WO2006038507A1 - Polyamide resin molding material for film and process for producing the same - Google Patents

Polyamide resin molding material for film and process for producing the same Download PDF

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Publication number
WO2006038507A1
WO2006038507A1 PCT/JP2005/017852 JP2005017852W WO2006038507A1 WO 2006038507 A1 WO2006038507 A1 WO 2006038507A1 JP 2005017852 W JP2005017852 W JP 2005017852W WO 2006038507 A1 WO2006038507 A1 WO 2006038507A1
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Prior art keywords
film
weight
polyamide resin
inorganic particles
molding material
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PCT/JP2005/017852
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French (fr)
Japanese (ja)
Inventor
Hajime Ooyama
Morio Tsunoda
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Mitsubishi Engineering-Plastics Corporation
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Publication of WO2006038507A1 publication Critical patent/WO2006038507A1/en

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/20Compounding polymers with additives, e.g. colouring
    • C08J3/22Compounding polymers with additives, e.g. colouring using masterbatch techniques
    • C08J3/226Compounding polymers with additives, e.g. colouring using masterbatch techniques using a polymer as a carrier
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2377/00Characterised by the use of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2477/00Characterised by the use of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/16Nitrogen-containing compounds
    • C08K5/20Carboxylic acid amides
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K9/00Use of pretreated ingredients
    • C08K9/08Ingredients agglomerated by treatment with a binding agent

Definitions

  • the present invention relates to a polyamide resin molding material suitable for producing a polyamide resin film excellent in transparency, slipperiness, printability, appearance and productivity, and a film obtained therefrom.
  • Polyamide resin films are excellent in gas barrier properties, mechanical 'thermal properties, etc., and therefore are mainly composed of food packaging, single layer films, multilayer films with other resins, and other materials. It is used in a wide range of applications as a laminated film.
  • the transparency of the polyamide resin film is an important characteristic because it greatly affects the appearance of the contents. In general, a film having good transparency is desired.
  • the slipperiness is poor, the film may be caught during bag making, or the ink may be misaligned during multicolor printing. For this reason, the slipperiness of the film is an extremely important characteristic of film productivity, quality and commercial value. Thus, it is necessary to achieve both transparency and slipperiness of the film, but the surface of the film with good transparency is smooth. The smooth surface of the film is slippery.
  • Patent Document 1 Japanese Patent Publication No.54-4741
  • Patent Document 2 Japanese Patent Publication No. 44-9825
  • Patent Document 3 Japanese Patent Application Laid-Open No. 63-251460
  • the present invention overcomes the disadvantages of the polyimide resin for film produced by the conventional method of blending inorganic particles as described above, and has excellent transparency, slipperiness and printability, and continuous film formation.
  • An object of the present invention is to provide a polyamide resin molding material for a film that does not easily cause appearance defects such as die lines and fish eyes even if it is performed.
  • the first gist of the present invention is that the total of (A) and (B) is 100 parts by weight, (A) 90 to 99 parts by weight of polyamide resin pellets, and (B) polyamide resin 2-8% by weight of inorganic particles and Master batch 10 to 1 parts by weight blended bisamide compound 1-5 wt 0/0, (C) Bisua bromide compound powder 0.1 005-0. 1 made by mixing parts by weight film for polyamide ⁇ molding Lies in the material.
  • the second gist of the present invention is that the total of (A) and (B) is 100 parts by weight, (A) 90 to 99 parts by weight of polyamide resin pellets, and (B) inorganic particles in polyamide resin. and 2-8 weight 0/0 and bisamide compound 1-5 wt% masterbatch 10-1 parts by weight blended, (C) a bisamide compound powder 0.1 005-0. 1 part by weight of a film manufacturing extruder
  • the present invention resides in a method for producing a polyamide resin film characterized in that the film is formed into a film.
  • the third gist of the present invention resides in a polyamide resin film in which the above-mentioned polyamide resin molding material strength is also formed.
  • the polyamide resin molding material for film according to the present invention includes the components (A), (B), and (C) as compounding, as is apparent from the description of the present specification.
  • it is a material that is uniformly stirred and mixed (referred to as “dry blend”) in a mixing device such as a tumbler mixer or a nauter mixer, and is used for film production as it is.
  • a mixture obtained by stirring and mixing (A), (B), and (C) in a mixing apparatus as described above may be referred to as a dry blend.
  • the polyamide resin molding material of the present invention By using the polyamide resin molding material of the present invention, it is possible to continuously form a film for a long time without stopping production, and the resulting film has an appearance, transparency, The excellent slipperiness and printability can be expected to reduce the manufacturing cost and expand the application to food packaging of polyamide resin film.
  • the polyamide resin used in the polyamide resin pellet is a polyamide obtained by polycondensation of ratata having a three-membered ring or more, polymerizable ⁇ -amino acid, dibasic acid and diamine, and the like. ⁇ ⁇ can be used.
  • ⁇ -force prolatatam aminocaproic acid, enantolactam and other ratatams
  • 7 aminoheptanoic acid 11 aminoundeca Polymers of ⁇ -amino acids such as acid, 9-aminononanoic acid, pyrrolidone, and ⁇ -piperidone
  • hexamethylenediamine nonamethylenediamine, undecamethylenediamine, dodecamethylenediamine
  • examples thereof include polycondensates of diamines such as metaxylene diamine and dicarboxylic acids such as terephthalic acid, isophthalic acid, adipic acid, sebacic acid, dodecanedioic acid, and glutaric acid, or copolymers thereof.
  • polyamide 4 6, 7, 8, 11, 12, 6, 6, 6, 10, 11, 6, 12, 6 ⁇ , 6/6-6, 6/12, 6 / 6 ⁇ , 6 ⁇ 6 ⁇ ⁇ ⁇ Illustrated.
  • These polyamide resin may be used alone or in combination of two or more.
  • polyamide 6 resin and polyamide 6-66 copolymer resin can be preferably used from the viewpoint of thermal and mechanical properties of the obtained film.
  • the shape of the polyamide resin pellets ( ⁇ ⁇ ⁇ ⁇ ) in the present invention may be any of a sphere, a cylinder, a prism, and a plate, but the pellet volume is preferably about 0.5 to 10 cm 3 Zg. More preferably, it is l-8cm 3 Zg.
  • pellets having a length of 1 to 5 mm and a diameter of 1 to 4 mm are easy to handle in the production of the polyamide resin material of the present invention, and bite into the extruder during film formation.
  • the stability force of is preferably used.
  • the viscosity number measured at 96% sulfuric acid concentration 1% and the temperature at 23 ° C is usually 115 to 300, preferably It is in the range of 130-210. If the viscosity number is too low, the resulting film has insufficient mechanical properties, and if it is too high, film formation becomes difficult.
  • the amount of water extract measured in accordance with JIS K6920-1 which is a method for measuring the content of low molecular weight substances in the polyamide resin used in the present invention is usually 1% by weight or less, Preferably it is 0.5 weight% or less.
  • the amount of water extraction is large, low molecular weight materials such as monomers and dimers easily adhere to the periphery of the die mouth, and such low molecular weight materials come into contact with or adhere to the film. Appearance defects are likely to occur.
  • the kind of the inorganic particles used in the present invention is not particularly limited, and any of the conventionally used inorganic fillers can be selected and used.
  • silica-alumina clay minerals hydroous aluminum silicates
  • kaolin kaolin
  • calcined kaolin silica-magnesium
  • talc calcium silicate
  • silica zeolite
  • alumina calcium carbonate
  • talc kaolin
  • calcined kaolin, silica and zeolite are also suitable for easy dispersibility.
  • silica and zeolite are particularly suitable.
  • These inorganic particles do not contain particles having a particle size of 10 ⁇ m or more and have an average particle size of 0.4 to 6
  • ⁇ / z m Those in the range of / z m are preferred. If the particle size is large, it will cause the generation of fish eyes. If the particle size is too large, the dispersibility will be poor, and it will be easy to cause fishery due to secondary aggregation of inorganic particles.
  • the inorganic particles are used alone or in combination of two or more.
  • any of so-called wet silica and dry silica can be used, and the specific surface area by the BET method is usually 50 m 2 Zg or more, preferably 100 m 2.
  • the oil absorption measured according to JIS K5101-13 is usually 50 mlZlOOg or more.
  • the zeolite that is preferably used as the inorganic particles of the present invention may be either amorphous or crystalline, but is preferably zeolite that is amorphous as measured by the X-ray method.
  • shape of zeolite it may be spherical or polygonal fine particles. Preferably, it has a spherical or cubic shape.
  • the amount of oil absorption measured by ZEOLITE by the JIS K5101-13 method is usually 1 to 70 mlZlOg, preferably 5 to 70 mlZlOOg. If the oil absorption is too low, the stretching stability will decrease, and if it is too high, the effect of improving the slipping property will be small when stretched. Also, the chemical composition of zeolite is: Si O force 0-60% by weight, Al O force 3 ⁇ 40-45% by weight, Na O 6-9% by weight, CaO 0-8%
  • the inorganic particles used in the present invention are surface-treated with a known surface treatment agent such as a silane coupling agent (silane treatment agent) or a titanium-based treatment agent, good dispersion is obtained. It is preferable because the transparency of the resulting film is improved at the same time that the properties are obtained.
  • the type of surface treatment agent and the surface treatment method are not particularly limited, but treatment with a silane coupling agent is preferred. In particular, when surface-treated silica or zeolite is used as the inorganic particles, favorable results are obtained in terms of transparency and slipperiness of the resulting film.
  • the silane coupling agent preferably used in the present invention has an organosiloxane group.
  • the organo group include alkyl groups such as methyl, ethyl and propyl; alkenyl groups such as butyl and allyl; cycloalkyl groups such as cyclopropyl and cyclohexyl; aryl groups such as phenyl and benzyl; ⁇ -Aminopropyl, ⁇ - ( ⁇ -aminoethyl) Contains functional groups such as chloro, thiol, and epoxy, such as aminoalkyl groups such as ⁇ -aminominopropyl, ⁇ -glycidoxy, ⁇ -chloropropyl, and ⁇ mercaptopropyl.
  • the amount of the silane coupling agent used is usually 1 to 99% by weight, preferably 2 to 70% by weight, more preferably 5 to 40% by weight, based on the inorganic particles. If the amount of the silane coupling agent used is less than 1% by weight relative to the inorganic particles, the effect of preventing film turbidity will be reduced. On the other hand, if it exceeds 99% by weight, the coupling agents will easily aggregate. There are features that cause poor appearance such as fish eyes in the film.
  • the method of surface treatment of inorganic particles with a silane coupling agent is not particularly limited, and is a method known per se. Specifically, for example, inorganic particles treated with a silane coupling agent are added to the inorganic particles with a silane coupling agent diluted with water under heating. Prepared and dried, blended during the production of the masterbatch (B), melt-kneaded, or dry blending of inorganic particles, silane coupling agent and polyamide resin, and blending For example, a method of melt-kneading a product to produce a master batch can be used.
  • the blending amount of the inorganic particles in the master batch (B) of the present invention is 2 to 8% by weight. If the amount of inorganic particles is less than 2% by weight, a large amount of masterbatch is used, resulting in poor thermal stability during film production and a reduction in film quality. On the other hand, when the content is more than 8% by weight, the dispersion of the inorganic particles is lowered and the appearance of the film such as fish eye is deteriorated.
  • the blending amount of the inorganic particles in the master batch is more preferably 2.5 to 7.5% by weight, particularly preferably 3 to 7% by weight.
  • R 1 represents a divalent hydrocarbon residue
  • R 2 and R 3 represent a monovalent hydrocarbon residue
  • R 4 and R 5 represent a hydrogen atom, or a monovalent hydrocarbon residue.
  • Examples of the bisamido compound of the general formula [I] include alkylene bis fatty acid amides and arylene bis fatty acid amides obtained by reaction of diamine and monocarboxylic acid.
  • Examples of the diamine include ethylene diamine, propylene diamine, butylene diamine, hexamethylene diamine, otatamethylene diamine, dodecamethylene diamine etc.
  • arylene alkyldiamines such as arylenediamine and xylylenediamine.
  • Monocarboxylic acids include fatty acids such as stearic acid, hexanoic acid, octanoic acid, decanoic acid, lauric acid, myristic acid, palmitic acid, arachidic acid, behenic acid, oleic acid, elaidic acid, and montanic acid. Can be mentioned.
  • N, N'-methylenebis Mention may be made of the tea amide and N, N'-ethylenebisstearic amide.
  • the bisamido compound represented by the general formula [ ⁇ ] is obtained by the reaction of a monoamine and a dicarboxylic acid.
  • the monoamine include alkylamines such as ethylamine, methylamine, butylamine, hexylamine, decylamine, pentadecylamine, octadecylamine, dodecylamine, aralkylamines such as a-line and naphthylamine, aralkylamines such as benzylamine, and cyclohexylamine.
  • dicarboxylic acid examples include terephthalic acid, p-phenylene dipropionic acid, succinic acid, and adipic acid.
  • representative examples include dioctadecyl dibasic acid amides such as N, N′-dioctadecyl terephthalic acid amide.
  • the bisamidite compound is characterized by being divided and mixed in the master notch of the component (B) and the bisamidyl compound powder of the component (C).
  • component of the bi Suamido compound as the amount in (master batch), 1 to 5 wt 0/0, the amount of component (C) (powder) is,
  • A) component and (B) It is 0.005 to 0.1 part by weight with respect to 100 parts by weight of the total of the components, and the blending amount of the entire polyamide resin molding material of the present invention is preferably 0.005 with respect to the total polyamide resin.
  • the bisamide compound is blended mainly for the purpose of improving the transparency and slipperiness of the film, but the bisamide in the component (B) is the dispersibility of the inorganic particles.
  • the bisamide powder as component (C) is essential for the stability of biting into the extruder. Therefore, in the component (B), the blending ratio (weight ratio) of the inorganic particle Z bisamide compound is preferably in the range of 1 to 5.
  • the blending ratio is less than 1 and the blending amount of the bisamide compound is 5% by weight or more, the dispersibility of the inorganic particles, which is difficult to stably melt and knead during the production of the masterbatch, is also lowered. If the blending ratio is larger than 5, the resulting film is difficult to disperse, and poor appearance tends to occur.
  • the production method of the masterbatch that is the component (B) of the present invention is not particularly limited, and is produced by a known method, preferably in the form of pellets.
  • a certain amount of polyamide Master blend pellets can be obtained by dry blending the resin, inorganic particles and bisamide compound, then melting and kneading with an extruder, and pelletizing with a conventional method.
  • the shape and size of the masterbatch pellets are the same as or similar to those of the polyamide resin pellets (A). From the viewpoint of preventing separation of the masterbatch and the polyamide pellets.
  • the molding material of the present invention comprises the three components of polyamide resin, inorganic particles and bisamide compound as essential components.
  • the production of such a three-component composition is usually performed by dry blending the three components together or by adding inorganic particles internally during the polymerization of the polyamide and dry blending the biamide compound.
  • a masterbatch (B) was prepared by blending 2 to 8% by weight of inorganic particles and 1 to 5% by weight of a bisamide compound in polyamide, and the masterbatch (B) and bisamide compound powder (C) were prepared. And 3 types of polyamide rosin pellets (A).
  • the content is less than 1% by weight, the inorganic particles are dispersed unevenly in the film, resulting in uneven transparency. If it is more than 10% by weight, the thermal stability deteriorates during film production, and poor film appearance tends to occur.
  • the blending amount of the bisamide compound powder (C) is 0.005 to 0.1 parts by weight, preferably 0.01 to 0.08 parts by weight per 100 parts by weight of the total amount of the components (A) and (B). is there. Less than 005 wt.%! / ⁇ and stable bite into the extruder during the manufacture of FINOLEM is not guaranteed, and if more than 0.1 wt.%, Stable bite into the beam extruder A failure occurs.
  • the polyamide used in the polyamide resin pellet (A) and the master notch (B) may be the same or different. If they are different, the melting point or melt viscosity of the polyamide in the masterbatch (B) is preferably lower than those of the polyamide resin pellet (A).
  • the bisamide compound in the master batch (B) and the bisamide compound in the bisamide compound powder (C) The compound may be the same or different.
  • the material according to the present invention is manufactured by mixing the components (A), (B), and (C).
  • A), (B) and (C) are dry blended and supplied to the hopper of an extruder for film production, and (A), (B) and (C) are separately supplied to the hopper of a film production extruder.
  • a method using a fixed amount feeder can be preferably used.
  • the material of the present invention can contain additives within a range that does not impair the effects of the present invention.
  • it contains a partial ester compound of tri- to hexavalent aliphatic alcohol and C10-22 fatty acid and magnesium metal salt of Z or hydroxy fatty acid Let me do it.
  • Examples of the aliphatic alcohol of a partial ester compound of a tri- to hexavalent aliphatic alcohol and a fatty acid having 10 to 22 carbon atoms include glycerin, trimethylpropane, pentaerythritol, mesoerythritol, and sorbitol. Carbon number
  • Examples of the fatty acids 10 to 22 include lauric acid, myristic acid, palmitic acid, stearic acid, behenic acid and the like.
  • a substituent such as a hydroxyl group may be present in the carbon skeleton of the fatty acid.
  • Such an ester compound of an aliphatic alcohol and a fatty acid needs to be substantially a partial ester, and preferably 30% or more of the total hydroxyl groups in the polyhydric alcohol are not esterified and remain. Is used.
  • glycerin monostearate, glycerin distearate, glycerin monobehenate, glycerin distearate, pentaerythritol monostearate, pentaerythritol distearate, pentaerythritol monobehenate, pentaerythritol dibehenate, etc. is preferred.
  • Such partial ester compounds can be used alone or in combination of a plurality of compounds.
  • the magnesium metal salt of hydroxy fatty acid is a salt of hydroxycarbonic acid having 12 to 30 carbon atoms and magnesium, for example, by direct reaction with hydroxycarboxylic acid and magnesium oxide or hydroxide. Can be obtained. In this case, a better result can be obtained by adding magnesium oxide or hydroxide in excess to synthesize a highly basic hydroxy fatty acid magnesium salt.
  • lauric acid, myristic acid A magnesium salt of a compound obtained by hydroxylating an aliphatic carboxylic acid such as palmitic acid, stearic acid or behenic acid. If the fatty acid has a small number of carbon atoms, a predetermined effect cannot be obtained.
  • the blending amount of the partial ester compound of aliphatic alcohol and fatty acid and the magnesium salt of hydroxy fatty acid is usually from 0.01 to 0.7 parts by weight, preferably from 0.03 to 0.7 parts per 100 parts by weight of the polyamide resin. 0. 4 parts by weight. If the blending amount is small, the effect of improving the appearance of the resulting film is insufficient, and if the blending amount is too large, the printing characteristics deteriorate.
  • the combination of the partial ester of the polyhydric alcohol and the magnesium metal salt of the hydroxy fatty acid may be a so-called external addition method in which dry blending is performed on the pelletized raw material of polyamide resin, a kneading method in which melt mixing is performed, or a high concentration
  • a so-called master one-batch method in which the raw materials contained in the compound are blended or an internal addition method to be added during polymerization can be used.
  • additives well known to those skilled in the art for example, hindered phenol, anti-oxidation agents such as phosphate ester and phosphite ester, and weather resistance improvement of triazine compounds, etc.
  • Contains colorants such as colorants, pigments and dyes, antistatic agents, lubricants, and surfactants.
  • the predetermined amount of component (C) and, if necessary, other additives may be dry blended in advance, or supplied to a molding machine for film production without preblending, and film formation may be performed according to a conventional method.
  • the film forming method to which the molding material of the present invention is applied is a force to which any of the known film forming methods can be applied, preferably the T-die method, the inflation method and the like.
  • the polyamide film of the present invention is used as an unstretched film or as a stretched film through a stretching process such as uniaxial stretching or biaxial stretching.
  • the film using the molding material of the present invention may be a single-layer polyamide film or a laminated film with other resin by coextrusion or lamination.
  • the thickness of the polyamide resin film of the present invention is not particularly limited, but if it is thick, the gas-noirality is improved, but the transparency is lowered. The strength you have is reduced.
  • the thickness of the polyamide resin monolayer is usually 2 to 100 ⁇ m for an unstretched film and usually 2 to 50 ⁇ m for a stretched film.
  • the thickness is usually about 10 to 300 m, and the thickness of the polyamide resin layer is preferably in the same range as the thickness of the single layer.
  • Polyamide resin Polyamide-6, “Novamid (registered trademark) 1020J” manufactured by Mitsubishi Engineering Plastics Co., Ltd., Viscosity number 182, Pellet size: Cylindrical shape with a length of 3mm and a diameter of 2.5mm
  • Inorganic particles 1 Silica, “Silysia 310” manufactured by Fuji Silysia Chemical Ltd., average particle size 2.5 m, specific surface area 300 m 2 Zg, oil absorption 310 ml ZlOOg.
  • Inorganic particles 2 Zeolite, “Silton JC20” manufactured by Mizusawa Chemical Co., Ltd., average particle size 2 .: L m, oil absorption 50 ml ZlOOg.
  • Inorganic particles 3 calcined kaolin, “Satinton No. 5” manufactured by Engelnodne earth, average particle size of 0.8 ⁇ .
  • Silane coupling agent y-aminopropyltriethoxysilane, “A 1100” manufactured by Nippon Kayaku Co., Ltd.
  • Polyamide resin, surface-treated inorganic particles 1 (silica), and bisamide compound are dry blended at a compounding ratio of 92/5/3 (weight ratio), and a twin screw extruder (“TEX30” manufactured by Nippon Steel) The mixture was melt-kneaded at 250 ° C, pelletized and dried to obtain a masterbatch containing inorganic particles and bisamido compound. 1.5 parts by weight of the master batch and 0.05 parts by weight of the bisamide compound powder were dry blended with 100 parts by weight of polyamide resin to obtain a molding material for film.
  • TEX30 twin screw extruder
  • This molding material is supplied to a hopper of a T-die type film-forming machine that has a T-die having a diameter of 600 mm and a T-die having a diameter of 600 mm.
  • a film having a thickness of 135 m was formed at ° C.
  • the bite into the extruder was stable and the film was formed smoothly.
  • use the film 2 hours, 4 hours, 6 hours after the start of film formation The stability of the film formation for a long time was evaluated by observing with the naked eye the presence or absence of streaky appearance defects called die lines.
  • the film 1 hour after the start of film formation was cut into a 120 mm x 120 mm square and simultaneously biaxially stretched 3 x 3 times at 80 ° C with a TM-Long biaxial stretching machine, and then 200 The film was heat fixed in a hot air oven at ° C for 30 seconds to obtain a biaxially stretched film with a thickness of 15 ⁇ m.
  • the haze value and static friction coefficient of the stretched film were measured. The results are shown in Table 2.
  • Polyamide resin, surface-treated inorganic particles 1 (silica), and bisamide compound were dry blended at a blending ratio of 99.83 / 0.075 / 0.095 (weight ratio) to obtain a molding material for film.
  • a film was formed and evaluated in the same manner as in Example 1. The results are shown in Table 2.
  • Surface-treated inorganic particles 1 (silica) was added in an amount of 0.05 to 5% by weight with respect to polyamide 6 during polymerization of polyamide 6, and polymerized by a conventional method to obtain polyamide 6 resin having a viscosity number of 182. .
  • a film molding material was obtained by dry blending the silica-containing polyamide 6 rosin pellets (3 mm in length and 2.5 mm in diameter) into a bisamide compound in an amount of 0.095% by weight. Using this molding material, film formation and evaluation were carried out in the same manner as in Example 1. The results are shown in Table 2.
  • Polyamide rosin and surface-treated inorganic particles 1 were dry blended at a blending ratio of 95Z5 (weight ratio), and melt-kneaded in the same manner as in Example 1 to obtain a master batch in which inorganic particles were blended.
  • 1.5 parts by weight of the master batch and 0.095 parts by weight of the bisamide compound powder were dry blended with 100 parts by weight of polyamide resin to obtain a molding material for film. Using this molding material, film formation and evaluation were carried out in the same manner as in Example 1. The results are shown in Table 2.
  • Polyamide, surface-treated inorganic particles 1 (silica), and a bisamide compound were dry blended at a blending ratio of 87Z10Z3 (weight ratio), and melt-kneaded in the same manner as in Example 1 to blend inorganic particles and a bisamide compound.
  • a master batch was obtained. 0.775 parts by weight of the masterbatch Then, 0.0725 parts by weight of bisamide compound powder and 100 parts by weight of polyamide resin were dry blended to obtain a molding material for film. Using this molding material, film formation and evaluation were carried out in the same manner as in Example 1. The results are shown in Table 2.
  • Polyamide rosin, surface-treated inorganic particles 1 (silica), and bisamide compound were dry blended at a blending ratio of 88.67 / 5 / 6.33 (weight ratio), and melt-kneaded in the same manner as in Example 1 to make inorganic
  • a master batch containing the particles and the bisamide compound was obtained. 1.5 parts by weight of the master batch and 100 parts by weight of polyamide resin were dry blended. Next, using this blend, film formation and evaluation were carried out in the same manner as in Example 1. The results are shown in Table 2.
  • a film molding material was obtained in the same manner as in Example 1 except that the inorganic particles 1 (silica) used in Example 1 were changed to surface-treated inorganic particles 2 (zeolite), and a film was formed. Evaluation was performed. The results are shown in Table 3.
  • a molding material for a film was obtained in the same manner as in Comparative Example 3 except that the inorganic particles 1 (silica) used in Comparative Example 3 were changed to surface-treated inorganic particles 2 (zeolite), and a film was formed. Evaluation was performed. The results are shown in Table 3.
  • a film molding material was obtained in the same manner as in Example 1 except that the inorganic particles 1 (silica) used in Example 1 were changed to surface-treated inorganic particles 3 (calcined kaolin). Went. The results are shown in Table 5.
  • the film of Example 1 formed using the molding material for film of the present invention was the film of Comparative Examples 1 to 3 formed using a material having the same additive composition. Compared with the film quality, the film quality such as transparency, slipperiness, presence of fish eyes and die lines was excellent, and the long-term stability of the film formation was also good.
  • the film formed from the material of Comparative Examples 4 and 5 in which the blending amount of the inorganic particles and the bisamido compound in the master batch is out of the scope of the present invention is stable in fish eyes and long-term film formation. Problems occur. For this reason, the ratio of inorganic particles to bisamide compounds in the masterbatch affects the dispersion of inorganic particles, and coarse particles due to aggregation are It is presumed that this will affect the generation of die and the generation of die lines due to the turbulent flow of grease near the die outlet.
  • the molding material of the present invention is excellent in transparency and slipperiness of the obtained film, can prevent appearance defects such as die lines, and can be continuously stable for a long time. It was. In addition, since it is excellent in slipperiness, it is apparently excellent in printability. Industrial applicability
  • the molding material for polyamide resin film of the present invention is excellent in long-term continuous film-forming stability, and the resulting film has good transparency, slipperiness and printability, and has poor appearance such as die lines. Since it has few excellent characteristics, it is useful for a wide range of food packaging and the like.

Abstract

A polyamide resin molding material for films which is obtained by mixing (A) 90-99 parts by weight of polyamide resin pellets, (B) 10-1 part by weight of a masterbatch comprising a polyamide resin and, compound therewith, 2-8 wt.% inorganic particles and 1-5 wt.% bisamide compound, and (C) 0.005-0.1 part by weight of a bisamide compound powder, the sum of (A) and (B) being 100 parts by weight. The polyamide resin molding material for films is suitable for use in producing a polyamide resin film which is excellent in transparency, slip properties, and printability and which, even when having been formed continuously, is less apt to have appearance defects such as die lines or fisheyes.

Description

明 細 書  Specification
フィルム用ポリアミド樹脂成形材料およびその製造方法  Polyamide resin molding material for film and method for producing the same
技術分野  Technical field
[0001] 本発明は、透明性、滑り性、印刷性、外観および生産性の優れたポリアミド榭脂フィ ルムの製造に好適なポリアミド榭脂成形材料およびそれから得られるフィルムに関す る。  The present invention relates to a polyamide resin molding material suitable for producing a polyamide resin film excellent in transparency, slipperiness, printability, appearance and productivity, and a film obtained therefrom.
背景技術  Background art
[0002] ポリアミド榭脂製フィルムは、ガスバリヤ一性、機械的'熱的特性などに優れて 、る ため、食品包装を主体として、単層フィルム、他榭脂との多層フィルム、他材料とのラ ミネートフィルム等として、広範囲な用途に使用されている。ポリアミド榭脂製フィルム の透明性は、内容物の見栄えに大きく影響するので重要な特性であり、一般的には 透明性が良好なものが要望されている。また、滑り性が悪いと、製袋時にフィルムが 引っ掛力つたり、多色印刷時にインクの印刷ズレが生じたりすることがある。このため、 フィルムの滑り性は、フィルムの生産性や品質 ·商品価値の点力 極めて重要な特性 である。このようにフィルムの透明性と滑り性の両立を図らねばならないが、透明性の 良好なフィルムの表面は平滑である力 平滑なフィルム表面は滑りが悪ぐ両特性は 相反する性質である。  [0002] Polyamide resin films are excellent in gas barrier properties, mechanical 'thermal properties, etc., and therefore are mainly composed of food packaging, single layer films, multilayer films with other resins, and other materials. It is used in a wide range of applications as a laminated film. The transparency of the polyamide resin film is an important characteristic because it greatly affects the appearance of the contents. In general, a film having good transparency is desired. In addition, if the slipperiness is poor, the film may be caught during bag making, or the ink may be misaligned during multicolor printing. For this reason, the slipperiness of the film is an extremely important characteristic of film productivity, quality and commercial value. Thus, it is necessary to achieve both transparency and slipperiness of the film, but the surface of the film with good transparency is smooth. The smooth surface of the film is slippery.
[0003] 力かるポリアミド榭脂製フィルムの改良のために、従来から種々の方法が試みられ てきた。例えば、シリカ、タルク等の無機粒子を配合する方法 (例えば特許文献 1参 照)、特定のビスアミドを配合する方法 (例えば特許文献 2参照)等が知られている。し カゝしながら、無機粒子を配合する方法では、無機粒子の表面活性が高い場合には、 ポリアミド榭脂の熱安定性が不良になり、フィッシュアイと称される粒状欠陥や、ダイラ インと称される筋状の外観不良が生じ易ぐ外観に優れたフィルムを安定的に連続生 産することが難しい。そこで、フィルム用無機粒子として代表的なシリカを配合する場 合に、シリカの表面処理を行うことが提案されている (例えば特許文献 3参照)。かか る処理をした無機粒子とビスアミドを配合することにより透明性と滑り性については比 較的良好な結果が得られる様になった。 [0004] 一方、ポリアミド榭脂にシリカ等の微細無機粒子を配合する一般的な方法として、 ( 1)ペレット表面に静電気を利用して無機粒子を付着させる方法、 (2)ペレット表面に 低粘凋液体を用いて無機粒子を付着させる方法、 (3)無機粒子を高濃度に混練した マスターバッチを製造してポリアミド榭脂と配合する方法、(4)ポリアミド榭脂の重合時 に無機粒子を添加する方法などが採用されてきた。 [0003] Various methods have been attempted in the past to improve a strong polyamide-resin film. For example, a method of blending inorganic particles such as silica and talc (for example, see Patent Document 1), a method of blending a specific bisamide (for example, see Patent Document 2), and the like are known. However, in the method of blending inorganic particles, if the surface activity of the inorganic particles is high, the thermal stability of the polyamide resin becomes poor, and granular defects called fish eyes, It is difficult to stably and continuously produce a film having an excellent appearance that easily causes streak-like appearance defects. In view of this, it has been proposed to treat the surface of silica when typical silica is blended as inorganic particles for film (see, for example, Patent Document 3). By blending such treated inorganic particles and bisamide, comparatively good results were obtained in terms of transparency and slipperiness. [0004] On the other hand, as a general method of blending fine inorganic particles such as silica with polyamide resin, (1) a method of attaching inorganic particles to the pellet surface using static electricity, (2) a low viscosity on the pellet surface A method of adhering inorganic particles using a liquid, (3) A method of manufacturing a masterbatch in which inorganic particles are kneaded at a high concentration and blending with polyamide resin, (4) Inorganic particles during polymerization of polyamide resin Addition methods and the like have been adopted.
[0005] しかし、(1)、 (2)及び(3)の方法により、上述のフィルム改良のための無機粒子や ビスアミドの配合を行っても、ポリアミド榭脂中の無機粒子の分散が不十分なため、得 られるフィルムはフィッシュアイの発生が避けられない。一方 (4)の方法は、無機粒子 の分散は十分良好に行われるが、ポリアミド榭脂の熱安定性が悪くなり、長時間の重 合後のペレットに焼けが混入し、フィルムを製造するとフィッシュアイ、ダイライン等の 外観不良が発生する恐れがある。従って、従来の一般的な無機粒子の配合方法で は、必ずしも外観欠陥の発生しない長時間安定した生産が困難な状況であった。  [0005] However, even when the inorganic particles and bisamide for improving the film are blended by the methods (1), (2) and (3), the dispersion of the inorganic particles in the polyamide resin is insufficient. For this reason, the resulting film cannot avoid the generation of fish eyes. On the other hand, in the method (4), the inorganic particles are dispersed sufficiently well, but the thermal stability of the polyamide resin is deteriorated, and burning is mixed into the pellets after the polymerization for a long time. There is a risk of appearance defects such as eyes and die lines. Therefore, in the conventional general method of blending inorganic particles, stable production for a long time without appearance defects is difficult.
[0006] 特許文献 1 :特公昭 54— 4741号公報  [0006] Patent Document 1: Japanese Patent Publication No.54-4741
特許文献 2:特公昭 44-9825号公報  Patent Document 2: Japanese Patent Publication No. 44-9825
特許文献 3:特開昭 63 - 251460号公報  Patent Document 3: Japanese Patent Application Laid-Open No. 63-251460
発明の開示  Disclosure of the invention
発明が解決しょうとする課題  Problems to be solved by the invention
[0007] 本発明は、上述のような従来の無機粒子の配合法で製造されたフィルム用ポリアミ ド榭脂が有する欠点を克服し、透明性、滑り性、印刷性に優れ、連続製膜を行っても ダイラインやフィッシュアイ等の外観不良が生じ難いフィルム用ポリアミド榭脂成形材 料を提供することを目的とする。 [0007] The present invention overcomes the disadvantages of the polyimide resin for film produced by the conventional method of blending inorganic particles as described above, and has excellent transparency, slipperiness and printability, and continuous film formation. An object of the present invention is to provide a polyamide resin molding material for a film that does not easily cause appearance defects such as die lines and fish eyes even if it is performed.
課題を解決するための手段  Means for solving the problem
[0008] 本発明者らは、上記課題を解決すべく鋭意検討した結果、無機粒子をマスターバ ツチにより、ビスアミドの所定量の一部をマスターバッチにより、ビスアミドの残りを粉体 のまま、それぞれポリアミド榭脂に配合することにより、上記課題を解決できることを見 出し、本発明を完成するに至った。 [0008] As a result of diligent investigations to solve the above problems, the present inventors have determined that each of the inorganic particles by a masterbatch, a predetermined amount of bisamide by a masterbatch, and the remainder of the bisamide in powder form, respectively. It has been found that the above-mentioned problems can be solved by blending with rosin, and the present invention has been completed.
[0009] すなわち、本発明の第 1の要旨は、(A)と (B)の合計を 100重量部として、(A)ポリ アミド榭脂ペレット 90〜99重量部と、 (B)ポリアミド榭脂に無機粒子 2〜8重量%及び ビスアミド化合物 1〜5重量0 /0を配合したマスターバッチ 10〜1重量部と、 (C)ビスァ ミド化合物粉体 0. 005-0. 1重量部とを混合して成るフィルム用ポリアミド榭脂成形 材料に存する。 [0009] That is, the first gist of the present invention is that the total of (A) and (B) is 100 parts by weight, (A) 90 to 99 parts by weight of polyamide resin pellets, and (B) polyamide resin 2-8% by weight of inorganic particles and Master batch 10 to 1 parts by weight blended bisamide compound 1-5 wt 0/0, (C) Bisua bromide compound powder 0.1 005-0. 1 made by mixing parts by weight film for polyamide榭脂molding Lies in the material.
[0010] 本発明の第 2の要旨は、(A)と (B)の合計を 100重量部として、(A)ポリアミド榭脂 ペレット 90〜99重量部と、 (B)ポリアミド榭脂に無機粒子 2〜8重量0 /0及びビスアミド 化合物 1〜5重量%を配合したマスターバッチ 10〜1重量部と、 (C)ビスアミド化合物 粉体 0. 005-0. 1重量部とをフィルム製造用押出機に供給し、成膜することを特徴 とするポリアミド榭脂フィルムの製造方法に存する。 [0010] The second gist of the present invention is that the total of (A) and (B) is 100 parts by weight, (A) 90 to 99 parts by weight of polyamide resin pellets, and (B) inorganic particles in polyamide resin. and 2-8 weight 0/0 and bisamide compound 1-5 wt% masterbatch 10-1 parts by weight blended, (C) a bisamide compound powder 0.1 005-0. 1 part by weight of a film manufacturing extruder The present invention resides in a method for producing a polyamide resin film characterized in that the film is formed into a film.
[0011] 本発明の第 3の要旨は、上記のポリアミド榭脂成形材料力も成形されたポリアミド榭 脂フィルムに存する。  [0011] The third gist of the present invention resides in a polyamide resin film in which the above-mentioned polyamide resin molding material strength is also formed.
[0012] なお、本発明に係わるフィルム用ポリアミド榭脂成形材料とは、本明細書の記載か ら明らかな様に、(A)、(B)、(C)の成分を、コンパゥンデイングと称される溶融混練を することなぐ好ましくは、例えばタンブラ一ミキサーやナウターミキサー等の混合装 置にて均一に攪拌混合した(「ドライブレンド」と称す。)材料であり、そのままフィルム 製造用の成形機に供給して製膜する材料を称す。なお、上述の如ぐ混合装置にて (A)、(B)、(C)を攪拌混合したものをドライブレンド物と称すこともある。  [0012] It should be noted that the polyamide resin molding material for film according to the present invention includes the components (A), (B), and (C) as compounding, as is apparent from the description of the present specification. Preferably, it is a material that is uniformly stirred and mixed (referred to as “dry blend”) in a mixing device such as a tumbler mixer or a nauter mixer, and is used for film production as it is. A material that is supplied to a molding machine to form a film. A mixture obtained by stirring and mixing (A), (B), and (C) in a mixing apparatus as described above may be referred to as a dry blend.
発明の効果  The invention's effect
[0013] 本発明のポリアミド榭脂成形材料を使用することにより、生産を途中で停止すること なく長時間連続して製膜することが可能であり、且つ、得られるフィルムは外観、透明 性、滑り性、印刷性が優れているので、製造コストの低下が期待できると共に、ポリア ミド榭脂フィルムの食品包装等へ用途を拡大する効果がある。  [0013] By using the polyamide resin molding material of the present invention, it is possible to continuously form a film for a long time without stopping production, and the resulting film has an appearance, transparency, The excellent slipperiness and printability can be expected to reduce the manufacturing cost and expand the application to food packaging of polyamide resin film.
発明を実施するための最良の形態  BEST MODE FOR CARRYING OUT THE INVENTION
[0014] 以下、本発明を詳細に説明するが、以下に記載する構成要件の説明は、本発明の 実施態様の代表例であり、これらの内容に本発明は限定されるものではない。本発 明における (A)ポリアミド榭脂ペレットに使用されるポリアミド榭脂としては、 3員環以 上のラタタム、重合可能な ω—アミノ酸、二塩基酸とジァミン等の重縮合によって得ら れるポリアミド榭脂を用いることが出来る。具体的には、 ε—力プロラタタム、アミノカ プロン酸、ェナントラクタム等のラタタム類; 7 ァミノヘプタン酸、 11 アミノウンデカ ン酸、 9—アミノノナン酸、 ひ ピロリドン、 α—ピぺリドン等の ω—アミノ酸類の重合 体;へキサメチレンジァミン、ノナメチレンジァミン、ゥンデカメチレンジァミン、ドデカメ チレンジァミン、メタキシレンジァミン等のジァミンと、テレフタル酸、イソフタル酸、ァ ジピン酸、セバシン酸、ドデカン二塩基酸、グルタール酸等のジカルボン酸との重縮 合体またはこれらの共重合体が例示される。さらに具体的には、ポリアミド 4、 6、 7、 8 、 11、 12、 6 · 6、 6 · 10、 6 · 11、 6 · 12、 6Τ、 6/6 - 6, 6/12, 6/6Τ, 6ΙΖ6Τ等力 例示される。これらポリアミド榭脂は、単独で使用しても 2種以上を混合して使用して もよい。これらのポリアミド榭脂中、得られるフィルムの熱的.機械的特性の面から、特 にポリアミド 6榭脂、ポリアミド 6Ζ66共重合樹脂が好適に使用できる。 [0014] Hereinafter, the present invention will be described in detail. However, the description of the constituent elements described below is a representative example of embodiments of the present invention, and the present invention is not limited to these contents. In the present invention, (A) the polyamide resin used in the polyamide resin pellet is a polyamide obtained by polycondensation of ratata having a three-membered ring or more, polymerizable ω-amino acid, dibasic acid and diamine, and the like.榭 脂 can be used. Specifically, ε-force prolatatam, aminocaproic acid, enantolactam and other ratatams; 7 aminoheptanoic acid, 11 aminoundeca Polymers of ω-amino acids such as acid, 9-aminononanoic acid, pyrrolidone, and α-piperidone; hexamethylenediamine, nonamethylenediamine, undecamethylenediamine, dodecamethylenediamine, Examples thereof include polycondensates of diamines such as metaxylene diamine and dicarboxylic acids such as terephthalic acid, isophthalic acid, adipic acid, sebacic acid, dodecanedioic acid, and glutaric acid, or copolymers thereof. More specifically, polyamide 4, 6, 7, 8, 11, 12, 6, 6, 6, 10, 11, 6, 12, 6Τ, 6/6-6, 6/12, 6 / 6Τ , 6ΙΖ6Τ 等 力 Illustrated. These polyamide resin may be used alone or in combination of two or more. Among these polyamide resins, polyamide 6 resin and polyamide 6-66 copolymer resin can be preferably used from the viewpoint of thermal and mechanical properties of the obtained film.
[0015] 本発明におけるポリアミド榭脂ペレット (Α)の形状は、球、円筒、角柱、板状のいず れでもよいが、ペレット体積として 0. 5〜10cm3Zg程度の大きさが好ましぐ更に好 ましくは l〜8cm3Zgである。例えば、円柱状においては長さ l〜5mmで、径が 1〜4 mmのペレットが、本発明のポリアミド榭脂材料の製造においての取り扱いやすさ、お よび製膜時の押出機への喰い込みの安定性力 好ましく使用される。 [0015] The shape of the polyamide resin pellets (ペ レ ッ ト) in the present invention may be any of a sphere, a cylinder, a prism, and a plate, but the pellet volume is preferably about 0.5 to 10 cm 3 Zg. More preferably, it is l-8cm 3 Zg. For example, in the case of a cylinder, pellets having a length of 1 to 5 mm and a diameter of 1 to 4 mm are easy to handle in the production of the polyamide resin material of the present invention, and bite into the extruder during film formation. The stability force of is preferably used.
[0016] また、本発明に使用されるポリアミド榭脂において、 JIS K6933— 99に従って、 96 %硫酸中濃度 1%、温度に 23°Cで測定した粘度数は、通常 115〜300、好ましくは 、 130〜210の範囲である。粘度数が低すぎると、得られるフィルムの機械的特性が 不十分であり、高すぎると製膜が困難になる。  [0016] Further, in the polyamide resin used in the present invention, according to JIS K6933-99, the viscosity number measured at 96% sulfuric acid concentration 1% and the temperature at 23 ° C is usually 115 to 300, preferably It is in the range of 130-210. If the viscosity number is too low, the resulting film has insufficient mechanical properties, and if it is too high, film formation becomes difficult.
[0017] 更に、本発明に使用されるポリアミド榭脂において、低分子量物の含有量を測定す る方法である JIS K6920— 1に準じて測定される水抽出量は、通常 1重量%以下、 好ましくは 0. 5重量%以下である。水抽出量が多いと、ダイス口周辺に、モノマー、ダ イマ一を始めとする低分子量物が付着し易ぐそうした低分子量物がフィルムに接し たり、付着したりすることによって、フィッシュアイ等の外観不良が生じ易くなる。  [0017] Furthermore, the amount of water extract measured in accordance with JIS K6920-1 which is a method for measuring the content of low molecular weight substances in the polyamide resin used in the present invention is usually 1% by weight or less, Preferably it is 0.5 weight% or less. When the amount of water extraction is large, low molecular weight materials such as monomers and dimers easily adhere to the periphery of the die mouth, and such low molecular weight materials come into contact with or adhere to the film. Appearance defects are likely to occur.
[0018] 本発明に使用される無機粒子の種類は特に制限はなぐ従来、榭脂の充填材とし て慣用されているものの中から任意のものを選択して使用することが出来る。具体的 には、クレー、カオリン、焼成カオリンに代表されるシリカ アルミナ系粘土鉱物 (含水 ケィ酸アルミニウム類)、タルクに代表されるシリカ マグネシウム類、ケィ酸カルシゥ ム、シリカ、ゼォライト、アルミナ、炭酸カルシウム等が挙げられる力 これらの中で、特 にタルク、カオリン、焼成カオリン、シリカ、ゼォライトが易分散性の点力も好適である 。中でも、シリカ、ゼォライトが特に好適である。 [0018] The kind of the inorganic particles used in the present invention is not particularly limited, and any of the conventionally used inorganic fillers can be selected and used. Specifically, silica-alumina clay minerals (hydrous aluminum silicates) typified by clay, kaolin, calcined kaolin, silica-magnesium typified by talc, calcium silicate, silica, zeolite, alumina, calcium carbonate Among these, among these, special In addition, talc, kaolin, calcined kaolin, silica and zeolite are also suitable for easy dispersibility. Of these, silica and zeolite are particularly suitable.
[0019] これらの無機粒子は、粒径 10 μ m以上の粒子を含まず、かつ平均粒径が 0. 4〜6  [0019] These inorganic particles do not contain particles having a particle size of 10 μm or more and have an average particle size of 0.4 to 6
/z mの範囲にあるものが好適である。粒径が大きいと、フィッシュアイの発生の原因に なり、粒径力 、さ過ぎると分散性が不良になり、また無機粒子の二次凝集によるフイツ シュアィを招き易くなつて好ましくない。  Those in the range of / z m are preferred. If the particle size is large, it will cause the generation of fish eyes. If the particle size is too large, the dispersibility will be poor, and it will be easy to cause fishery due to secondary aggregation of inorganic particles.
[0020] また、無機粒子は、上述のものを 1種単独で、もしくは 2種以上を組み合わせて使用 する。その配合量は、全ポリアミド榭脂、すなわち本発明の成形材料中に占めるポリ アミド榭月旨の総重量を 100%として、 0. 02〜0. 8重量0 /0、好ましくは 0. 05〜0. 5重 量%の範囲で選ばれる。無機粒子の配合量が少ないと、得られるフィルムの滑り性の 改良がみられず、配合量が多すぎると透明性が低下する。 [0020] Further, as the inorganic particles, the above-mentioned particles are used alone or in combination of two or more. The amount thereof, the total polyamide榭脂, i.e. 100% on the total weight of the poly amide榭月fact occupied in the molding material of the present invention, 0.02 to 0.8 wt 0/0, preferably 0. 05~ Selected in the range of 0.5% by weight. If the amount of the inorganic particles is small, the improvement of the slipperiness of the resulting film is not observed, and if the amount is too large, the transparency is lowered.
[0021] 本発明の無機粒子として好ましく使用されるシリカとしては、いわゆる湿式シリカ、及 び乾式シリカの何れも使用出来、 BET法による比表面積が、通常 50m2Zg以上、好 ましくは 100m2Zg以上であり、かつ、 JIS K5101— 13に従って測定した吸油量が 、通常 50mlZlOOg以上である。 As the silica preferably used as the inorganic particles of the present invention, any of so-called wet silica and dry silica can be used, and the specific surface area by the BET method is usually 50 m 2 Zg or more, preferably 100 m 2. The oil absorption measured according to JIS K5101-13 is usually 50 mlZlOOg or more.
[0022] 本発明の無機粒子として好ましく使用されるゼオライトとしては、無定形、結晶形を 問わないが、 X線法の測定で無定形であるゼォライトが好ましい。 X線法で測定して 結晶構造が認められるゼォライトを使用すると、得られるフィルムの延伸安定性が低 下し、延伸破断が頻発しやすい。ゼォライトの形状としては、特に規定はないが、球 状でも多角形状をした微粒子でもよい。好ましくは、球状または立方体の形状を有す るものである。  [0022] The zeolite that is preferably used as the inorganic particles of the present invention may be either amorphous or crystalline, but is preferably zeolite that is amorphous as measured by the X-ray method. Use of zeolite, which has a crystal structure as measured by the X-ray method, reduces the stretching stability of the resulting film and tends to cause frequent stretching breaks. There is no particular limitation on the shape of zeolite, but it may be spherical or polygonal fine particles. Preferably, it has a spherical or cubic shape.
[0023] ゼォライトの JIS K5101— 13法にて測定される吸油量は、通常 l〜70mlZl〇0g 、好ましくは 5〜70mlZlOOgである。吸油量が低すぎると延伸安定性が低下し、高 すぎると延伸した時に滑り性の改良効果が小さい。また、ゼォライトの化学組成は、 Si O力 0〜60重量%、 Al O力 ¾0〜45重量%、 Na Oが 6〜9重量%、 CaOが 0〜8 [0023] The amount of oil absorption measured by ZEOLITE by the JIS K5101-13 method is usually 1 to 70 mlZlOg, preferably 5 to 70 mlZlOOg. If the oil absorption is too low, the stretching stability will decrease, and if it is too high, the effect of improving the slipping property will be small when stretched. Also, the chemical composition of zeolite is: Si O force 0-60% by weight, Al O force ¾0-45% by weight, Na O 6-9% by weight, CaO 0-8%
2 2 3 2 2 2 3 2
重量%であるのが好まし!/、。  It is preferred to be weight%! /.
[0024] 本発明に使用される無機粒子は、シランカップリング剤(シラン処理剤)やチタユウ ム系処理剤等の周知の表面処理剤で表面処理したものを使用すると、良好な分散 性が得られると同時に、得られるフィルムの透明性も改良されるので好ましい。表面 処理剤の種類や表面処理の方法については特に限定されるものではないが、シラン カップリング剤による処理が好ましい。特に、無機粒子として、表面処理されたシリカ、 ゼォライトを用いると、得られるフィルムの透明性、滑り性において好ましい結果が得 られる。 [0024] When the inorganic particles used in the present invention are surface-treated with a known surface treatment agent such as a silane coupling agent (silane treatment agent) or a titanium-based treatment agent, good dispersion is obtained. It is preferable because the transparency of the resulting film is improved at the same time that the properties are obtained. The type of surface treatment agent and the surface treatment method are not particularly limited, but treatment with a silane coupling agent is preferred. In particular, when surface-treated silica or zeolite is used as the inorganic particles, favorable results are obtained in terms of transparency and slipperiness of the resulting film.
[0025] 本発明で好ましく用いるシランカップリング剤としては、オルガノシロキサン基を有す るものである。具体的にオルガノ基としては、メチル、ェチル、プロピル等のアルキル 基;ビュル、ァリル等のァルケ-ル基;シクロプロピル、シクロへキシル等のシクロアル キル基;フエ-ル、ベンジル等のァリール基; γ—ァミノプロピル、 Ν—( β—アミノエ チル) γ—ァミノプロピル等のアミノアルキル基、 γ—グリシドキシ、 γ—クロ口プロ ピル、 γ メルカプトプロピル等のようにクロル、チオール、エポキシ等の官能基を含 むちのち挙げられる。  [0025] The silane coupling agent preferably used in the present invention has an organosiloxane group. Specific examples of the organo group include alkyl groups such as methyl, ethyl and propyl; alkenyl groups such as butyl and allyl; cycloalkyl groups such as cyclopropyl and cyclohexyl; aryl groups such as phenyl and benzyl; γ-Aminopropyl, Ν- (β-aminoethyl) Contains functional groups such as chloro, thiol, and epoxy, such as aminoalkyl groups such as γ-aminominopropyl, γ-glycidoxy, γ-chloropropyl, and γ mercaptopropyl. There is a whip.
[0026] 具体的には、トリメチルメトキシシラン、ビュルトリエトキシシラン、 γ—クロ口プロピル トリメトキシシラン、 γ—ァミノプロピルトリエトキシシラン、 Ν— ( j8—アミノエチル) —ァミノプロピルトリメトキシシラン、 Ί—メルカプトプロピルトリメトキシシラン、 γ—ダリ シドキシプロピルトリメトキシシラン、 γ—メタクリロキシプロピルトリメトキシシラン、へキ サメチルジシラザン、 Ν, Ν,一ビス(トリメチルシリル)ゥレア、 Ν, Ν,一ビス(トリメチル シリル)ァセトアミド、ジェチルトリメチルシリルァミン、 Ν, Ν,—ビス(トリメチルシリル)ト リフロロァセトアミド、ステアリルトリメトキシシラン等を挙げることができる。特に γ アミ ノプロピルトリエトキシシラン等のアミノシランが好適である。 [0026] Specifically, trimethylmethoxysilane, butyltriethoxysilane, γ-chloropropyl methoxytrimethoxysilane, γ-aminopropyltriethoxysilane, Ν- (j8-aminoethyl) -aminopropyltrimethoxysilane , Ί -Mercaptopropyltrimethoxysilane, γ- Dalicydoxypropyltrimethoxysilane , γ-methacryloxypropyltrimethoxysilane, hexamethyldisilazane, Ν, Ν, monobis (trimethylsilyl) urea, Ν, Ν, Examples thereof include monobis (trimethylsilyl) acetamide, jetyltrimethylsilylamine, Ν, Ν, -bis (trimethylsilyl) trifluoroacetamide, stearyltrimethoxysilane, and the like. In particular, aminosilanes such as γ aminopropyltriethoxysilane are suitable.
[0027] シランカップリング剤の使用量は、無機粒子に対して、通常 1〜99重量%、好ましく は 2〜70重量%、さらに好ましくは 5〜40重量%である。シランカップリング剤の使用 量が無機粒子に対して 1重量%より少ないとフィルム白濁化を防止する効果が小さく なり、一方、 99重量%を超えると、カップリング剤同志の凝集が起こり易くなり、フィル ム中のフィッシュアイ等の外観不良となる†具れがある。  [0027] The amount of the silane coupling agent used is usually 1 to 99% by weight, preferably 2 to 70% by weight, more preferably 5 to 40% by weight, based on the inorganic particles. If the amount of the silane coupling agent used is less than 1% by weight relative to the inorganic particles, the effect of preventing film turbidity will be reduced. On the other hand, if it exceeds 99% by weight, the coupling agents will easily aggregate. There are features that cause poor appearance such as fish eyes in the film.
[0028] シランカップリング剤による無機粒子の表面処理の方法は特に制限はなぐそれ自 体公知の方法により行われる。具体的には、例えば、無機粒子に、水で希釈したシラ ンカップリング剤を加熱下に加えて攪拌し、シランカップリング剤で処理した無機粒子 を調製し、乾燥後、これを (B)成分であるマスターバッチの製造時に配合し、溶融混 練する方法、或いは、無機粒子とシランカップリング剤およびポリアミド榭脂とをドライ ブレンドし、そのブレンド物を溶融混練し、マスターバッチの製造を行う方法等が挙げ られる。 [0028] The method of surface treatment of inorganic particles with a silane coupling agent is not particularly limited, and is a method known per se. Specifically, for example, inorganic particles treated with a silane coupling agent are added to the inorganic particles with a silane coupling agent diluted with water under heating. Prepared and dried, blended during the production of the masterbatch (B), melt-kneaded, or dry blending of inorganic particles, silane coupling agent and polyamide resin, and blending For example, a method of melt-kneading a product to produce a master batch can be used.
[0029] 本発明の(B)マスターバッチ中の無機粒子の配合量は 2〜8重量%である。無機粒 子が 2重量%より少ない配合量であると、大量のマスターバッチを使用することになり 、フィルム製造時の熱安定性が悪ィ匕し、フィルム品質が低下する。一方、 8重量%より 多いと、無機粒子の分散が低下し、フィッシュアイ等のフィルムの外観不良を引き起こ す。マスターバッチ中の無機粒子の配合量は、更に好ましくは 2. 5〜7. 5重量%、 特に好ましくは 3〜7重量%である。  [0029] The blending amount of the inorganic particles in the master batch (B) of the present invention is 2 to 8% by weight. If the amount of inorganic particles is less than 2% by weight, a large amount of masterbatch is used, resulting in poor thermal stability during film production and a reduction in film quality. On the other hand, when the content is more than 8% by weight, the dispersion of the inorganic particles is lowered and the appearance of the film such as fish eye is deteriorated. The blending amount of the inorganic particles in the master batch is more preferably 2.5 to 7.5% by weight, particularly preferably 3 to 7% by weight.
[0030] 本発明材料にぉ ヽて、滑り性および透明性を改良する目的で配合されるビスアミド 化合物としては、下記一般式〔I〕又は〔II〕で表される化合物が用いられる。  [0030] As the bisamide compound to be blended for the purpose of improving slipperiness and transparency over the material of the present invention, a compound represented by the following general formula [I] or [II] is used.
[0031] [化 1]  [0031] [Chemical 1]
Figure imgf000008_0001
Figure imgf000008_0001
[0032] 式中、 R1は 2価の炭化水素残基、 R2及び R3は 1価の炭化水素残基、 R4及び R5は 水素原子、または 1価の炭化水素残基を示す。 In the formula, R 1 represents a divalent hydrocarbon residue, R 2 and R 3 represent a monovalent hydrocarbon residue, R 4 and R 5 represent a hydrogen atom, or a monovalent hydrocarbon residue. .
[0033] 前記一般式 [I]のビスアミドィ匕合物としては、例えば、ジァミンとモノカルボン酸の反 応により得られるアルキレンビス脂肪酸アミド、ァリーレンビス脂肪酸アミドが挙げられ る。当該ジァミンとしては、例えばエチレンジァミン、プロピレンジァミン、ブチレンジァ ミン、へキサメチレンジァミン、オタタメチレンジァミン、ドデカメチレンジァミン等のァ ルキレンジァミン、フエ二レンジァミン、ナフタレンジァミン等のァリーレンジァミン、キ シリレンジァミン等のァリーレンアルキルジァミン等が挙げられる。またモノカルボン酸 としては、ステアリン酸、へキサン酸、オクタン酸、デカン酸、ラウリン酸、ミリスチン酸、 パルミチン酸、ァラキジン酸、ベへニン酸、ォレイン酸、エライジン酸、モンタン酸等の 脂肪酸などが挙げられる。これらの中で代表的なものとして、 N, N'—メチレンビスス テアリン酸アミド及び N, N'—エチレンビスステアリン酸アミドを挙げることが出来る。 [0033] Examples of the bisamido compound of the general formula [I] include alkylene bis fatty acid amides and arylene bis fatty acid amides obtained by reaction of diamine and monocarboxylic acid. Examples of the diamine include ethylene diamine, propylene diamine, butylene diamine, hexamethylene diamine, otatamethylene diamine, dodecamethylene diamine etc. And arylene alkyldiamines such as arylenediamine and xylylenediamine. Monocarboxylic acids include fatty acids such as stearic acid, hexanoic acid, octanoic acid, decanoic acid, lauric acid, myristic acid, palmitic acid, arachidic acid, behenic acid, oleic acid, elaidic acid, and montanic acid. Can be mentioned. Among these, N, N'-methylenebis Mention may be made of the tea amide and N, N'-ethylenebisstearic amide.
[0034] 前記一般式 [Π]で表されるビスアミドィ匕合物は、モノアミンとジカルボン酸の反応で 得られる。モノアミンとしては、例えば、ェチルァミン、メチルァミン、ブチルァミン、へ キシルァミン、デシルァミン、ペンタデシルァミン、ォクタデシルァミン、ドデシルァミン 等のアルキルァミン、ァ-リン、ナフチルァミン等のァリールァミン、ベンジルァミン等 のァラルキルァミン、シクロへキシルァミン等のシクロアルキルアミン等が挙げられ、ジ カルボン酸としてはテレフタル酸、 p—フエ-レンジプロピオン酸、コハク酸、アジピン 酸等が挙げられる。これらの中で代表的なものとして、 N, N'—ジォクタデシルテレフ タル酸アミド等のジォクタデシルニ塩基酸アミドを挙げることが出来る。  [0034] The bisamido compound represented by the general formula [Π] is obtained by the reaction of a monoamine and a dicarboxylic acid. Examples of the monoamine include alkylamines such as ethylamine, methylamine, butylamine, hexylamine, decylamine, pentadecylamine, octadecylamine, dodecylamine, aralkylamines such as a-line and naphthylamine, aralkylamines such as benzylamine, and cyclohexylamine. Examples of the dicarboxylic acid include terephthalic acid, p-phenylene dipropionic acid, succinic acid, and adipic acid. Among these, representative examples include dioctadecyl dibasic acid amides such as N, N′-dioctadecyl terephthalic acid amide.
[0035] これらのビスアミドィ匕合物は一種を用いても良いし、二種以上を組み合わせて用い てもよい。本発明において、上記ビスアミドィ匕合物は、(B)成分のマスターノツチ中と 、(C)成分のビスアミドィ匕合物粉体とに分割して配合されることを特徴とする。上記ビ スアミド化合物の(B)成分 (マスターバッチ)中の配合量としては、 1〜5重量0 /0、 (C) 成分 (粉体)としての配合量は、(A)成分および (B)成分の合計 100重量部に対して 0. 005〜0. 1重量部であり、本発明のポリアミド榭脂成形材料全体での配合量とし ては、全ポリアミド榭脂に対し、好ましくは 0. 015〜0. 6重量%、より好ましくは 0. 02 〜0. 5重量%の範囲である。配合量が少ないと、滑り性改良の効果が観られず、多 すぎるとフィルムの印刷性やラミネート加工時の密着性が低下するので好ましくない。 [0035] One of these bisamido compounds may be used, or two or more may be used in combination. In the present invention, the bisamidite compound is characterized by being divided and mixed in the master notch of the component (B) and the bisamidyl compound powder of the component (C). (B) component of the bi Suamido compound as the amount in (master batch), 1 to 5 wt 0/0, the amount of component (C) (powder) is, (A) component and (B) It is 0.005 to 0.1 part by weight with respect to 100 parts by weight of the total of the components, and the blending amount of the entire polyamide resin molding material of the present invention is preferably 0.005 with respect to the total polyamide resin. It is in the range of ~ 0.6% by weight, more preferably 0.02 to 0.5% by weight. If the blending amount is small, the effect of improving the slipperiness is not observed, and if it is too large, the printability of the film and the adhesiveness at the time of laminating process are lowered, which is not preferable.
[0036] 本発明材料にお!、て、ビスアミドィ匕合物は、フィルムの透明性、滑り性の改良を主 目的として配合されるが、(B)成分中のビスアミドは、無機粒子の分散性改良の目的 も併せ持ち、(C)成分としてのビスアミド粉体は押出機への喰い込み安定性効果の ために必須である。従って、(B)成分中においては、無機粒子 Zビスアミド化合物の 配合比率 (重量比)は、 1〜5の範囲が好ましい。配合比率が 1より小さぐ同時にビス アミド化合物の配合量が 5重量%以上となる様な配合では、マスターバッチの製造時 に安定した溶融混練が難しぐ無機粒子の分散性も低下する。配合比率が 5より大き い場合は、無機粒子の分散が難しぐ得られるフィルムに外観不良が発生しやすい。  [0036] In the material of the present invention, the bisamide compound is blended mainly for the purpose of improving the transparency and slipperiness of the film, but the bisamide in the component (B) is the dispersibility of the inorganic particles. In addition to the purpose of improvement, the bisamide powder as component (C) is essential for the stability of biting into the extruder. Therefore, in the component (B), the blending ratio (weight ratio) of the inorganic particle Z bisamide compound is preferably in the range of 1 to 5. When the blending ratio is less than 1 and the blending amount of the bisamide compound is 5% by weight or more, the dispersibility of the inorganic particles, which is difficult to stably melt and knead during the production of the masterbatch, is also lowered. If the blending ratio is larger than 5, the resulting film is difficult to disperse, and poor appearance tends to occur.
[0037] 本発明の(B)成分であるマスターバッチの製造法は特に限定されるものではなぐ 公知の方法により製造され、好ましくはペレット状である。例えば、所定量のポリアミド 榭脂、無機粒子、ビスアミド化合物をドライブレンド後、押出機により溶融、混練し、定 法によりペレツトイ匕することによりマスターバッチペレットが得られる。その際、ポリアミド 榭脂ペレット表面に無機粒子を均一に付着させ、分散を容易にするため、水や液状 界面活性剤でポリアミド榭脂表面を濡らした後、ドライブレンド、溶融混練を行うことも 好ましい。また、マスターバッチペレットの形状や大きさは、ポリアミド榭脂ペレット (A) と同等もしくは類似しているの力 マスターバッチとポリアミドペレットとの分離の防止 の観点力も好ましい。 [0037] The production method of the masterbatch that is the component (B) of the present invention is not particularly limited, and is produced by a known method, preferably in the form of pellets. For example, a certain amount of polyamide Master blend pellets can be obtained by dry blending the resin, inorganic particles and bisamide compound, then melting and kneading with an extruder, and pelletizing with a conventional method. At that time, in order to make the inorganic particles uniformly adhere to the surface of the polyamide resin pellet and facilitate dispersion, it is also preferable to wet the polyamide resin surface with water or a liquid surfactant, and then perform dry blending and melt-kneading. . Further, the shape and size of the masterbatch pellets are the same as or similar to those of the polyamide resin pellets (A). From the viewpoint of preventing separation of the masterbatch and the polyamide pellets.
[0038] 本発明の成形材料は、ポリアミド榭脂、無機粒子及びビスアミド化合物の 3成分を必 須成分とする。従来、この様に 3成分から成る組成物の製造は、通常、 3成分を一括 ドライブレンドする方法、または無機粒子をポリアミドの重合時に内添し、これにビスァ ミドィ匕合物をドライブレンドする配合方法により製造されてきた。しかして、本発明では 、この 3成分を次のように配合することにより、得られるフィルムの外観不良の発生が 抑制でき、同時に優れた透明性、滑り性、印刷性を得られる。  [0038] The molding material of the present invention comprises the three components of polyamide resin, inorganic particles and bisamide compound as essential components. Conventionally, the production of such a three-component composition is usually performed by dry blending the three components together or by adding inorganic particles internally during the polymerization of the polyamide and dry blending the biamide compound. Has been manufactured by a method. Therefore, in the present invention, by blending these three components as follows, it is possible to suppress the appearance failure of the resulting film, and at the same time, excellent transparency, slipperiness and printability can be obtained.
[0039] 即ち、無機粒子 2〜8重量%およびビスアミドィ匕合物 1〜5重量%をポリアミドに配合 したマスターバッチ (B)を作成し、そのマスターバッチ (B)とビスアミド化合物粉体 (C )及びポリアミド榭脂ペレット (A)との 3種類を用いて配合する。マスターバッチ(B)の 配合量は、ポリアミド榭脂ペレット (A)との合計量のうち、 1〜10重量0 /0、好ましくは 2 〜8重量%である。 1重量%より少ない場合は、無機粒子等がフィルム中で不均一に 分散するため、透明性にむらが発生する。 10重量%より多いとフィルム製造時に熱 安定性が悪化し、フィルム外観不良が発生しやすくなる。またビスアミド化合物粉体( C)の配合量は、(A)および(B)成分の合計量 100重量部当り 0. 005-0. 1重量部 、好ましくは 0. 01〜0. 08重量咅である。 0. 005重量咅より少な!/ヽと、フイノレム製造 時の押出機への安定した喰い込み性が保証されないし、 0. 1重量部より多いと、や はり押出機への安定した喰い込みに障害が発生する。 [0039] That is, a masterbatch (B) was prepared by blending 2 to 8% by weight of inorganic particles and 1 to 5% by weight of a bisamide compound in polyamide, and the masterbatch (B) and bisamide compound powder (C) were prepared. And 3 types of polyamide rosin pellets (A). The amount of masterbatch (B), of the total amount of the polyamide榭脂pellets (A), 1 to 10 weight 0/0, preferably 2 to 8 wt%. When the content is less than 1% by weight, the inorganic particles are dispersed unevenly in the film, resulting in uneven transparency. If it is more than 10% by weight, the thermal stability deteriorates during film production, and poor film appearance tends to occur. The blending amount of the bisamide compound powder (C) is 0.005 to 0.1 parts by weight, preferably 0.01 to 0.08 parts by weight per 100 parts by weight of the total amount of the components (A) and (B). is there. Less than 005 wt.%! / ヽ and stable bite into the extruder during the manufacture of FINOLEM is not guaranteed, and if more than 0.1 wt.%, Stable bite into the beam extruder A failure occurs.
[0040] ポリアミド榭脂ペレット (A)とマスターノツチ (B)に使用されるポリアミドは、同じでも 異なっていてもよい。異なっている場合はマスターバッチ(B)中のポリアミドの融点ま たは溶融粘度は、ポリアミド榭脂ペレット (A)のそれらより低いのが好ましい。また、マ スターバッチ(B)中のビスアミド化合物とビスアミド化合物粉体 (C)中のビスアミドィ匕 合物も、同じであっても異なっていてもよい。 [0040] The polyamide used in the polyamide resin pellet (A) and the master notch (B) may be the same or different. If they are different, the melting point or melt viscosity of the polyamide in the masterbatch (B) is preferably lower than those of the polyamide resin pellet (A). In addition, the bisamide compound in the master batch (B) and the bisamide compound in the bisamide compound powder (C) The compound may be the same or different.
[0041] 本発明に係わる材料の製造は、(A)、(B)、(C)成分を混合することにより行われる [0041] The material according to the present invention is manufactured by mixing the components (A), (B), and (C).
。混合はフィルム製造前のいずれの時点でも通常の方法により可能であり、例えば(. Mixing is possible at any point before film production by conventional methods, for example (
A)、(B)および (C)をドライブレンドし、フィルム製造用の押出機のホッパーに供給す る方法、またフィルム製造押出機のホッパーに (A)、(B)および (C)を別々に定量フ ィーダ一で供給する方法等が好ましく採用できる。 A), (B) and (C) are dry blended and supplied to the hopper of an extruder for film production, and (A), (B) and (C) are separately supplied to the hopper of a film production extruder. For example, a method using a fixed amount feeder can be preferably used.
[0042] また、本発明材料は必須成分である上記 (A)、 (B)、 (C)成分の他に、本発明の効 果を損なわない範囲で添加剤を含有することが出来る。例えば、外観欠陥発生防止 効果の更なる向上のために、 3〜6価の脂肪族アルコールと炭素数 10〜22の脂肪 酸との部分エステルイ匕合物および Zまたはヒドロキシ脂肪酸のマグネシウム金属塩を 含有させてもょ 、。 3〜6価の脂肪族アルコールと炭素数 10〜22の脂肪酸との部分 エステルイ匕合物の脂肪族アルコールとしては、例えば、グリセリン、トリメチルプロパン 、ペンタエリスリトール、メソエリスリトール、ソルビトール等が挙げられる。また、炭素数[0042] In addition to the components (A), (B), and (C), which are essential components, the material of the present invention can contain additives within a range that does not impair the effects of the present invention. For example, in order to further improve the appearance defect prevention effect, it contains a partial ester compound of tri- to hexavalent aliphatic alcohol and C10-22 fatty acid and magnesium metal salt of Z or hydroxy fatty acid Let me do it. Examples of the aliphatic alcohol of a partial ester compound of a tri- to hexavalent aliphatic alcohol and a fatty acid having 10 to 22 carbon atoms include glycerin, trimethylpropane, pentaerythritol, mesoerythritol, and sorbitol. Carbon number
10〜22の脂肪酸としては、例えば、ラウリン酸、ミリスチン酸、パルミチル酸、ステアリ ン酸、ベヘン酸等が挙げられる。脂肪酸の炭素骨格には、水酸基等の置換基が存在 していてもよい。こうした脂肪族アルコール類と脂肪酸とのエステルイ匕合物は、実質 的に部分エステルであることが必要であり、好ましくは、多価アルコール中の水酸基 全体の 30%以上がエステルイ匕せず、残存しているものが用いられる。中でも、グリセ リンモノステアレート、グリセリンジステアレート、グリセリンモノべへネート、グリセリンジ ステアレート、ペンタエリスリトールモノステアレート、ペンタエリスリトールジステアレー ト、ペンタエリスリトールモノべへネート、ペンタエリスリトールジベへネート等の使用が 好ましい。こうした部分エステルイ匕合物は、単独もしくは複数の化合物を併用して使 用することが出来る。 Examples of the fatty acids 10 to 22 include lauric acid, myristic acid, palmitic acid, stearic acid, behenic acid and the like. A substituent such as a hydroxyl group may be present in the carbon skeleton of the fatty acid. Such an ester compound of an aliphatic alcohol and a fatty acid needs to be substantially a partial ester, and preferably 30% or more of the total hydroxyl groups in the polyhydric alcohol are not esterified and remain. Is used. Among them, glycerin monostearate, glycerin distearate, glycerin monobehenate, glycerin distearate, pentaerythritol monostearate, pentaerythritol distearate, pentaerythritol monobehenate, pentaerythritol dibehenate, etc. Is preferred. Such partial ester compounds can be used alone or in combination of a plurality of compounds.
[0043] また、ヒドロキシ脂肪酸のマグネシウム金属塩は、炭素数 12〜30のヒドロキシカル ボン酸とマグネシウムの塩であり、例えば、ヒドロキシカルボン酸とマグネシウム酸化 物もしくは水酸ィ匕物と加熱直接反応によって得ることが出来る。この際、マグネシウム 酸化物もしくは水酸化物を過剰に加えて、塩基性の高いヒドロキシ脂肪酸マグネシゥ ム塩を合成すると、より良好な結果が得られる。具体的には、ラウリン酸、ミリスチン酸 、パルミチン酸、ステアリン酸、ベヘン酸などの脂肪族カルボン酸をヒドロキシ化した 化合物のマグネシウム塩である。脂肪酸の炭素数が小さ!/、と所定の効果が得られず 、炭素数が大き過ぎると得られるフィルムの透明性の低下が生じるため好ましくない。 このため、炭素数は通常 12〜30、好ましくは 12〜24の範囲で選ばれる。脂肪族ァ ルコールと脂肪酸との部分エステルイ匕合物およびヒドロキシ脂肪酸のマグネシウム塩 の配合量は、ポリアミド榭脂 100重量部に対し、通常 0. 01-0. 7重量部、好ましくは 0. 03〜0. 4重量部である。配合量が少ないと、得られるフィルムの外観改良効果が 不十分であり、配合量が多すぎると、印刷特性が悪化する。 [0043] Further, the magnesium metal salt of hydroxy fatty acid is a salt of hydroxycarbonic acid having 12 to 30 carbon atoms and magnesium, for example, by direct reaction with hydroxycarboxylic acid and magnesium oxide or hydroxide. Can be obtained. In this case, a better result can be obtained by adding magnesium oxide or hydroxide in excess to synthesize a highly basic hydroxy fatty acid magnesium salt. Specifically, lauric acid, myristic acid , A magnesium salt of a compound obtained by hydroxylating an aliphatic carboxylic acid such as palmitic acid, stearic acid or behenic acid. If the fatty acid has a small number of carbon atoms, a predetermined effect cannot be obtained. If the number of carbon atoms is too large, the transparency of the resulting film is lowered, which is not preferable. For this reason, carbon number is normally selected in the range of 12-30, Preferably 12-24. The blending amount of the partial ester compound of aliphatic alcohol and fatty acid and the magnesium salt of hydroxy fatty acid is usually from 0.01 to 0.7 parts by weight, preferably from 0.03 to 0.7 parts per 100 parts by weight of the polyamide resin. 0. 4 parts by weight. If the blending amount is small, the effect of improving the appearance of the resulting film is insufficient, and if the blending amount is too large, the printing characteristics deteriorate.
[0044] 多価アルコールの部分エステルおよびヒドロキシ脂肪酸のマグネシウム金属塩の配 合は、ポリアミド榭脂のペレット状原料にドライブレンドするいわゆる外添法でも、溶融 混合する練込法でも、あるいは、高濃度に含有する原料を配合するいわゆるマスタ 一バッチ法でも、重合時に添加する内添法でも、いずれの方法も可能である。特にマ スターバッチ(B)に同時に添加、溶融混練するのが好ましい。  [0044] The combination of the partial ester of the polyhydric alcohol and the magnesium metal salt of the hydroxy fatty acid may be a so-called external addition method in which dry blending is performed on the pelletized raw material of polyamide resin, a kneading method in which melt mixing is performed, or a high concentration Either a so-called master one-batch method in which the raw materials contained in the compound are blended or an internal addition method to be added during polymerization can be used. In particular, it is preferable to simultaneously add to the master batch (B) and melt knead.
[0045] 更に、上記の配合物以外に当該業者に周知の各種の添加剤、例えば、ヒンダード フエノール、リン酸エステルや亜リン酸エステル等の酸ィ匕防止剤、トリアジン系化合物 等の耐候性改良剤、顔料、染料等の着色剤、帯電防止剤、滑剤、界面活性剤などを 含有してちょい。  [0045] In addition to the above-mentioned blends, various additives well known to those skilled in the art, for example, hindered phenol, anti-oxidation agents such as phosphate ester and phosphite ester, and weather resistance improvement of triazine compounds, etc. Contains colorants such as colorants, pigments and dyes, antistatic agents, lubricants, and surfactants.
[0046] 本発明の成形材料を用いてポリアミド榭脂フィルムを製造するには、(A) , (B)及び  In order to produce a polyamide resin film using the molding material of the present invention, (A), (B) and
(C)成分の所定量、及び要すれば他の添加物とを、予めドライブレンドし、或いは予 めブレンドすることなぐフィルム製造用成形機に供給し、定法に従って、製膜すれば よい。本発明の成形材料が適用されるフィルム製膜法としては、公知のフィルム製膜 法が何れも適用可能である力 好ましくは、 Tダイ法、インフレーション法などである。 本発明のポリアミドフィルムは、未延伸フィルムのまま、もしくは一軸延伸、二軸延伸 などの延伸工程を経て延伸フィルムとして使用される。また、本発明の成形材料を使 用したフィルムは、単層ポリアミドフィルムであってもよいし、共押出やラミネート等によ る他の樹脂との積層フィルムであってもよ 、。  The predetermined amount of component (C) and, if necessary, other additives may be dry blended in advance, or supplied to a molding machine for film production without preblending, and film formation may be performed according to a conventional method. The film forming method to which the molding material of the present invention is applied is a force to which any of the known film forming methods can be applied, preferably the T-die method, the inflation method and the like. The polyamide film of the present invention is used as an unstretched film or as a stretched film through a stretching process such as uniaxial stretching or biaxial stretching. The film using the molding material of the present invention may be a single-layer polyamide film or a laminated film with other resin by coextrusion or lamination.
[0047] 本発明のポリアミド榭脂フィルムの厚みは、特に規定されるものではないが、厚けれ ばガスノ リア一性が向上する一方、透明性が低下し、薄すぎるとポリアミド榭脂が本 来持っている強度が低下する。この点を鑑みれば、ポリアミド榭脂単層としての厚み は、未延伸フィルムでは通常 2〜 100 μ m、延伸フィルムでは通常 2〜50 μ mである ことが好ましぐ積層フィルム全体としての厚みは通常 10〜300 m程度であり、その うちのポリアミド榭脂層としての厚みは、前記単層としての厚みと同様の範囲が良い。 実施例 [0047] The thickness of the polyamide resin film of the present invention is not particularly limited, but if it is thick, the gas-noirality is improved, but the transparency is lowered. The strength you have is reduced. In view of this point, the thickness of the polyamide resin monolayer is usually 2 to 100 μm for an unstretched film and usually 2 to 50 μm for a stretched film. The thickness is usually about 10 to 300 m, and the thickness of the polyamide resin layer is preferably in the same range as the thickness of the single layer. Example
[0048] 以下、本発明を実施例及び比較例によって更に具体的に説明するが、本発明はそ の要旨を超えない限り、以下の例に限定されるものではない。なお、実施例および比 較例で使用した添加剤成分、表面処理無機粒子の製造法、得られたフィルムの評価 法は次の通りである。  [0048] Hereinafter, the present invention will be described more specifically with reference to Examples and Comparative Examples. However, the present invention is not limited to the following examples unless it exceeds the gist. The additive components used in the examples and comparative examples, the method for producing the surface-treated inorganic particles, and the method for evaluating the obtained film are as follows.
[0049] <添加剤成分 >  [0049] <Additive component>
(1)ポリアミド榭脂:ポリアミド— 6、三菱エンジニアリングプラスチックス社製「ノバミツ ド(登録商標) 1020J」、粘度数 182、ペレットサイズ:長さ 3mm、径 2. 5mmの円筒状  (1) Polyamide resin: Polyamide-6, “Novamid (registered trademark) 1020J” manufactured by Mitsubishi Engineering Plastics Co., Ltd., Viscosity number 182, Pellet size: Cylindrical shape with a length of 3mm and a diameter of 2.5mm
[0050] (2)無機粒子 1 :シリカ、富士シリシァ化学社製「サイリシァ 310」、平均粒径 2. 5 m、比表面積 300m2Zg、吸油量 310mlZlOOg。 [0050] (2) Inorganic particles 1: Silica, “Silysia 310” manufactured by Fuji Silysia Chemical Ltd., average particle size 2.5 m, specific surface area 300 m 2 Zg, oil absorption 310 ml ZlOOg.
[0051] (3)無機粒子 2 :ゼォライト、水沢化学社製「シルトン JC20」、平均粒径 2. : L m、吸 油量 50mlZlOOg。 [0051] (3) Inorganic particles 2: Zeolite, “Silton JC20” manufactured by Mizusawa Chemical Co., Ltd., average particle size 2 .: L m, oil absorption 50 ml ZlOOg.
[0052] (4)無機粒子 3 :焼成カオリン、エンゲルノヽードネ土製「サチントン No. 5」、平均粒径 0. 8 πι。  [0052] (4) Inorganic particles 3: calcined kaolin, “Satinton No. 5” manufactured by Engelnodne earth, average particle size of 0.8πι.
[0053] (5)シランカップリング剤: y—ァミノプロピルトリエトキシシラン、 日本ュ-カ社製「A 1100」。  [0053] (5) Silane coupling agent: y-aminopropyltriethoxysilane, “A 1100” manufactured by Nippon Kayaku Co., Ltd.
[0054] (6)ビスアミド化合物:エチレンビスステアリン酸アミド、花王社製「カオ一ワックス EB [0054] (6) Bisamide compound: ethylenebisstearic acid amide, "Kao Wax EB" manufactured by Kao Corporation
J o J o
[0055] <表面処理無機粒子の製造法 >  [0055] <Method for producing surface-treated inorganic particles>
無機粒子 (シリカまたはゼォライトまたは焼成カオリン)とシランカップリング剤を水で 6倍に希釈した水溶液をスーパーミキサー中で 80°Cに加熱しながら攪拌、混合し、 水を蒸発させた。次いで 120°Cで乾燥させ、表面処理した無機粒子を得た。  An aqueous solution in which inorganic particles (silica or zeolite or calcined kaolin) and a silane coupling agent were diluted 6-fold with water was stirred and mixed in a supermixer while heating to 80 ° C to evaporate the water. Subsequently, it was dried at 120 ° C. to obtain surface-treated inorganic particles.
[0056] <フィルムの評価方法 > (1)ヘーズ:東京電色社製ヘーズメーターを用いて、ヘーズ値を測定した。 [0056] <Film Evaluation Method> (1) Haze: The haze value was measured using a haze meter manufactured by Tokyo Denshoku.
[0057] (2)滑り性:相対湿度 65%および 90%、温度 23°Cの条件下、平行移動式で静止 摩擦係数 s)を測定した。滑り性の指標である静止摩擦係数が 1. 0を超えるという ことは、ひつカゝかった状態を示す。例えば、静止摩擦係数が 1. 0を超えるフィルムを 自動充填機などを用いて包材として使用するとき、フィルムが当該機械に引つかかつ てしまうという問題が起きる。従って、静止摩擦係数の最大許容値は、 1. 0である。 [0057] (2) Sliding property: The coefficient of static friction s) was measured by the parallel displacement method under the conditions of relative humidity of 65% and 90% and a temperature of 23 ° C. If the coefficient of static friction, which is an index of slipperiness, exceeds 1.0, it indicates a serious situation. For example, when a film having a static friction coefficient exceeding 1.0 is used as a packaging material using an automatic filling machine, the film may be attracted to the machine. Therefore, the maximum allowable value of the static friction coefficient is 1.0.
[0058] (3)製膜長時間連続成形性: Tダイ製膜機によって製膜開始後、 2時間、 4時間、 6 時間後に、フィルムの中央部を 300mm X 300mmの正方形に切取り、その部分のダ イライン発生の有無を肉眼で観察し、以下の基準で評価した。また同時に押出機へ の喰い込みの有無も観察し、安定性を〇△ Xの 3段階で評価した。 [0058] (3) Long-term continuous formability of film formation: After 2 hours, 4 hours, and 6 hours from the start of film formation by a T-die film forming machine, the central part of the film was cut into a 300 mm X 300 mm square, and the part The presence or absence of these lines was observed with the naked eye and evaluated according to the following criteria. At the same time, the presence or absence of biting into the extruder was also observed, and the stability was evaluated on a three-point scale.
[0059] [表 1] [0059] [Table 1]
〇:ダイラインが認められなかった。 ◯: Die line was not recognized.
△:ダイラインが部分的に認められた。  Δ: Die line was partially recognized.
X : フィルム全面にわたりダイラインが認められた。  X: Die lines were observed over the entire film.
[0060] (4)フィッシュアイの有無:製膜開始後 1時間目のフィルムを 2軸延伸した後、 300m m X 300mmの正方形に切取り、その部分のフィッシュアイの有無を肉眼観察によつ て個数を数えた。通常約 300 m以上のサイズのフィッシュアイを数えられる。 [0060] (4) Presence or absence of fish eyes: After biaxial stretching of the film 1 hour after the start of film formation, it was cut into a 300 mm x 300 mm square, and the presence or absence of fish eyes in the part was visually observed. Counted the number. Normally, fish eyes with a size of about 300 m or more can be counted.
[0061] 実施例 1 :  [0061] Example 1:
ポリアミド榭脂、表面処理した無機粒子 1 (シリカ)、ビスアミド化合物を、 92/5/3 ( 重量比)の配合率でドライブレンドし、 2軸押出機(日本製鋼所社製「TEX30」)を用 い、 250°Cにて溶融混練、ペレツトイ匕し、乾燥して無機粒子およびビスアミドィ匕合物を 配合したマスターバッチを得た。そのマスターバッチ 1. 5重量部とビスアミドィ匕合物粉 末 0. 05重量部をポリアミド榭脂 100重量部とドライブレンドし、フィルム用成形材料を 得た。  Polyamide resin, surface-treated inorganic particles 1 (silica), and bisamide compound are dry blended at a compounding ratio of 92/5/3 (weight ratio), and a twin screw extruder (“TEX30” manufactured by Nippon Steel) The mixture was melt-kneaded at 250 ° C, pelletized and dried to obtain a masterbatch containing inorganic particles and bisamido compound. 1.5 parts by weight of the master batch and 0.05 parts by weight of the bisamide compound powder were dry blended with 100 parts by weight of polyamide resin to obtain a molding material for film.
[0062] この成形材料を、先端に幅 600mmの Tダイを装着した直径 40mmの単軸押出機 力もなる Tダイ式製膜機のホッパーに供給し、榭脂温度 270°C、冷却ロール温度 30 °Cにて、厚み 135 mのフィルムを製膜した。押出機への食い込みは安定しており順 調に製膜ができた。その際、製膜開始後、 2時間、 4時間、 6時間後のフィルムを用い 、ダイラインと称される筋状の外観不良の有無を肉眼で観察し長時間連続製膜安定 性を評価した。また、製膜開始後 1時間目のフィルムを 120mm X 120mmの正方形 に切り取り、 TM— Long社製二軸延伸機にて 80°Cで 3 X 3倍の同時二軸延伸し、そ の後 200°Cの熱風オーブンにて 30秒熱固定を行い、厚み 15 μ mの 2軸延伸フィル ムを得た。その延伸フィルムのヘーズ値および静止摩擦係数を測定した。結果を表 2 に示した。 [0062] This molding material is supplied to a hopper of a T-die type film-forming machine that has a T-die having a diameter of 600 mm and a T-die having a diameter of 600 mm. A film having a thickness of 135 m was formed at ° C. The bite into the extruder was stable and the film was formed smoothly. At that time, use the film 2 hours, 4 hours, 6 hours after the start of film formation The stability of the film formation for a long time was evaluated by observing with the naked eye the presence or absence of streaky appearance defects called die lines. In addition, the film 1 hour after the start of film formation was cut into a 120 mm x 120 mm square and simultaneously biaxially stretched 3 x 3 times at 80 ° C with a TM-Long biaxial stretching machine, and then 200 The film was heat fixed in a hot air oven at ° C for 30 seconds to obtain a biaxially stretched film with a thickness of 15 μm. The haze value and static friction coefficient of the stretched film were measured. The results are shown in Table 2.
[0063] 比較例 1 : [0063] Comparative Example 1:
ポリアミド榭脂、表面処理した無機粒子 1 (シリカ)、ビスアミド化合物を、 99. 83/0 . 075/0. 095 (重量比)の配合率でドライブレンドしてフィルム用成形材料を得た。 この成形材料を用い、実施例 1と同様にしてフィルムを製膜し、評価した。結果を表 2 に示した。  Polyamide resin, surface-treated inorganic particles 1 (silica), and bisamide compound were dry blended at a blending ratio of 99.83 / 0.075 / 0.095 (weight ratio) to obtain a molding material for film. Using this molding material, a film was formed and evaluated in the same manner as in Example 1. The results are shown in Table 2.
[0064] 比較例 2 : [0064] Comparative Example 2:
表面処理した無機粒子 1 (シリカ)をポリアミド 6の重合中に、ポリアミド 6に対し 0. 07 5重量%となる量添加し、常法により重合し、粘度数 182のポリアミド 6榭脂を得た。こ のシリカ含有ポリアミド 6榭脂のペレット(長さ 3mm、径 2. 5mmの円筒状)にビスアミ ド化合物を 0. 095重量%となる量ドライブレンドしてフィルム用成形材料を得た。この 成形材料を用い、実施例 1と同様にフィルム製膜および評価を実施した。結果を表 2 に示した。  Surface-treated inorganic particles 1 (silica) was added in an amount of 0.05 to 5% by weight with respect to polyamide 6 during polymerization of polyamide 6, and polymerized by a conventional method to obtain polyamide 6 resin having a viscosity number of 182. . A film molding material was obtained by dry blending the silica-containing polyamide 6 rosin pellets (3 mm in length and 2.5 mm in diameter) into a bisamide compound in an amount of 0.095% by weight. Using this molding material, film formation and evaluation were carried out in the same manner as in Example 1. The results are shown in Table 2.
[0065] 比較例 3 : [0065] Comparative Example 3:
ポリアミド榭脂、表面処理した無機粒子 1 (シリカ)を、 95Z5 (重量比)の配合率でド ライブレンドし、実施例 1と同様に溶融混練して無機粒子を配合したマスターバッチを 得た。そのマスターバッチ 1. 5重量部とビスアミドィ匕合物粉末 0. 095重量部をポリア ミド榭脂 100重量部とドライブレンドしてフィルム用成形材料を得た。この成形材料を 用い、実施例 1と同様にフィルム製膜および評価を実施した。結果を表 2に示した。  Polyamide rosin and surface-treated inorganic particles 1 (silica) were dry blended at a blending ratio of 95Z5 (weight ratio), and melt-kneaded in the same manner as in Example 1 to obtain a master batch in which inorganic particles were blended. 1.5 parts by weight of the master batch and 0.095 parts by weight of the bisamide compound powder were dry blended with 100 parts by weight of polyamide resin to obtain a molding material for film. Using this molding material, film formation and evaluation were carried out in the same manner as in Example 1. The results are shown in Table 2.
[0066] 比較例 4 : [0066] Comparative Example 4:
ポリアミド、表面処理した無機粒子 1 (シリカ)、ビスアミド化合物を、 87Z10Z3(重 量比)の配合率でドライブレンドし、実施例 1と同様に溶融混練して無機粒子および ビスアミドィ匕合物を配合したマスターバッチを得た。そのマスターバッチ 0. 75重量部 とビスアミド化合物粉末 0. 0725重量部をポリアミド榭脂 100重量部とドライブレンドし てフィルム用成形材料を得た。この成形材料を用い、実施例 1と同様にフィルム製膜 および評価を実施した。結果を表 2に示した。 Polyamide, surface-treated inorganic particles 1 (silica), and a bisamide compound were dry blended at a blending ratio of 87Z10Z3 (weight ratio), and melt-kneaded in the same manner as in Example 1 to blend inorganic particles and a bisamide compound. A master batch was obtained. 0.775 parts by weight of the masterbatch Then, 0.0725 parts by weight of bisamide compound powder and 100 parts by weight of polyamide resin were dry blended to obtain a molding material for film. Using this molding material, film formation and evaluation were carried out in the same manner as in Example 1. The results are shown in Table 2.
[0067] 比較例 5 : [0067] Comparative Example 5:
ポリアミド榭脂、表面処理した無機粒子 1 (シリカ)、ビスアミド化合物を、 88. 67/5 /6. 33 (重量比)の配合率でドライブレンドし、実施例 1と同様に溶融混練して無機 粒子およびビスアミド化合物を配合したマスターバッチを得た。そのマスターバッチ 1 . 5重量部とポリアミド榭脂 100重量部とをドライブレンドした。次いでこのブレンドを用 い、実施例 1と同様にフィルム製膜および評価を実施した。結果を表 2に示した。  Polyamide rosin, surface-treated inorganic particles 1 (silica), and bisamide compound were dry blended at a blending ratio of 88.67 / 5 / 6.33 (weight ratio), and melt-kneaded in the same manner as in Example 1 to make inorganic A master batch containing the particles and the bisamide compound was obtained. 1.5 parts by weight of the master batch and 100 parts by weight of polyamide resin were dry blended. Next, using this blend, film formation and evaluation were carried out in the same manner as in Example 1. The results are shown in Table 2.
[0068] 実施例 2 : [0068] Example 2:
実施例 1で用いた無機粒子 1 (シリカ)を、表面処理した無機粒子 2 (ゼオライト)に変 更した以外は実施例 1と同様にしてフィルム用成形材料を得て、フィルムを製膜し、 評価を行った。結果を表 3に示した。  A film molding material was obtained in the same manner as in Example 1 except that the inorganic particles 1 (silica) used in Example 1 were changed to surface-treated inorganic particles 2 (zeolite), and a film was formed. Evaluation was performed. The results are shown in Table 3.
[0069] 比較例 6 : [0069] Comparative Example 6:
比較例 1で用いた無機粒子 1 (シリカ)を、表面処理した無機粒子 2 (ゼオライト)に変 更した以外は比較例 1と同様にして、フィルム用成形材料を得て、フィルムを製膜し、 評価を行った。結果を表 3に示した。  In the same manner as in Comparative Example 1, except that the inorganic particles 1 (silica) used in Comparative Example 1 were changed to surface-treated inorganic particles 2 (zeolite), a film molding material was obtained, and a film was formed. Evaluation was performed. The results are shown in Table 3.
[0070] 比較例 7 : [0070] Comparative Example 7:
比較例 2で用いた無機粒子 1 (シリカ)を、表面処理した無機粒子 2 (ゼオライト)に変 更した以外は比較例 2と同様にして、フィルム用成形材料を得て、フィルムを製膜し、 評価を行った。結果を表 3に示した。  In the same manner as in Comparative Example 2 except that the inorganic particles 1 (silica) used in Comparative Example 2 were changed to surface-treated inorganic particles 2 (zeolite), a film molding material was obtained, and a film was formed. Evaluation was performed. The results are shown in Table 3.
[0071] 比較例 8 : [0071] Comparative Example 8:
比較例 3で用いた無機粒子 1 (シリカ)を、表面処理した無機粒子 2 (ゼオライト)に変 更した以外は比較例 3と同様にしてフィルム用成形材料を得て、フィルムを製膜し、 評価を行った。結果を表 3に示した。  A molding material for a film was obtained in the same manner as in Comparative Example 3 except that the inorganic particles 1 (silica) used in Comparative Example 3 were changed to surface-treated inorganic particles 2 (zeolite), and a film was formed. Evaluation was performed. The results are shown in Table 3.
[0072] 実施例 3 : [0072] Example 3:
実施例 1の無機粒子 1 (シリカ)およびビスアミドィ匕合物を配合したマスターノツチを 0. 5重量部、実施例 2の無機粒子 2 (ゼォライト)およびビスアミドィ匕合物を配合したマ スターバッチを 1. 0重量部、及びビスアミド化合物粉末 0. 05重量部をポリアミド榭脂 100重量部とドライブレンドし、フィルム用成形材料を得た。この成形材料を用い、実 施例 1と同様にフィルム製膜および評価を実施した。結果を表 4に示した。 0.5 parts by weight of master notch containing inorganic particles 1 (silica) and bisamido compound of Example 1 and male particles containing inorganic particles 2 (zeolite) of Example 2 and bisamidi compound 1.0 part by weight of the star batch and 0.05 part by weight of the bisamide compound powder were dry blended with 100 parts by weight of polyamide resin to obtain a molding material for film. Using this molding material, film formation and evaluation were carried out in the same manner as in Example 1. The results are shown in Table 4.
[0073] 実施例 4 : [0073] Example 4:
実施例 1で用いた無機粒子 1 (シリカ)を、表面処理した無機粒子 3 (焼成カオリン) に変更した以外は、実施例 1と同様にしてフィルム用成形材料を得て、制膜および評 価を行った。結果を表 5に示した。  A film molding material was obtained in the same manner as in Example 1 except that the inorganic particles 1 (silica) used in Example 1 were changed to surface-treated inorganic particles 3 (calcined kaolin). Went. The results are shown in Table 5.
[0074] [表 2] [0074] [Table 2]
Figure imgf000017_0001
Figure imgf000017_0001
[0075] [表 3] 実施例 2 比較例 6 比較例 7 比較例 8 ポリアミド 92 ― 95 無機粒子 [0075] [Table 3] Example 2 Comparative Example 6 Comparative Example 7 Comparative Example 8 Polyamide 92-95 Inorganic particles
5 ― ― 5 (ゼォライト)  5 ― ― 5 (Zeolite)
ビスアミド 3 ― ―  Bisamide 3 ― ―
マスターバッチ Master Badge
1.5 - 1.5 1.5-1.5
(MB2)配合量 (MB2) Blending amount
ポリアミド 100 99.8 99.925 100 ビスアミド 0.05 0.095 0.095 0.095 無離立子 (ゼォライト) ― 0 A.075 0.075Polyamide 100 99.8 99.925 100 Bisamide 0.05 0.095 0.095 0.095 Zeolite ― 0 A.075 0.075
O C  O C
ポリアミド 101.38 101.3 σ8 101.38 101.38 最終 無機粒子  Polyamide 101.38 101.3 σ8 101.38 101.38 Final inorganic particles
0.075 0.076 0.076 0.075 組成 (ゼォライト)  0.075 0.076 0.076 0.075 Composition (Zeolite)
ビスアミド 0.095 0.097 0.096 0.095 へ一ズ 1.8 2.0 1.5 1.8 滑り性 (65%) 0.4 0.6 0.5 0.4 滑り性(90%) 0.8 2.0 1.4 0.8 フィッシュアィ個数 17 32 86 ダイライン (2時間後) 〇 〇 〇 〇 ダイライン (4時間後) 〇 Δ 〇 〇 ダイライン (6時間後) 〇 X Δ Δ 喰い込み安定性 〇 Δ 〇 〇 4] Bisamide 0.095 0.097 0.096 0.095 Hedge 1.8 2.0 1.5 1.8 Slip (65%) 0.4 0.6 0.5 0.4 Slip (90%) 0.8 2.0 1.4 0.8 Number of fishey 17 32 86 Die line (after 2 hours) 〇 〇 〇 Die line ( 4 hours later) ○ Δ ○ ○ Die line (after 6 hours) ○ X Δ Δ Biting stability ○ Δ ○ ○ 4]
Figure imgf000019_0001
5]
Figure imgf000020_0001
Figure imgf000019_0001
Five]
Figure imgf000020_0001
[0078] 表 2から明らかな様に、本発明のフィルム用成形材料を用いて成形された実施例 1 のフィルムは、同一添加剤組成の材料を用いて成形された比較例 1〜3のフィルムに 比較して、透明性、滑り性、フィッシュアイやダイラインの有無等のフィルム品質が優 れており、また、製膜の長期安定性も良好であった。 As apparent from Table 2, the film of Example 1 formed using the molding material for film of the present invention was the film of Comparative Examples 1 to 3 formed using a material having the same additive composition. Compared with the film quality, the film quality such as transparency, slipperiness, presence of fish eyes and die lines was excellent, and the long-term stability of the film formation was also good.
[0079] マスターバッチにおける、無機粒子およびビスアミドィ匕合物の配合量が、本発明の 範囲から外れる比較例 4、 5の材料カゝら成形されたフィルムは、フィッシュアイや長期 製膜の安定性に問題が発生する。このことからマスターバッチ中の無機粒子とビスァ ミドィ匕合物の比率が無機粒子の分散に影響しており、凝集による粗大粒子がフイツシ ュアイの発生や、ダイスの出口付近における榭脂の乱れた流れによるダイラインの発 生に影響すると推測される。 [0079] The film formed from the material of Comparative Examples 4 and 5 in which the blending amount of the inorganic particles and the bisamido compound in the master batch is out of the scope of the present invention is stable in fish eyes and long-term film formation. Problems occur. For this reason, the ratio of inorganic particles to bisamide compounds in the masterbatch affects the dispersion of inorganic particles, and coarse particles due to aggregation are It is presumed that this will affect the generation of die and the generation of die lines due to the turbulent flow of grease near the die outlet.
[0080] シリカの代わりにゼォライト、ゼォライトとシリカ、カオリンを用いた実施例 2〜4の材 料カゝら得られたフィルムも実施例 1と同様に品質が優れ、製膜の安定性も良好であつ た。  [0080] Films obtained from the materials of Examples 2 to 4 using zeolite, zeolite and silica, and kaolin instead of silica are excellent in quality and stable in film formation as in Example 1. It was.
[0081] 以上から、本発明の成形材料は、得られるフィルムの、透明性、滑り性に優れ、ダイ ライン等の外観不良の発生が抑えられ、長時間連続安定が可能であることが判明し た。また、滑り性が優れていることから印刷性にも優れていることは明ら力と考える。 産業上の利用可能性  [0081] From the above, it has been found that the molding material of the present invention is excellent in transparency and slipperiness of the obtained film, can prevent appearance defects such as die lines, and can be continuously stable for a long time. It was. In addition, since it is excellent in slipperiness, it is apparently excellent in printability. Industrial applicability
[0082] 本発明のポリアミド榭脂フィルム用成形材料は、長時間連続製膜安定性に優れ、ま た、得られるフィルムは透明性、滑り性および印刷性が良好で、ダイライン等の外観 不良が少な 、優れた特性を有して 、るので、食品包装等の広!、範囲にぉ 、て有用 である。 [0082] The molding material for polyamide resin film of the present invention is excellent in long-term continuous film-forming stability, and the resulting film has good transparency, slipperiness and printability, and has poor appearance such as die lines. Since it has few excellent characteristics, it is useful for a wide range of food packaging and the like.
[0083] 以上、現時点において、最も実践的であり、且つ、好ましいと思われる実施形態に 関連して本発明を説明したが、本発明は、本願明細書中に開示された実施形態に 限定されるものではなぐ請求の範囲および明細書全体力 読みとれる発明の要旨 或いは思想に反しない範囲で適宜変更可能であり、その様な変更を伴う場合も本発 明の技術的範囲であると理解されなければならない。なお、本出願は、 2004年 10月 6日付で出願された日本特許出願 (特願 2004— 293153号)に基づいており、その 全体が引用により援用される。  [0083] While the present invention has been described in connection with the most practical and preferred embodiments at present, the present invention is not limited to the embodiments disclosed herein. However, it is understood that the scope of the present invention can be changed as appropriate without departing from the gist or philosophy of the invention that can be read, and that such changes are also within the technical scope of the present invention. There must be. This application is based on a Japanese patent application (Japanese Patent Application No. 2004-293153) filed on October 6, 2004, which is incorporated by reference in its entirety.

Claims

請求の範囲 The scope of the claims
[1] (A)と (B)の合計を 100重量部として、(A)ポリアミド榭脂ペレット 90〜99重量部と 、 (B)ポリアミド榭脂に無機粒子 2〜8重量%及びビスアミド化合物 1〜5重量%を配 合したマスターバッチ 10〜1重量部と、(C)ビスアミド化合物粉体 0. 005-0. 1重量 部とを混合して成るフィルム用ポリアミド榭脂成形材料。  [1] The total of (A) and (B) is 100 parts by weight, (A) 90 to 99 parts by weight of polyamide resin pellets, and (B) 2 to 8% by weight of inorganic particles in polyamide resin and bisamide compound 1 A polyamide resin composition for film, comprising 10 to 1 part by weight of master batch mixed with ˜5% by weight and 0.005 to 0.1 part by weight of (C) bisamide compound powder.
[2] 無機粒子がシリカ、ゼォライト及びカオリンカも選択される少なくとも 1種である請求 項 1に記載のフィルム用ポリアミド榭脂成形材料。  [2] The polyamide resin composition for film according to claim 1, wherein the inorganic particles are at least one selected from silica, zeolite and kaolinka.
[3] 無機粒子がシランカップリング剤で表面処理されたものである請求項 1又は 2に記 載のフィルム用ポリアミド榭脂成形材料。  [3] The polyamide resin molding material for film according to claim 1 or 2, wherein the inorganic particles are surface-treated with a silane coupling agent.
[4] (A)と (B)の合計を 100重量部として、(A)ポリアミド榭脂ペレット 90〜99重量部と [4] When the total of (A) and (B) is 100 parts by weight, (A) 90 to 99 parts by weight of polyamide resin pellets
、 (B)ポリアミド榭脂に無機粒子 2〜8重量%及びビスアミド化合物 1〜5重量%を配 合したマスターバッチ 10〜1重量部と、(C)ビスアミド化合物粉体 0. 005-0. 1重量 部とをフィルム製造用押出機に供給し、成膜することを特徴とするポリアミド榭脂フィ ルムの製造方法。 (B) 10 to 1 part by weight of a masterbatch in which 2 to 8% by weight of inorganic particles and 1 to 5% by weight of a bisamide compound are mixed with polyamide resin, and (C) bisamide compound powder 0.005-0. A method for producing a polyamide resin film, wherein a part by weight is supplied to an extruder for film production to form a film.
[5] (A)と (B)の合計を 100重量部として、(A)ポリアミド榭脂ペレット 90〜99重量部と [5] The total of (A) and (B) is 100 parts by weight.
、 (B)ポリアミド榭脂に無機粒子 2〜8重量%及びビスアミド化合物 1〜5重量%を配 合したマスターバッチ 10〜1重量部と、(C)ビスアミド化合物粉体 0. 005-0. 1重量 部とを予め均一混合した後に、フィルム製造用押出機に供給する請求項 4に記載の ポリアミド榭脂フィルムの製造方法。 (B) 10 to 1 part by weight of a masterbatch in which 2 to 8% by weight of inorganic particles and 1 to 5% by weight of a bisamide compound are mixed with polyamide resin, and (C) bisamide compound powder 0.005-0. The method for producing a polyamide resin film according to claim 4, wherein the weight parts are uniformly mixed in advance and then supplied to an extruder for film production.
[6] 請求項 1〜3の何れかに記載のポリアミド榭脂成形材料力も成形されたポリアミド榭 脂フィルム。  [6] A polyamide resin film in which the polyamide resin molding material strength according to any one of claims 1 to 3 is also molded.
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