であると製膜時にフィルム破れや欠点(穴開き)が生じにくく、製膜性が良好となるので、引張伸度は50%以上であることが好ましい。引張伸度が150%以上であると、さらに延伸、エンボスなどの加工性が良好となるので、引張伸度は150%以上であることがより好ましい。引張伸度は、200%以上がさらに好ましい。引張伸度が500%以下であると製膜時にロール間走行時や巻き取り時のタルミやシワが生じにくく、ロール巻姿や巻出し性が良好となるので、引張伸度は500%以下が好ましい。
(引張弾性率)
本発明のポリ乳酸系フィルムは、十分な柔軟性を付与するために、長さ方向および幅方向の引張弾性率が、いずれも100~1,500MPaであることが好ましい。引張弾性率は、150~1,200MPaであることがより好ましく、200~1,000MPaであることがさらに好ましい。
(厚み)
本発明のポリ乳酸系フィルムは、フィルム厚みが5~300μmであることが好ましい。フィルム厚みを5μm以上とすることで、フィルムの延伸、エンボスなどの加工性が良好となり、また、フィルムとした際のコシが強くなり、取り扱い性に優れ、さらには、ロール巻姿や巻出し性が良好となる。フィルム厚みを300μm以下とすることで柔軟性、加工後の透湿性に優れるものとなり、また、特にインフレーション製膜法においては、自重によりバブルが不安定化しない。フィルム厚みは、7~200μmがより好ましく、10~100μmがさらに好ましく、12~50μmがさらにより好ましい。
(熱収縮率)
本発明のポリ乳酸系フィルムは、65℃、30分間で処理した時の、長さ方向と幅方向の熱収縮率は、-5~5%であることが好ましい。5%以下とすることで、巻き取った後のフィルムの経時収縮、いわゆる巻締りによる巻姿の悪化を抑制できる。さらには巻き硬度が高くなりすぎることによるブロッキングの発生を抑制できる。また、-5%以上とすることで、巻き取った後のフィルムが経時で長さ方向に弛むことによる、巻姿の悪化を抑制できる。なおここで、熱収縮率が0未満の値(マイナスの値)をとる場合は、フィルムが伸長することを意味する。
(有機滑剤)
本発明のポリ乳酸系フィルムを構成する組成物は、組成物全体100質量%において有機滑剤を0.1~5質量%含むことが好ましい。この場合、巻き取り後のフィルムのブロッキングを良好に抑制できる。さらに、後述するように、本発明のポリ乳酸系フィルムを製造する際に、組成物を一旦ペレット化して乾燥、再度溶融混練して押出・製膜する場合、ペレット間でのブロッキングを防ぐことができ、取り扱い性の点で好ましい。
(添加剤)
本発明のポリ乳酸系フィルムを構成する組成物には、本発明の効果を損なわない範囲で前述した以外の添加剤を含有してもよい。例えば、公知の可塑剤、酸化防止剤、分散剤、紫外線安定化剤、着色防止剤、艶消し剤、抗菌剤、消臭剤、難燃剤、耐候剤、帯電防止剤、抗酸化剤、イオン交換剤、粘着性付与剤、消泡剤、着色顔料、染料などが含有できる。
(カルボキシル基末端)
本発明のポリ乳酸系フィルムは、特に各種工業製品の包装用途など生分解性を必要としない場合や保管耐久性があった方が好ましい用途においては、樹脂(A)(ポリ乳酸系樹脂)や樹脂(B)としてのポリエステル系樹脂の加水分解による強度低下を抑制し、良好な耐久性を付与する観点から、該フィルムのカルボキシル基末端濃度が30当量/103kg以下であることが好ましく、より好ましくは20当量/103kg以下、さらに好ましくは10当量/103kg以下である。該フィルムのカルボキシル基末端濃度が30当量/103kg以下であると、加水分解の自己触媒ともなるカルボキシ基末端濃度が十分低いために、用途にもよるが実用的に良好な耐久性を付与できる場合が多い。
(乳酸オリゴマー成分量)
本発明のポリ乳酸系フィルムは、フィルム中に含まれる乳酸オリゴマー成分量が0.3質量%以下であることが好ましい。より好ましくは0.2質量%以下、さらに好ましくは0.1質量%以下である。フィルム中に含まれる乳酸オリゴマー成分量を0.3質量%以下とすることで、フィルム中に残留している乳酸オリゴマー成分が粉末状あるいは液状として析出した際のハンドリング性の悪化を抑制したり、ポリ乳酸系樹脂の加水分解進行を抑制してフィルムの耐経時性劣化を防止したり、さらには、ポリ乳酸特有の臭気を抑制することができる。ここでいう乳酸オリゴマー成分とは、フィルム中に存在する乳酸や乳酸の線状オリゴマーや環状オリゴマーなどの中で量的に最も代表的である乳酸の環状二量体(ラクチド)をいい、LL-ラクチドおよびDD-ラクチド、DL(メソ)-ラクチドである。乳酸オリゴマー成分量を0.3質量%以下とする方法は後述する。
(製造方法)
次に、本発明のポリ乳酸系フィルムを製造する方法について具体的に説明するがこれに限定されるものではない。
(加工方法)
本発明のポリ乳酸系フィルムを、良好な透湿度を発現するフィルムとするための延伸、エンボスなどの加工法を具体的に説明するがこれに限定されるものではない。
(第2の態様のポリ乳酸系フィルム)
本発明の第2の態様は、樹脂(A)としてポリ乳酸系樹脂を含み、樹脂全体の合計100質量部に対し、充填剤(C)及び/又は充填剤(D)を10~400質量部含み、前記充填剤(C)が、表面処理剤により処理された化合物であり、前記充填剤(D)が、表面処理剤により処理されていない無機充填剤及び/又は有機充填剤であり、引張伸度が150~500%であることを特徴とする、ポリ乳酸系フィルム、である。
(充填剤(D))
本発明の第2の態様のポリ乳酸系フィルムにおける充填剤(D)とは、(充填剤(C))の項で説明した充填剤(C)の前駆体、つまり、充填剤(C)に表面処理剤により処理を施す前の化合物である、無機充填剤および/または有機充填剤である。
(引張伸度)
本発明の第2の態様のポリ乳酸系フィルムでは、長さ方向と幅方向(長さ方向と垂直な方向)の平均の引張伸度が、150%以上500%以下であることが重要である。平均の引張伸度が150%未満の場合、延伸、エンボスなどの加工性が悪化する。また、平均の引張伸度が500%を超える場合、製膜時に、ロール間走行時や巻き取り時のタルミやシワが生じ易く、ロール巻姿や巻出し性が悪化する。長さ方向と幅方向の平均の引張伸度は、200%以上500%以下がより好ましく、250%以上500%以下がさらに好ましい。
(樹脂(A))
本発明の第2の態様のポリ乳酸系フィルムにおいては、前記の引張伸度の条件さえ満たせば、結晶性ポリ乳酸系樹脂と非晶性ポリ乳酸系樹脂の混合物である必要は無く、それぞれ単独、つまり、結晶性ポリ乳酸系樹脂単独、非晶性ポリ乳酸系樹脂単独で使用することができる。
[測定及び評価方法]
実施例中に示す測定や評価は次に示すような条件で行った。
(1)引張弾性率(MPa)
オリエンテック社製TENSILON UCT-100を用いて、室温23℃、相対湿度65%の雰囲気にて、引張弾性率を測定した。
(2)耐熱性
枠内サイズが150mm角であるアルミ製フレーム枠に、評価用のフィルムをシワがないように緊張状態で貼り付け、文具用のダブルクリップを複数用いてフィルムをフレームに固定し、庫内を一定温度に保った熱風式オーブンに5分間放置した後に取り出してフィルムの状態を観察した。熱風式オーブンの設定温度を120℃から5℃刻みで上げて試験を繰り返し、フィルムに穴が空いたり、フィルムがフレームに融着したりするなどの変化が認められなかった最も高い温度を耐熱温度(℃)として求めた。
◎(優):160℃以上
○(良):140℃以上160℃未満
△(可):120℃以上140℃未満
×(不可):120℃未満。
(3)耐ブリードアウト性
次の通り、熱水処理後の質量減少率(%)を求めることで、耐ブリードアウト性の指標とした。質量減少率が小さいほど、耐ブリードアウト性が良好となる。
(4)加工性A(引張伸度)
オリエンテック社製TENSILON UCT-100を用いて、室温23℃、相対湿度65%の雰囲気にて、引張伸度を測定した。
◎(優):150%以上
○(良):100%以上150%未満
△(可):50%以上100%未満
×(不可):50%未満。
(5)加工性B
厚さ100μm、長さ100mm、幅100mmのフィルムサンプルを、ブルックナー社製フィルムストレッチャー“KARO-IV”を用いて延伸を行った。その際の延伸条件は、延伸室にて、温度80℃、時間10秒で予熱を行い、続いて、温度80℃、速度30%/秒で、長手方向に3.5倍の延伸を行った後、幅方向に3.5倍の延伸を行い、次に、熱処理室にて、温度100℃、時間10秒で熱処理を行うことで、逐次二軸延伸したフィルムを得た。
逐次二軸延伸フィルムの状態から、以下の基準で評価した。
○(良):良好に延伸可能(フィルムに破れや穴開きが無い)
△(可):延伸可能(フィルムに微小な穴開きがあるが、破れは無い)
×(不可):延伸不可能(フィルムが破れているなど、○及び△以外が該当)
(6)加工性C
厚さ15μm、長さ300mm、幅210mmのフィルムサンプルを、由利ロール社製電気加熱式エンボス機“HTEM-300型”を用いてエンボス加工を行った。
エンボス加工後のフィルムの状態から、以下の基準で評価した。
○(良):良好に加工可能(フィルムに破れや円形の穴がない)
△(可):加工可能(フィルムに円形の穴があるが、破れはない)
×(不可):加工不可能(○及び△以外が該当)
(7)加工後の透湿性
25℃、90%RHに設定した恒温恒湿装置にて、JIS Z0208(1976)に規定された方法に従って、(5)または(6)に記載の方法で加工した後のフィルムの透湿度(g/(m2・day))を測定した。
◎(優):1,500g/(m2・day)以上
○(良):1,000g/(m2・day)以上1,500g/(m2・day)未満
△(可):200g/(m2・day)以上1,000g/(m2・day)未満
×(不可):200g/(m2・day)未満。
(8)比表面積S(m2/g)
表面処理剤で処理する前の充填剤(充填剤(C)の前駆体)を用いて、JIS R5201(1997)に規定されたブレーン透過法により測定した。
(9)表面処理剤に由来する部分の質量割合T(質量%)
表面処理剤で処理する前の充填剤(充填剤(C)の前駆体)を、容器固定型混合機であるヘンシェルミキサー内に仕込み、回転翼の回転数1500rpmで攪拌しながら昇温し、缶内温度が90℃に達した時点で、充填剤(C)中の表面処理剤に由来する部分の質量割合がT(質量%)となるように噴霧させながら表面処理剤を添加した。その後10分間混合して反応させた。なお、回転翼の回転数、缶内温度、混合時間は、充填剤、表面処理剤の種類によって適宜変更できる。
(10)耐久性
(5)または(6)に記載の方法で加工した後のフィルムを、枠内サイズが150mm角であるアルミ製フレーム枠に、シワがないように緊張状態で貼り付け、文具用のダブルクリップを複数用いてフィルムをフレームに固定し、40℃、75%RHに保った恒温恒湿オーブンに30日間保存した後に取り出して、(4)と同様にして引張伸度を測定し、強制劣化後の引張伸度Eaとした。
◎(優):0.9以上
○(良):0.8以上0.9未満
△(可):0.5以上0.8未満
×(不可):0.5未満。
[樹脂(A)]
(A1)
ポリ乳酸系樹脂、質量平均分子量=200,000、D体含有量=1.4%、融点=166℃
(A2)
ポリ乳酸系樹脂、質量平均分子量=200,000、D体含有量=5.0%、融点=150℃、
(A3)
ポリ乳酸系樹脂、質量平均分子量=200,000、D体含有量=12.0%、融点=無し
なお、上記の質量平均分子量は 日本Warters(株)製、Warters2690を用い、ポリメチルメタクリレートを標準とし、カラム温度40℃、クロロホルム溶媒を用いて測定した。
[樹脂(B)]
(B1)
ポリブチレンアジペート・テレフタレート樹脂(BASF社製、商品名“エコフレックス”FBX7011)
(B2)
ポリブチレンサクシネート樹脂(三菱化学社製、商品名“GSPla”AZ91T)
(B3)
ポリブチレンサクシネート・アジペート樹脂(昭和高分子社製、商品名“ビオノーレ”#3001)
(B4)
数平均分子量8,000のポリエチレングリコール62質量部とL-ラクチド38質量部とオクチル酸スズ0.05質量部を混合し、撹拌装置付きの反応容器中で、窒素雰囲気下160℃で3時間重合することで、数平均分子量8,000のポリエチレングリコールの両末端に数平均分子量2,500のポリ乳酸セグメントを有するブロック共重合体可塑剤B4を得た。
[可塑剤(P)]
(P1)
アセチルクエン酸トリブチル、ファイザー社製、商品名“シトロフレックスA-4”)
[充填剤]
(C1)
炭酸カルシウム(味の素ファインテクノ株式会社製、商品名“トップフローH200”、平均粒子径:1.7μm、表面処理剤:リン酸エステル系化合物(末端にメタクリル酸エステル基を含む)、比表面積S=2.0m2/g、表面処理剤に由来する部分の質量割合T=1.8質量%、T/S=0.90)
(C2)
炭酸カルシウム(三共精粉株式会社製、商品名“E#2010”、平均粒子径:1.8μm、表面処理剤:ステアリン酸、比表面積S=2.0m2/g、表面処理剤に由来する部分の質量割合T=1.0質量%、T/S=0.50)
(D1)
炭酸カルシウム(三共精粉株式会社製、商品名“#2000”、平均粒子径:1.8μm、表面処理剤:無し)
(C3)
炭酸カルシウム(味の素ファインテクノ株式会社製、商品名“トップフローH100”、平均粒子径:3.6μm、表面処理剤:リン酸エステル系化合物(末端にメタクリル酸エステル基を含む)、比表面積S=1.0m2/g、表面処理剤に由来する部分の質量割合T=0.7質量%、T/S=0.70)
(C4)
炭酸カルシウム(平均粒子径:1.7μm、表面処理剤:リン酸エステル系化合物(末端にメタクリル酸エステル基を含む)、比表面積S=2.0m2/g、表面処理剤に由来する部分の質量割合T=0.7質量%、T/S=0.35)
(C5)
炭酸カルシウム(平均粒子径:3.6μm、表面処理剤:リン酸エステル系化合物(末端にメタクリル酸エステル基を含む)、比表面積S=1.0m2/g、表面処理剤に由来する部分の質量割合T=0.4質量%、T/S=0.40)
(C6)
炭酸カルシウム(平均粒子径:1.7μm、表面処理剤:リン酸エステル系化合物(末端にメタクリル酸エステル基を含む)、比表面積S=2.0m2/g、表面処理剤に由来する部分の質量割合T=0.5質量%、T/S=0.25)
[反応型化合物(E)]
(E1)
カルボジイミド化合物(Rhein Chemie社製“Stabaxol I-LF”
(E2)
エポキシ化合物(日産化学社製“TEPIC-S”)
[ポリ乳酸系フィルムの作成]
(実施例1)
ポリ乳酸樹脂(A1)15質量部、ポリ乳酸樹脂(A3)45質量部、ポリブチレンアジペート・テレフタレート樹脂(B1)20質量部、ブロック共重合体可塑剤(B4)20質量部、充填剤(C1)70質量部の混合物をシリンダー温度190℃のスクリュー径44mmの真空ベント付き2軸押出機に供し、真空ベント部を脱気しながら溶融混練し、均質化した後にペレット化して組成物を得た。
(実施例2~8、17~29、比較例1~3)
フィルムの組成を表のように変更した以外は、実施例1と同様にしてフィルムを得た。得られたフィルムの物性を表1に示した。
(実施例9)
ポリ乳酸樹脂(A1)15質量部、ポリ乳酸樹脂(A3)45質量部、ポリブチレンアジペート・テレフタレート樹脂(B1)20質量部、ブロック共重合体可塑剤(B4)20質量部、充填剤(C1)70質量部の混合物をシリンダー温度190℃のスクリュー径44mmの真空ベント付き2軸押出機に供し、真空ベント部を脱気しながら溶融混練し、均質化した後にペレット化して組成物を得た。
(実施例10~16、30~42、比較例4~6)
フィルムの組成を表2のように変更した以外は、実施例9と同様にしてフィルムを得た。得られたフィルムの物性を表2に示した。
Claims (10)
- 樹脂(A)としてポリ乳酸系樹脂、樹脂(B)としてポリ乳酸系樹脂以外の熱可塑性樹脂、充填剤(C)として表面処理剤により処理された化合物を含む組成物からなるフィルムであり、
前記ポリ乳酸系樹脂が、結晶性ポリ乳酸系樹脂及び非晶性ポリ乳酸系樹脂を含み、
樹脂(A)と樹脂(B)の合計100質量%において、樹脂(A)を10~95質量%、樹脂(B)を5~90質量%含有し、樹脂(A)と樹脂(B)の合計100質量部に対して、充填剤(C)を10~400質量部含有する組成物からなることを特徴とする、ポリ乳酸系フィルム。 - 前記表面処理剤が、リン酸エステル系化合物及び/又は脂肪酸であることを特徴とする、請求項1に記載のポリ乳酸系フィルム。
- 前記表面処理剤が、メタクリル酸エステル基を含むことを特徴とする、請求項1または2に記載のポリ乳酸系フィルム。
- 前記充填剤(C)が、無機充填剤および/または有機充填剤に対して、表面処理剤で処理することで得られたであり、該無機充填剤および/または有機充填剤の比表面積S(m2/g)と、前記充填剤(C)中の表面処理剤に由来する部分の質量割合T(質量%)が以下の条件を満たすことを特徴とする、請求項1~3のいずれかに記載のポリ乳酸系フィルム。
条件:0.15≦T/S≦0.45 - 前記樹脂(B)が、ポリエーテル系セグメントとポリ乳酸セグメントとを有するブロック共重合体、ポリエステル系セグメントとポリ乳酸セグメントとを有するブロック共重合体、脂肪族ポリエステル系樹脂、及び脂肪族芳香族ポリエステル系樹脂からなる群より選ばれる少なくとも1つの樹脂であることを特徴とする、請求項1~4のいずれかに記載のポリ乳酸系フィルム。
- 前記樹脂(B)が、ポリエーテル系セグメントとポリ乳酸セグメントとを有するブロック共重合体及びポリエステル系セグメントとポリ乳酸セグメントとを有するブロック共重合体からなる群より選ばれる少なくとも1つの樹脂、並びに、脂肪族ポリエステル系樹脂及び脂肪族芳香族ポリエステル系樹脂からなる群より選ばれる少なくとも1つの樹脂からなること特徴とする、請求項5に記載のポリ乳酸系フィルム。
- 樹脂(A)及び/又は樹脂(B)に対して反応型化合物を反応させた組成物を用いて得られることを特徴とする、請求項1~6のいずれかに記載のポリ乳酸系フィルム。
- 引張伸度が150~500%であることを特徴とする、請求項1~7のいずれかに記載のポリ乳酸系フィルム。
- 引張弾性率が100~1,500MPaであることを特徴とする請求項1~8のいずれかに記載のポリ乳酸系フィルム。
- 樹脂(A)としてポリ乳酸系樹脂、並びに、樹脂全体の合計100質量部に対し、充填剤(C)及び/又は充填剤(D)を10~400質量部含む組成物からなるフィルムであり、
前記充填剤(C)が、表面処理剤により処理された化合物であり、
前記充填剤(D)が、表面処理剤により処理されていない無機充填剤及び/又は有機充填剤であり、
引張伸度が150~500%であることを特徴とする、ポリ乳酸系フィルム。
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2013031755A1 (ja) * | 2011-08-31 | 2013-03-07 | 東レ株式会社 | ポリ乳酸系フィルム |
JP2014074148A (ja) * | 2012-09-11 | 2014-04-24 | Fuji Xerox Co Ltd | 樹脂組成物、および樹脂成形体 |
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Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03285944A (ja) * | 1990-03-30 | 1991-12-17 | Toyobo Co Ltd | 配向ポリエステルフイルム |
JPH0439336A (ja) * | 1990-06-01 | 1992-02-10 | Toyobo Co Ltd | 配向ポリエステルフイルム |
JPH07331038A (ja) * | 1994-06-01 | 1995-12-19 | Toray Ind Inc | ポリエステル系樹脂用改質剤、ポリエステル組成物およびそれからなる成形品 |
JP2004149679A (ja) | 2002-10-31 | 2004-05-27 | Unitika Ltd | 生分解性を有する多孔性フィルムおよびその製造方法 |
JP2007112867A (ja) | 2005-10-19 | 2007-05-10 | Kao Corp | 多孔性シート |
JP2008169239A (ja) * | 2007-01-09 | 2008-07-24 | Toray Ind Inc | ポリエステルフィルム |
JP2009138085A (ja) * | 2007-12-06 | 2009-06-25 | Toray Ind Inc | ポリ乳酸系フィルム |
Family Cites Families (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS603431B2 (ja) * | 1980-12-24 | 1985-01-28 | 株式会社 白石中央研究所 | 表面改質無機充填剤 |
JP2695479B2 (ja) * | 1989-03-16 | 1997-12-24 | 株式会社クラレ | 表面処理された無機粉末及び該粉末を含有する樹脂組成物 |
JP2695467B2 (ja) | 1989-05-10 | 1997-12-24 | 株式会社クラレ | 表面処理された無機粉末 |
JPH11256045A (ja) * | 1998-03-06 | 1999-09-21 | Sumitomo Chem Co Ltd | 異方性粒子含有成形品およびその用途 |
JP3410075B2 (ja) * | 2000-11-17 | 2003-05-26 | ユニチカ株式会社 | 結晶性ポリ乳酸樹脂組成物、これを用いたフィルムおよびシート |
JP2003082140A (ja) * | 2001-09-10 | 2003-03-19 | Unitika Ltd | 生分解性を有する多孔性フィルム及びその製造方法 |
CN1305940C (zh) * | 2001-11-01 | 2007-03-21 | 旭化成生活制品株式会社 | 聚乳酸树脂双轴定向膜 |
JP2004176042A (ja) * | 2002-10-04 | 2004-06-24 | Toray Ind Inc | 容器成形用白色ポリエステルフィルムおよび容器 |
JP2004292677A (ja) * | 2003-03-27 | 2004-10-21 | Kuraray Co Ltd | 樹脂組成物、多層構造体及び成形品 |
JP4313076B2 (ja) * | 2003-04-16 | 2009-08-12 | ユニチカ株式会社 | 生分解性ポリエステル系フィルムおよびその製造方法 |
JP2005263931A (ja) * | 2004-03-17 | 2005-09-29 | Asahi Kasei Life & Living Corp | 無機フィラー入り艶消しフィルム |
US20090171065A1 (en) * | 2006-02-16 | 2009-07-02 | Toray Industries, Inc. A Corporation Of Japan | Polyether-polylactic acid composition and polylactic acid film containing same |
JP2009138180A (ja) * | 2007-11-14 | 2009-06-25 | Dic Corp | ポリカーボネート樹脂組成物 |
EP2285902B1 (en) * | 2008-06-13 | 2016-10-26 | Toray Plastics (America) , Inc. | Matte biaxially oriented polylactic acid film |
CN101638509B (zh) * | 2009-07-31 | 2011-06-01 | 四川大学 | 制备增韧型碳酸钙填充聚乳酸的方法 |
KR20130108277A (ko) * | 2010-08-18 | 2013-10-02 | 도레이 카부시키가이샤 | 다공성 필름 |
-
2012
- 2012-01-24 EP EP12749284.1A patent/EP2679633A4/en not_active Withdrawn
- 2012-01-24 CN CN201280009441.7A patent/CN103384702B/zh active Active
- 2012-01-24 JP JP2012506015A patent/JP5751250B2/ja active Active
- 2012-01-24 KR KR1020137022278A patent/KR20140007859A/ko not_active Application Discontinuation
- 2012-01-24 WO PCT/JP2012/051421 patent/WO2012114810A1/ja active Application Filing
- 2012-01-24 US US14/000,904 patent/US8927632B2/en not_active Expired - Fee Related
- 2012-02-21 TW TW101105557A patent/TWI510546B/zh not_active IP Right Cessation
-
2015
- 2015-03-13 JP JP2015050587A patent/JP2015108160A/ja active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03285944A (ja) * | 1990-03-30 | 1991-12-17 | Toyobo Co Ltd | 配向ポリエステルフイルム |
JPH0439336A (ja) * | 1990-06-01 | 1992-02-10 | Toyobo Co Ltd | 配向ポリエステルフイルム |
JPH07331038A (ja) * | 1994-06-01 | 1995-12-19 | Toray Ind Inc | ポリエステル系樹脂用改質剤、ポリエステル組成物およびそれからなる成形品 |
JP2004149679A (ja) | 2002-10-31 | 2004-05-27 | Unitika Ltd | 生分解性を有する多孔性フィルムおよびその製造方法 |
JP2007112867A (ja) | 2005-10-19 | 2007-05-10 | Kao Corp | 多孔性シート |
JP2008169239A (ja) * | 2007-01-09 | 2008-07-24 | Toray Ind Inc | ポリエステルフィルム |
JP2009138085A (ja) * | 2007-12-06 | 2009-06-25 | Toray Ind Inc | ポリ乳酸系フィルム |
Non-Patent Citations (1)
Title |
---|
See also references of EP2679633A4 |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2013031755A1 (ja) * | 2011-08-31 | 2013-03-07 | 東レ株式会社 | ポリ乳酸系フィルム |
JP2014074148A (ja) * | 2012-09-11 | 2014-04-24 | Fuji Xerox Co Ltd | 樹脂組成物、および樹脂成形体 |
WO2014069379A1 (en) * | 2012-11-01 | 2014-05-08 | Toray Industries,Inc. | Multi-layered film |
US20140186563A1 (en) * | 2012-12-27 | 2014-07-03 | University Of Massachusetts | Stabilized polyester based compositions |
US10059839B2 (en) * | 2012-12-27 | 2018-08-28 | University Of Massachusetts | Stabilized polyester based compositions |
Also Published As
Publication number | Publication date |
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TW201241083A (en) | 2012-10-16 |
US8927632B2 (en) | 2015-01-06 |
JP2015108160A (ja) | 2015-06-11 |
JP5751250B2 (ja) | 2015-07-22 |
KR20140007859A (ko) | 2014-01-20 |
JPWO2012114810A1 (ja) | 2014-07-07 |
TWI510546B (zh) | 2015-12-01 |
CN103384702A (zh) | 2013-11-06 |
EP2679633A1 (en) | 2014-01-01 |
US20130331493A1 (en) | 2013-12-12 |
CN103384702B (zh) | 2015-02-18 |
EP2679633A4 (en) | 2017-03-22 |
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