Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/0008—Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
  • C08K5/005—Stabilisers against oxidation, heat, light, ozone
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
  • C08J5/18—Manufacture of films or sheets
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08C—TREATMENT OR CHEMICAL MODIFICATION OF RUBBERS
  • C08C19/00—Chemical modification of rubber
  • C08C19/28—Reaction with compounds containing carbon-to-carbon unsaturated bonds
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K3/00—Use of inorganic substances as compounding ingredients
  • C08K3/30—Sulfur-, selenium- or tellurium-containing compounds
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/36—Sulfur-, selenium-, or tellurium-containing compounds
  • C08K5/38—Thiocarbonic acids; Derivatives thereof, e.g. xanthates ; i.e. compounds containing -X-C(=X)- groups, X being oxygen or sulfur, at least one X being sulfur
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2309/00—Characterised by the use of homopolymers or copolymers of conjugated diene hydrocarbons
  • C08J2309/10—Latex
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K3/00—Use of inorganic substances as compounding ingredients
  • C08K3/01—Use of inorganic substances as compounding ingredients characterized by their specific function
  • C08K3/011—Crosslinking or vulcanising agents, e.g. accelerators
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K3/00—Use of inorganic substances as compounding ingredients
  • C08K3/02—Elements
  • C08K3/06—Sulfur
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/0008—Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
  • C08K5/0025—Crosslinking or vulcanising agents; including accelerators
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/04—Oxygen-containing compounds
  • C08K5/13—Phenols; Phenolates
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/16—Nitrogen-containing compounds
  • C08K5/34—Heterocyclic compounds having nitrogen in the ring
  • C08K5/3467—Heterocyclic compounds having nitrogen in the ring having more than two nitrogen atoms in the ring
  • C08K5/3477—Six-membered rings
  • C08K5/3492—Triazines
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/16—Nitrogen-containing compounds
  • C08K5/34—Heterocyclic compounds having nitrogen in the ring
  • C08K5/3467—Heterocyclic compounds having nitrogen in the ring having more than two nitrogen atoms in the ring
  • C08K5/3477—Six-membered rings
  • C08K5/3495—Six-membered rings condensed with carbocyclic rings

Definitions

• the present invention relates to a film molded body.
• a dip molding composition containing rubber latex may be dip molded to obtain a film molded body such as a dip molded body used in contact with a human body such as a nipple, a balloon, a glove, a balloon, or a sack.
• a film molded product such as a dip molded product is required to have excellent tensile strength from the viewpoint that it can be suitably used for these applications.
• Patent Document 1 describes a dip molding containing a synthetic polyisoprene latex, a sulfur-based vulcanizing agent, zinc oxide, a vulcanization accelerator, a specific dispersant, and a specific amount of a monovalent salt of dithiocarbamic acids.
• a dip-molded body obtained by dip-molding a composition is disclosed. According to the technique of Patent Document 1, a dip molded product having excellent tensile strength can be obtained.
• a film molded body is required.
• the present invention has been made in view of such an actual situation, and an object of the present invention is to provide a film-molded article in which a decrease in mechanical strength is suppressed when stored at a high temperature.
• the present inventor has made a latex containing a latex of a conjugated diene polymer, a cross-linking agent, a cross-linking accelerator, and an antiaging agent having a specific structure and molecular weight. It has been found that the film-molded body obtained by using the composition can suppress a decrease in mechanical strength when stored at a high temperature, and has completed the present invention.
• a latex composition containing a latex of a conjugated diene polymer, a sulfur-based vulcanizing agent, a vulcanization accelerator, and an antiaging agent can be used to obtain a thickness of 20 to 20 to.
• the body is provided.
• the anti-aging agent contains at least an aromatic compound (a) having two or more phenolic hydroxyl groups.
• the anti-aging agent contains at least an aromatic compound (a-1) having two or more hindered phenol structures.
• the anti-aging agent contains at least an aromatic compound (a-2) having a diphenylmethane skeleton having two or more hindered phenol structures.
• the antioxidant has an aromatic compound (a) having two or more phenolic hydroxyl groups, one phenolic hydroxyl group, and one or more -NH- bonds.
• the latex of the conjugated diene polymer is preferably a latex of synthetic polyisoprene, a latex of a styrene-isoprene-styrene block copolymer, or a latex of natural rubber.
• the latex of the conjugated diene-based polymer is preferably the latex of the carboxy-modified conjugated diene-based polymer.
• the swell index of the conjugated diene polymer is preferably 105 to 300% (SI).
• the content of the sulfur-based vulcanizing agent in the latex composition is 0.1 to 1.2 with respect to 100 parts by weight of the conjugated diene-based polymer in the latex composition. It is preferably a part by weight.
• the cross-linking accelerator is preferably a xanthate compound.
• the film-molded product of the present invention uses a latex composition containing a latex of a conjugated diene-based polymer, a sulfur-based vulcanizing agent, a vulcanization accelerator, and an antiaging agent having a specific structure and molecular weight. Can be obtained.
• the film molded body has excellent mechanical properties such as tensile strength and tear strength at room temperature, if the film thickness is as thin as 20 to 300 ⁇ m, the film molded body is used. It has been found that there is a problem that the mechanical strength when stored at a high temperature (for example, about 70 ° C.) is significantly reduced. Then, as a result of diligent research by the present inventors in order to suppress a decrease in mechanical strength of a film molded product having a thin film thickness of 20 to 300 ⁇ m when stored at a high temperature (for example, about 70 ° C.), it is conjugated.
• a high temperature for example, about 70 ° C.
• a film molded product obtained by using a latex composition containing a latex of a diene polymer, a cross-linking agent, a cross-linking accelerator, and an anti-aging agent having a specific structure and molecular weight can achieve the above object.
• a latex composition containing a latex of a diene polymer, a cross-linking agent, a cross-linking accelerator, and an anti-aging agent having a specific structure and molecular weight can achieve the above object.
• the latex composition used in the present invention contains a latex of a conjugated diene-based polymer.
• the conjugated diene polymer constituting the latex of the conjugated diene polymer is not particularly limited, and for example, synthetic polyisoprene, styrene-isoprene-styrene block copolymer (SIS), and natural rubber (natural product from which proteins have been removed). (Including rubber) and the like.
• synthetic polyisoprene, styrene-isoprene-styrene block copolymer (SIS) or natural rubber (including natural rubber from which protein has been removed) is preferable, and synthetic polyisoprene and styrene-isoprene-styrene block are preferable.
• SIS styrene-isoprene-styrene block copolymer
• SIS synthetic polyisoprene
• the synthetic polyisoprene may be a homopolymer of isoprene or may be a copolymer of isoprene and another ethylenically unsaturated monomer. It may be a polymer.
• the content of isoprene units in the synthetic polyisoprene is preferably 70% by weight or more, more preferably 90% by weight or more, still more preferably 95% by weight or more, and particularly preferably 100% by weight, based on all the monomer units. (Isoprene homopolymer).
• the content of the isoprene unit in the synthetic polyisoprene is in the above range, it is possible to further suppress the decrease in mechanical strength when the membrane molded product of the present invention is stored at a high temperature.
• ethylenically unsaturated monomers copolymerizable with isoprene include conjugated diene monomers other than isoprene such as butadiene, chloroprene, 1,3-pentadiene; acrylonitrile, methacrylonitrile, fumaronitrile, ⁇ -.
• Ethylene unsaturated nitrile monomer such as chloroacrylonitrile; vinyl aromatic monomer such as styrene and alkylstyrene; methyl (meth) acrylate (meaning "methyl acrylate and / or methyl methacrylate", and the following.
• Ethyl unsaturated carboxylic acid ester monomers such as (meth) ethyl acrylate, (meth) butyl acrylate, (meth) -2-ethylhexyl acrylate; etc. Can be mentioned.
• the other ethylenically unsaturated monomers copolymerizable with these isoprenes may be used alone or in combination of two or more.
• Synthetic polyisoprene is prepared in an inert polymerization solvent using a conventionally known method, for example, a Cheegler-based polymerization catalyst composed of trialkylaluminum-titanium tetrachloride or an alkyllithium polymerization catalyst such as n-butyllithium or sec-butyllithium.
• a Cheegler-based polymerization catalyst composed of trialkylaluminum-titanium tetrachloride or an alkyllithium polymerization catalyst such as n-butyllithium or sec-butyllithium.
• Isoprene and other copolymerizable ethylenically unsaturated monomers used as needed can be obtained by solution polymerization.
• the polymer solution of synthetic polyisoprene obtained by solution polymerization may be used as it is as a latex of synthetic polyisoprene, but after taking out solid synthetic polyisoprene from the polymer solution, it is dissolved in an organic solvent for synthesis. It may be a latex of polyisoprene. Further, when a polymer solution of synthetic polyisoprene is obtained by the above-mentioned method, impurities such as the residue of the polymerization catalyst remaining in the polymer solution may be removed. Further, an antiaging agent described later may be added to the solution during or after the polymerization. In addition, commercially available solid synthetic polyisoprene can also be used.
• the content ratio of the cis-bonding unit in the isoprene unit contained in the synthetic polyisoprene is preferably 70% by weight or more with respect to the total isoprene unit. It is more preferably 90% by weight or more, still more preferably 95% by weight or more.
• the weight average molecular weight of the synthetic polyisoprene is preferably 10,000 to 5,000,000, more preferably 500,000 to 5,000,000, still more preferably, in terms of standard polystyrene by gel permeation chromatography analysis. Is between 800,000 and 3,000,000.
• the weight average molecular weight of the synthetic polyisoprene is in the above range, it is possible to further suppress a decrease in mechanical strength when the membrane molded product of the present invention is stored at a high temperature, and it is easy to produce a synthetic polyisoprene latex. Tend to be.
• the polymer Mooney viscosity (ML1 + 4, 100 ° C.) of the synthetic polyisoprene is preferably 50 to 85, more preferably 60 to 85, and further preferably 70 to 85.
• a solution or a fine suspension of synthetic polyisoprene dissolved or finely dispersed in an organic solvent is emulsified in water in the presence of an anionic surfactant. Then, if necessary, a method for producing a synthetic polyisoprene latex by removing an organic solvent, (2) isoprene alone or a mixture of isoprene and an ethylenically unsaturated monomer copolymerizable therewith, anionic surface activity.
• a method of directly producing a synthetic polyisoprene latex by emulsification polymerization or suspension polymerization in the presence of an agent can be mentioned, but synthetic polyisoprene having a high ratio of cis-binding units in isoprene units can be used.
• the production method of (1) above is preferable because it is possible to further suppress a decrease in mechanical strength when the film-molded product of the present invention is stored at a high temperature.
• Examples of the organic solvent used in the above-mentioned production method (1) include aromatic hydrocarbon solvents such as benzene, toluene and xylene; alicyclic hydrocarbon solvents such as cyclopentane, cyclopentene, cyclohexane and cyclohexene; pentane, hexane and the like.
• An aliphatic hydrocarbon solvent such as heptane; a halogenated hydrocarbon solvent such as methylene chloride, chloroform and ethylene dichloride; and the like can be mentioned.
• an alicyclic hydrocarbon solvent is preferable, and cyclohexane is particularly preferable.
• the amount of the organic solvent used is preferably 2,000 parts by weight or less, more preferably 20 to 1,500 parts by weight, and further preferably 500 to 1500 parts by weight with respect to 100 parts by weight of the synthetic polyisoprene.
• anionic surfactant used in the above-mentioned production method (1) examples include fatty acid salts such as sodium laurate, potassium myristate, sodium palmitate, potassium oleate, sodium linolenate, and sodium dodecylbenzene.
• Alkylbenzene sulfonates such as sodium acid, sodium dodecylbenzene sulfonate, sodium decylbenzene sulfonate, potassium decylbenzene sulfonate, sodium cetylbenzenesulfonate, potassium cetylbenzenesulfonate; di (2-ethylhexyl) sodium sulfosuccinate, di.
• alkyl sulfosuccinates such as potassium sulfosuccinate and sodium dioctyl sulfosuccinate; alkyl sulfates such as sodium lauryl sulfate and potassium lauryl sulfate; sodium polyoxyethylene lauryl ether sulfate, potassium polyoxyethylene lauryl ether sulfate and the like.
• fatty acid salts, alkylbenzene sulfonates, alkylsulfosuccinates, alkylsulfate esters and polyoxyethylene alkylether sulfates are preferred, and fatty acid salts and alkylbenzenesulfonates are particularly preferred.
• a trace amount of the polymerization catalyst (particularly aluminum and titanium) derived from synthetic polyisoprene can be removed more efficiently, and the generation of aggregates in the production of the conjugated diene-based polymer latex composition is suppressed. Therefore, it is preferable to use at least one selected from the group consisting of an alkylbenzene sulfonate, an alkylsulfosuccinate, an alkylsulfate ester salt and a polyoxyethylene alkyl ether sulfate ester salt in combination with a fatty acid salt. It is particularly preferable to use the alkylbenzene sulfonate in combination with the fatty acid salt.
• fatty acid salt sodium loginate and potassium loginate are preferable, and as the alkylbenzene sulfonate, sodium dodecylbenzene sulfonate and potassium dodecylbenzene sulfonate are preferable.
• these surfactants may be used alone or in combination of two or more.
• At least one selected from the group consisting of alkylbenzene sulfonates, alkylsulfosuccinates, alkylsulfate esters and polyoxyethylene alkylether sulfates should be used in combination with fatty acid salts.
• the resulting latex contains at least one selected from an alkylbenzene sulfonate, an alkylsulfosuccinate, an alkylsulfate ester salt and a polyoxyethylene alkylether sulfate ester salt, and a fatty acid salt. ..
• a surfactant other than the anionic surfactant may be used in combination, and the surfactant other than the anionic surfactant may be ⁇ , ⁇ -non.
• examples thereof include copolymerizable surfactants such as sulfoesters of saturated carboxylic acids, sulfate esters of ⁇ , ⁇ -unsaturated carboxylic acids, and sulfoalkylaryl ethers.
• the amount of the anionic surfactant used in the production method (1) is preferably 0.1 to 50 parts by weight, more preferably 0.5 to 30 parts by weight, based on 100 parts by weight of the synthetic polyisoprene. be.
• the total amount of these surfactants used is in the above range. That is, for example, when at least one selected from an alkylbenzene sulfonate, an alkylsulfosuccinate, an alkylsulfate ester salt and a polyoxyethylene alkyl ether sulfate ester salt is used in combination with a fatty acid salt, these It is preferable that the total amount used is in the above range.
• fatty acid salt "alkylbenzene sulfonate, alkyl sulfosuccinate, alkyl sulfate ester salt and polyoxyethylene alkyl ether sulfate ester salt".
• the weight ratio of "total of agents” is preferably in the range of 1: 1 to 10: 1, more preferably in the range of 1: 1 to 7: 1.
• the amount of water used in the production method (1) is preferably 10 to 1,000 parts by weight, more preferably 30 to 500 parts by weight, and most preferably 30 parts by weight, based on 100 parts by weight of the organic solvent solution of synthetic polyisoprene. Is 50 to 100 parts by weight.
• Examples of the type of water used include hard water, soft water, ion-exchanged water, distilled water, zeolite water and the like, and soft water, ion-exchanged water and distilled water are preferable.
• a device for emulsifying a solution or microsuspension of synthetic polyisoprene dissolved or finely dispersed in an organic solvent in water in the presence of an anionic surfactant may be commercially available as an emulsifier or disperser. It can be used without particular limitation.
• the method of adding the anionic surfactant to the synthetic polyisoprene solution or the microsuspension is not particularly limited, and the method may be previously added to either water, the synthetic polyisoprene solution or the microsuspension, or both. It may be added, may be added to the emulsified solution during the emulsification operation, may be added all at once, or may be added in portions.
• emulsifying device examples include batch emulsification such as the product name "homogenizer” (manufactured by IKA), the product name “Polytron” (manufactured by Kinematica), and the product name “TK autohomo mixer” (manufactured by Special Machinery Co., Ltd.).
• Membrane emulsifier such as product name "Membrane emulsifier” (manufactured by Refrigeration Industry Co., Ltd.); Vibration type emulsifier such as product name “Vibro mixer” (manufactured by Refrigeration Industry Co., Ltd.); Product name “Ultrasonic homogenizer” (Branson) An ultrasonic emulsifier such as (manufactured by the company); etc.
• the conditions for the emulsification operation by the emulsification device are not particularly limited, and the treatment temperature, treatment time, and the like may be appropriately selected so as to obtain a desired dispersion state.
• the organic solvent from the emulsion obtained through the emulsification operation.
• a method for removing the organic solvent from the emulsion a method capable of reducing the content of the organic solvent (preferably alicyclic hydrocarbon solvent) in the obtained synthetic polyisoprene latex to 500% by weight ppm or less is preferable.
• methods such as vacuum distillation, atmospheric distillation, steam distillation, and centrifugation can be adopted.
• a concentration operation may be performed by a method such as vacuum distillation, atmospheric distillation, centrifugation, or membrane concentration.
• centrifugation it is preferable to perform centrifugation from the viewpoint that the solid content concentration of the synthetic polyisoprene latex can be increased and the residual amount of the surfactant in the synthetic polyisoprene latex can be reduced.
• Centrifugation uses, for example, a continuous centrifuge to centrifuge the centrifugal force, preferably 100 to 10,000 G, and the solid content concentration of the synthetic polyisoprene latex before centrifugation, preferably 2 to 15% by weight.
• the flow velocity to be fed into the machine is preferably 500 to 1700 kg / hr, and the back pressure (gauge pressure) of the centrifuge is preferably 0.03 to 1.6 MPa.
• a synthetic polyisoprene latex can be obtained.
• the residual amount of the surfactant in the synthetic polyisoprene latex can be reduced.
• the solid content concentration of the synthetic polyisoprene latex is preferably 30 to 70% by weight, more preferably 40 to 70% by weight. When the solid content concentration is in the above range, the latex viscosity becomes appropriate and it becomes easy to handle.
• the volume average particle size of the synthetic polyisoprene latex is preferably 0.1 to 10 ⁇ m, more preferably 0.5 to 3 ⁇ m, and even more preferably 0.5 to 2.0 ⁇ m.
• the volume average particle size is in the above range, the latex viscosity becomes appropriate and easy to handle, and it is possible to suppress the formation of a film on the latex surface when the synthetic polyisoprene latex is stored.
• the synthetic polyisoprene latex may be mixed with additives such as a pH adjuster, a defoaming agent, a preservative, a cross-linking agent, a chelating agent, an oxygen scavenger, and a dispersant, which are usually blended in the field of latex. good.
• a pH adjuster include hydroxides of alkali metals such as sodium hydroxide and potassium hydroxide; alkali metal carbonates such as sodium carbonate and potassium carbonate; alkali metal hydrogen carbonates such as sodium hydrogen carbonate; ammonia. ; Organic amine compounds such as trimethylamine and triethanolamine; and the like; but alkali metal hydroxides or ammonia are preferable.
• SIS styrene-isoprene-styrene block copolymer
• SIS can be obtained by block copolymerization of isoprene and styrene in an inert polymerization solvent using a conventionally known method, for example, an active organometallic such as n-butyllithium as an initiator.
• the obtained SIS polymer solution may be used as it is for the production of SIS latex, but after taking out the solid SIS from the polymer solution, the solid SIS is dissolved in an organic solvent to SIS. It can also be used in the production of latex.
• the method for producing SIS latex is not particularly limited, but a SIS solution or fine suspension dissolved or finely dispersed in an organic solvent is emulsified in water in the presence of a surfactant, and the organic solvent is removed if necessary.
• the method for producing the SIS latex is preferable. At this time, impurities such as the residue of the polymerization catalyst remaining in the polymer solution after the synthesis may be removed. Further, an antiaging agent described later may be added to the solution during or after the polymerization. Further, a commercially available solid SIS can also be used.
• organic solvent the same ones as in the case of the above synthetic polyisoprene can be used, aromatic hydrocarbon solvents and alicyclic hydrocarbon solvents are preferable, and cyclohexane and toluene are particularly preferable.
• the amount of the organic solvent used is usually 50 to 2,000 parts by weight, preferably 80 to 1,000 parts by weight, more preferably 100 to 500 parts by weight, still more preferably 150 to 300 parts by weight with respect to 100 parts by weight of SIS. It is a weight part.
• anionic surfactant is suitable, and sodium loginate and sodium dodecylbenzene sulfonate are particularly preferable.
• the amount of the surfactant used is preferably 0.1 to 50 parts by weight, more preferably 0.5 to 30 parts by weight, based on 100 parts by weight of SIS.
• the amount of water used in the above-mentioned method for producing SIS latex is preferably 10 to 1,000 parts by weight, more preferably 30 to 500 parts by weight, and most preferably 50 parts by weight with respect to 100 parts by weight of the organic solvent solution of SIS. ⁇ 100.
• Examples of the type of water used include hard water, soft water, ion-exchanged water, distilled water, and zeolite water. Further, a polar solvent typified by alcohol such as methanol may be used in combination with water.
• the same method as in the case of the above synthetic polyisoprene can be exemplified.
• an apparatus for emulsifying an organic solvent solution or a fine suspension of SIS in water in the presence of a surfactant can be exemplified as the same as in the case of the synthetic polyisoprene described above.
• the method of adding the surfactant is not particularly limited, and may be added in advance to either water, an organic solvent solution of SIS, a fine suspension, or both, and during the emulsification operation. In addition, it may be added to the emulsion, may be added all at once, or may be added separately.
• the organic solvent from the emulsion obtained through the emulsification operation it is preferable to remove the organic solvent from the emulsion obtained through the emulsification operation to obtain SIS latex.
• the method for removing the organic solvent from the emulsion is not particularly limited, and methods such as vacuum distillation, atmospheric distillation, steam distillation, and centrifugation can be adopted.
• a concentration operation may be performed by a method such as vacuum distillation, atmospheric distillation, centrifugation, or membrane concentration.
• the solid content concentration of the SIS latex is preferably 30 to 70% by weight, more preferably 50 to 70% by weight. When the solid content concentration is in the above range, the latex viscosity becomes appropriate and it becomes easy to handle.
• SIS latex contains additives such as pH adjusters, antifoaming agents, preservatives, cross-linking agents, chelating agents, oxygen scavengers, dispersants, and anti-aging agents, which are usually blended in the field of latex. May be.
• pH adjuster the same as in the case of the above synthetic polyisoprene can be exemplified, and an alkali metal hydroxide or ammonia is preferable.
• the content of the styrene unit in the styrene block in the SIS contained in the SIS latex thus obtained is preferably 70 to 100% by weight, more preferably 90 to 100% by weight, based on all the monomer units. , More preferably 100% by weight.
• the content of the isoprene unit in the isoprene block in SIS is preferably 70 to 100% by weight, more preferably 90 to 100% by weight, still more preferably 100% by weight, based on all the monomer units.
• the content ratio of the styrene unit and the isoprene unit in the SIS is a weight ratio of "styrene unit: isoprene unit", usually 1:99 to 90:10, preferably 3:97 to 70:30, more preferably 5. : 95 to 50:50, more preferably 10:90 to 30:70.
• the weight average molecular weight of SIS is preferably 10,000 to 1,000,000, more preferably 50,000 to 500,000, still more preferably 100,000 in terms of standard polystyrene by gel permeation chromatography analysis. ⁇ 300,000. When the weight average molecular weight of SIS is in the above range, the latex of SIS tends to be easily produced.
• the volume average particle diameter of the latex particles (SIS particles) in the SIS latex is preferably 0.1 to 10 ⁇ m, more preferably 0.5 to 3 ⁇ m, and even more preferably 0.5 to 2.0 ⁇ m.
• the volume average particle diameter of the latex particles is in the above range, the latex viscosity becomes appropriate and easy to handle, and it is possible to suppress the formation of a film on the latex surface when the SIS latex is stored.
• natural rubber can also be used.
• latex of natural rubber latex obtained from a natural rubber tree and latex treated with the latex can be used.
• field latex collected from a natural rubber tree or field latex is used with ammonia or the like.
• Commercially available natural rubber latex or the like which has been treated can be used.
• the conjugated diene-based polymer natural rubber from which proteins have been removed can also be used. Since the protein-removed natural rubber has the protein removed that causes the symptoms of immediate allergy (Type I), the obtained film-formed body is brought into contact with the human body such as a nipple, a balloon, a glove, a balloon, or a sack. It can be suitably used for the intended use.
• the method for obtaining the latex of natural rubber from which the protein has been removed is not particularly limited, but the protein contained in the natural rubber is modified by reacting the natural rubber latex with a urea compound in the presence of a surfactant.
• the natural rubber latex containing such a denatured protein is subjected to treatments such as centrifugation, coagulation of rubber content, and ultrafiltration to separate the natural rubber and the denatured protein, and this denatured protein is obtained. By removing it, a latex of natural rubber from which proteins have been removed can be obtained.
• conjugated diene-based polymer as described above, synthetic polyisoprene, styrene-isoprene-styrene block copolymer (SIS), natural rubber (including natural rubber from which protein has been removed) and the like can be used.
• SIS styrene-isoprene-styrene block copolymer
• natural rubber including natural rubber from which protein has been removed
• present invention is not limited to these, and a nitrile group-containing conjugated diene-based copolymer, a butadiene polymer, a styrene-butadiene copolymer, or the like may be used.
• the conjugated diene-based polymer is a carboxy-modified carboxy-modified conjugated diene-based polymer because it can further suppress a decrease in mechanical strength when the membrane molded product of the present invention is stored at a high temperature. Is preferable.
• the carboxy-modified conjugated diene-based polymer can be obtained by modifying the above-mentioned conjugated diene-based polymer with a monomer having a carboxyl group.
• the method for modifying the conjugated diene-based polymer with a monomer having a carboxyl group is not particularly limited, but for example, a monomer having a carboxyl group is graft-polymerized on the conjugated diene-based polymer in an aqueous phase.
• the method can be mentioned.
• the method for graft-polymerizing a monomer having a carboxyl group in the conjugated diene-based polymer in an aqueous phase is not particularly limited, and a conventionally known method may be used.
• a latex of a conjugated diene-based polymer may be used.
• a method of reacting the conjugated diene-based polymer with the monomer having a carboxyl group after adding the monomer having a carboxyl group and the organic peroxide is preferable.
• the organic peroxide is not particularly limited, and is, for example, diisopropylbenzene hydroperoxide, cumene hydroperoxide, t-butyl hydroperoxide, 1,1,3,3-tetramethylbutylhydroperoxide, di-t.
• -Butyl peroxide, isobutyryl peroxide, benzoyl peroxide and the like can be mentioned, but 1,1,3,3-tetramethylbutylhydroperoxide is particularly preferable from the viewpoint of improving the mechanical strength of the obtained film molded product. ..
• These organic peroxides may be used alone or in combination of two or more.
• the amount of the organic peroxide added is not particularly limited, but is preferably 0.01 to 3 parts by weight, more preferably 0, based on 100 parts by weight of the conjugated diene polymer contained in the latex of the conjugated diene polymer. .1-1 to 1 part by weight.
• the organic peroxide can be used as a redox-based polymerization initiator in combination with a reducing agent.
• the reducing agent is not particularly limited, but for example, a compound containing a metal ion in a reduced state such as ferrous sulfate and ferrous naphthenate; a sulfinate such as sodium hydroxymethanesulfinate; a dimethylaniline and the like. Amine compounds; and the like. These reducing agents may be used alone or in combination of two or more.
• the amount of the reducing agent added is not particularly limited, but is preferably 0.01 to 1 part by weight with respect to 1 part by weight of the organic peroxide.
• the method for adding the organic peroxide and the reducing agent is not particularly limited, and known addition methods such as batch addition, divided addition, and continuous addition can be used, respectively.
• the reaction temperature when reacting the conjugated diene polymer with the monomer having a carboxyl group is not particularly limited, but is preferably 15 to 80 ° C, more preferably 30 to 50 ° C.
• the reaction time for reacting the conjugated diene polymer with the monomer having a carboxyl group may be appropriately set according to the above reaction temperature, but is preferably 30 to 300 minutes, more preferably 60 to 120 minutes. be.
• the solid content concentration of the latex of the conjugated diene polymer in reacting the conjugated diene polymer with the monomer having a carboxyl group is not particularly limited, but is preferably 5 to 60% by weight, more preferably 10 to 10 to 100% by weight. It is 40% by weight.
• Examples of the monomer having a carboxyl group include ethylenically unsaturated monocarboxylic acid monomers such as acrylic acid and methacrylic acid; ethylenically unsaturated polyvalents such as itaconic acid, maleic acid, fumaric acid and butentricarboxylic acid.
• Carboxylic acid monomer Partial ester monomer of ethylenically unsaturated polyvalent carboxylic acid such as monobutyl fumarate, monobutyl maleate, mono2-hydroxypropyl maleate; polyvalent carboxylic acid such as maleic anhydride and citraconic anhydride.
• Acid anhydrides; and the like can be mentioned, but ethylenically unsaturated monocarboxylic acid monomers are preferable, and acrylic acid and methacrylic acid are particularly preferable, because the effect of carboxy modification becomes more remarkable.
• these monomers may be used individually by 1 type or in combination of 2 or more types.
• the above-mentioned carboxyl group includes those which are salts with alkali metals, ammonia and the like.
• the amount of the monomer having a carboxyl group to be used is preferably 0.01 parts by weight to 100 parts by weight, more preferably 0.01 parts by weight to 40 parts by weight, and further, with respect to 100 parts by weight of the conjugated diene polymer. It is preferably 0.5 parts by weight to 20 parts by weight.
• the method of adding the monomer having a carboxyl group to the latex of the conjugated diene polymer is not particularly limited, and known addition methods such as batch addition, split addition, continuous addition and the like can be adopted.
• the modification rate of the carboxy-modified conjugated diene-based polymer due to the monomer having a carboxyl group may be appropriately controlled according to the intended use of the obtained conjugated diene-based polymer latex composition, but is preferably 0.01 to 10. By weight%, more preferably 0.2 to 5% by weight, still more preferably 0.3 to 3% by weight, and particularly preferably 0.4 to 2% by weight.
• the modification rate of the monomer having a carboxyl group is within the above range, the viscosity of the latex of the obtained conjugated diene polymer becomes more appropriate, it becomes easier to transfer, and the film molded product of the present invention is heated to a high temperature. It is possible to further suppress the decrease in mechanical strength when stored in.
• X represents the weight of the unit of the monomer having a carboxyl group in the carboxy-modified conjugated diene-based polymer
• Y represents the weight of the carboxy-modified conjugated diene-based polymer.
• X is calculated from the acid amount obtained by 1 H-NMR measurement of the carboxy-modified conjugated diene polymer and 1 H -NMR measurement result, or by neutralization titration. It can be obtained by a method or the like.
• the polymerization catalyst (graft polymerization catalyst) used for graft polymerization is not particularly limited, and is, for example, an inorganic peroxide such as sodium persulfate, potassium persulfate, ammonium persulfate, potassium perphosphate, hydrogen peroxide, etc .; diisopropylbenzenehydro.
• Organic peroxides such as peroxide, cumenehydroperoxide, t-butylhydroperoxide, 1,1,3,3-tetramethylbutylhydroperoxide, di-t-butyl peroxide, isobutyryl peroxide, benzoyl peroxide, etc.
• Oxides such as 2,2'-azobisisobutyronitrile, azobis-2,4-dimethylvaleronitrile, methyl azobisisobutyrate; etc., but organic peroxides are preferable, 1, 1,3,3-Tetramethylbutylhydroperoxide is particularly preferred.
• the above graft polymerization catalysts can be used alone or in combination of two or more.
• the amount of the graft polymerization catalyst used varies depending on the type, but is preferably 0.1 to 10 parts by weight, more preferably 0.2 to 5 parts by weight, based on 100 parts by weight of the conjugated diene-based polymer.
• the method for adding the graft polymerization catalyst is not particularly limited, and known addition methods such as batch addition, divided addition, and continuous addition can be adopted.
• the swell index (SI) of the conjugated diene-based polymer (including the carboxy-modified conjugated diene-based polymer) used in the present invention is preferably 105 to 300%, more preferably 110 to 250, and even more preferably. Is 120-200%.
• SI swell index
• the latex of the conjugated diene polymer is formed into a film, and the obtained film of the conjugated diene polymer is immersed in toluene at 25 ° C. for 1 hour to adjust the width of the film before and after immersion in toluene. It can be obtained by measuring and measuring the linear swelling rate.
• the following dip method can be adopted. That is, in the dip method, first, an acid or an alkali is added to the latex of the conjugated diene polymer to adjust the pH to 8.2. Then, a ceramic mold with a ground surface was prepared, washed, preheated in an oven at 70 ° C. for 30 minutes, and then 18% by weight calcium nitrate and 0.05% by weight polyoxy.
• the film for measurement can be obtained by peeling the film for measurement from the ceramic molding die.
• the thickness of the film for measurement is not particularly limited, but is preferably about 0.2 mm.
• the method for adjusting the swell index (SI) of the latex of the conjugated diene polymer is not particularly limited to the above range, and examples thereof include a method for adjusting the type and composition of the conjugated diene polymer.
• the reaction temperature modification reaction temperature
• the reaction time modification reaction time
• the method for adjusting the type and amount of the monomer having a carboxyl group used in the modification reaction, and the type and amount of the reducing agent used in combination with the organic peroxide in the modification reaction examples include a method of adjustment, and it is desirable to make adjustments by appropriately combining these.
• the latex of the conjugated diene polymer (including the carboxy-modified conjugated diene polymer) used in the present invention contains a pH adjuster, an antifoaming agent, a preservative, and a chelating agent, which are usually blended in the field of latex. , Oxygen scavengers, dispersants and other additives may be added.
• Examples of the pH adjuster include hydroxides of alkali metals such as sodium hydroxide and potassium hydroxide; alkali metal carbonates such as sodium carbonate and potassium carbonate; alkali metal hydrogen carbonates such as sodium hydrogen carbonate; ammonia. ; Organic amine compounds such as trimethylamine and triethanolamine; and the like; but alkali metal hydroxides or ammonia are preferable.
• the solid content concentration of the latex of the conjugated diene polymer (including the carboxy-modified conjugated diene polymer) used in the present invention is preferably 30 to 70% by weight, more preferably 40 to 70% by weight.
• the solid content concentration is in the above range, the generation of agglomerates in the latex can be more effectively suppressed, and the separation of the polymer particles when the latex is stored can be more effectively suppressed.
• the latex composition used in the present invention contains a sulfur-based vulcanizing agent.
• the sulfur-based sulfurizing agent is not particularly limited, and is, for example, sulfur such as powdered sulfur, sulfur flower, precipitated sulfur, colloidal sulfur, surface-treated sulfur, and insoluble sulfur; sulfur chloride, sulfur dichloride, morpholin / disulfide, and alkylphenol disulfide. , Sulfur-containing compounds such as caprolactam disulfide (N, N'-dithio-bis (hexahydro-2H-azepinone-2)), phosphorus-containing polysulfide, high molecular weight polysulfide, 2- (4'-morpholinodithio) benzothiazole Can be mentioned. Of these, sulfur can be preferably used.
• the sulfur-based vulcanizing agent can be used alone or in combination of two or more.
• the content of the sulfur-based vulcanizer in the latex composition is not particularly limited, but is preferably 0.01 to 3 parts by weight, more preferably 0.01 to 3 parts by weight, based on 100 parts by weight of the conjugated diene-based polymer contained in the latex composition. Is 0.1 to 1.2 parts by weight, more preferably 0.1 to 0.8 parts by weight, still more preferably 0.1 to 0.6 parts by weight, and particularly preferably 0.2 to 0.6 parts by weight. Is.
• the content of the sulfur-based vulcanizing agent is within the above range, it is possible to increase the tensile strength and the tear strength at room temperature while suppressing the occurrence of the symptoms of delayed type allergy (Type IV) in the obtained dip molded product. can.
• the latex composition used in the present invention contains a vulcanization accelerator.
• a vulcanization accelerator it is preferable to use a xanthate compound from the viewpoint that the obtained dip molded product is preferably suppressed from the occurrence of delayed type allergy (Type IV) symptoms.
• the xanthogen compound is not particularly limited, and is, for example, xanthate acid, xanthogen acid salt, xanthogen disulfide (a compound in which two xanthogen acids are bonded via a sulfur atom or the like), xanthogen polysulfide (3 or more xanthogens).
• xanthate acid a compound in which two xanthogen acids are bonded via a sulfur atom or the like
• xanthogen disulfide a compound in which two xanthogen acids are bonded via a sulfur atom or the like
• xanthogen polysulfide 3 or more xanthogens
• the xanthate salt may be any as long as it has a xanthate structure, and is not particularly limited.
• Hydrocarbons and Z are metal atoms.
• X is a number corresponding to the valence of Z, and examples thereof include compounds represented by 1 to 4, preferably 2 to 4, and particularly preferably 2.).
• These xanthogenates may be used alone or in combination of two or more.
• the xanthogen disulfide is a compound in which two xanthogen acids are bonded via a sulfur atom or the like, and is not particularly limited, but is not particularly limited, but is not particularly limited, but is dimethylxanthogen disulfide, diethylxantogen disulfide, diisopropylxantogen disulfide, dibutylxantogen disulfide, dimethylxantogen polysulfide, diethyl.
• Examples thereof include xanthogen polysulfide, diisopropylxantogen polysulfide, dibutylxanthogen polysulfide, and among these, diisopropylxantogen disulfide and dibutylxantogen disulfide are preferable.
• Xanthogen polysulfide is a compound in which three or more xanthogen acids are bonded via a sulfur atom or the like, a xanthogen trisulfide in which three xanthate acids are bonded via sulfur, and four xanthogen acids via sulfur. Examples thereof include xanthogen tetrasulfide to which five xanthogen acids are bound via sulfur and xanthogen pentasulfide to which five xanthate acids are bound via sulfur.
• these xanthate compounds may be contained alone in the latex composition, it is preferable that two or more of them are contained.
• a part of the blended xanthate acid is present in the form of xanthogenate, and as a result, the latex composition contains two or more kinds of xanthogen compounds. May be to be done.
• a part of xanthate acid blended in the latex composition may be present in the form of xanthogen disulfide or xanthogen polysulfide by the action of the sulfur-based vulcanizing agent in the latex composition.
• xanthate xanthogen disulfide or xanthogen polysulfide
• these are any of xanthate acid, xanthate salt, xanthogen disulfide and xanthogen polysulfide, respectively. It may exist in the form of.
• a vulcanization accelerator other than the xanthate compound may be used instead of the xanthate compound or together with the xanthate compound.
• sulfurization accelerator other than such a xanthogen compound those usually used in dip molding can be used, for example, diethyldithiocarbamic acid, dibutyldithiocarbamic acid, di-2-ethylhexyldithiocarbamic acid, dicyclohexyldithiocarbamic acid, diphenyldithiocarbamic acid.
• Dithiocarbamic acids such as dibenzyldithiocarbamic acid and their zinc salts; 2-mercaptobenzothiazole, 2-mercaptobenzothiazole zinc, 2-mercaptothiazolin, dibenzothiazyl disulfide, 2- (2,4-dinitrophenylthio) Benzothiazole, 2- (N, N-diethylthio-carbaylthio) benzothiazole, 2- (2,6-dimethyl-4-morpholinothio) benzothiazole, 2- (4'-morpholino-dithio) benzothiazole, 4-morphonylyl -2-Benzothiazole / disulfide, 1,3-bis (2-benzothiazyl / mercaptomethyl) urea and the like can be mentioned.
• the vulcanization accelerator can be used alone or in combination of two or more.
• the content of the vulcanization accelerator in the latex composition is 100% by weight of the conjugated diene polymer contained in the latex composition. It is preferably 0.01 to 10 parts by weight, more preferably 0.1 to 7 parts by weight, and further preferably 0.5 to 5 parts by weight.
• the content of the vulcanization accelerator is in the above range, it is possible to further suppress a decrease in mechanical strength when the membrane molded product of the present invention is stored at a high temperature, and the film molded product of the present invention can be used. The tensile strength and tear strength at room temperature can also be improved.
• the latex composition used in the present invention may further contain an activator.
• the activator acts as a vulcanization accelerator together with the above-mentioned xanthogen compound, whereby the film-molded article after the cross-linked product is cross-linked. It is possible to further suppress the decrease in tear strength when the product is stored at a high temperature, and it is also possible to improve the tear strength of the film-molded article after the crosslinked product at room temperature.
• the activator is not particularly limited, but it is preferable to use a metal compound from the viewpoint of further improving the tear strength of the film-molded product.
• the metal compound is not particularly limited, and examples thereof include a metal oxide and a metal compound containing at least one carbon atom.
• the metal constituting the metal compound is not particularly limited, but is a typical metal (Group 1 element, Group 2 element, Group 12 element, Group 13 element, Group 14 element, Group 15 element, Group 16). At least one element selected from the group consisting of elements, Group 17 elements, and Group 18 elements) is preferable, and Group 2 elements, Group 12 elements, Group 13 elements, and Group 14 elements are more preferable.
• Zinc, magnesium, calcium, aluminum and lead are more preferred, zinc, magnesium and calcium are particularly preferred, and zinc is most preferred.
• These metal compounds may be used alone or in combination of two or more.
• the metal oxide is not particularly limited, but from the viewpoint of further improving the tear strength of the obtained dip molded product, zinc oxide, magnesium oxide, titanium oxide, calcium oxide, lead oxide, iron oxide, copper oxide, and oxidation. Tin, nickel oxide, chromium oxide, cobalt oxide, and aluminum oxide are preferable, and zinc oxide is more preferable.
• the metal compound containing at least one carbon atom a carbonate, a hydrogen carbonate, a hydroxide, and an organic metal compound are preferable from the viewpoint of further improving the tear strength of the obtained dip molded product, and the carbonate and the carbonic acid are preferable.
• Bicarbonates and organic metal compounds are more preferred.
• inorganic salts such as carbonates and hydrogen carbonates are particularly preferable from the viewpoint of excellent stability of the compound itself and excellent availability.
• the content of the activator in the latex composition is preferably 0.01 to 10 parts by weight, more preferably 0.1 to 5 parts by weight, based on 100 parts by weight of the conjugated diene polymer contained in the latex composition. Parts, more preferably 1 to 3 parts by weight.
• the content of the activator is in the above range, it is possible to further suppress a decrease in tear strength when the membrane molded product of the present invention is stored at a high temperature, and the membrane molded product of the present invention is at room temperature. The tear strength can also be improved.
• the method of blending the activator is not particularly limited as long as it is a method in which the latex of the conjugated diene polymer and the activator are finally mixed.
• the latex composition used in the present invention is at least one selected from a phenol-based anti-aging agent and a quinoline-based anti-aging agent as an anti-aging agent, and has a molecular weight of 300 to 600 (hereinafter, "" May be referred to as "specific anti-aging agent").
• the phenolic antioxidant is an aromatic compound having one or more phenolic hydroxyl groups (hydroxyls directly bonded to the benzene ring structure in the aromatic compound).
• the phenolic anti-aging agent as a specific anti-aging agent, an aromatic compound having a hindered phenol structure is preferable.
• the hindered phenol structure refers to a substituent other than a hydrogen atom in which one of the two ortho positions of the phenolic hydroxyl group is substituted with a hydrocarbon group having 4 or more carbon atoms. Means the structure replaced by.
• the above-mentioned hydrocarbon group having 4 or more carbon atoms, which is located at one of the ortho positions of the phenolic hydroxyl group, may have a substituent.
• Aromatic compounds having a hindered phenol structure one of the two ortho positions of the phenolic hydroxyl group is substituted with a tert-butyl group, and the other is substituted with a substituent other than a hydrogen atom.
• the phenolic antioxidant as the specific antioxidant may be any one having at least one phenolic hydroxyl group and having a molecular weight in the range of 300 to 600.
• the phenolic antioxidant may be used. It can be classified into an aromatic compound (a) having two or more phenolic hydroxyl groups and an aromatic compound (b) having one phenolic hydroxyl group.
• the "compound having two or more phenolic hydroxyl groups” includes a compound having one or more benzene ring structures in which two or more phenolic hydroxyl groups are bonded, and one or more phenolic hydroxyl groups. A compound having two or more benzene ring structures bonded to the compound is included.
• the phenolic hydroxyl groups present in two or more in the aromatic compound (a) having two or more phenolic hydroxyl groups may be bonded to the same benzene ring or may be bonded to different benzene rings. There may be.
• aromatic compound (a) having two or more phenolic hydroxyl groups examples include 2,2'-methylenebis (4-methyl-6-tert-butylphenol) and 2,2'-methylenebis (4-ethyl-6-).
• t-butylphenol 4,4'-methylenebis (2,6-di-t-butylphenol), 2,2'-methylene-bis (6- ⁇ -methyl-benzyl-p-cresol), 4,4'- Butylidenebis (3-methyl-6-tert-butylphenol), 4,4'-thiobis (6-tert-butyl-o-cresol), 2,2'-thiobis- (4-methyl-6-t-butylphenol), 4,4'-thiobis (3-methyl-6-tert-butylphenol), bis [3- (3-t-butyl-4-hydroxy-5-methylphenyl) propionic acid] [ethylenebis (oxyethylene)], etc. Can be mentioned.
• aromatic compound (a) having two or more phenolic hydroxyl groups it is possible to suppress the decrease in mechanical strength when the obtained membrane molded product is stored at a high temperature, and thus hindered.
• An aromatic compound (a-1) having two or more phenolic structures is preferable.
• examples of the aromatic compound (a-1) having two or more hindered phenol structures include 2,2'-methylenebis (4-methyl-6-tert-butylphenol) and 2,2'-methylenebis (4-ethyl).
• the aromatic compound (a-1) having two or more hindered phenol structures has a molecular weight of 300 to 600 and has two or more hindered phenol structures, and has a diphenylmethane skeleton (a-2). Is more preferable.
• Examples of the aromatic compound (a-2) having two or more hindered phenol structures and having a diphenylmethane skeleton include 2,2'-methylenebis (4-methyl-6-tert-butylphenol) and 2,2'-. Methylenebis (4-ethyl-6-t-butylphenol), 4,4'-methylenebis (2,6-di-t-butylphenol), 2,2'-methylene-bis (6- ⁇ -methyl-benzyl-p- Cresol) and the like.
• the aromatic compound (a-2) having a diphenylmethane skeleton having two or more hindered phenol structures the aromatic compound (a-) having a hindered phenol structure on each of the two benzene rings constituting the diphenylmethane skeleton.
• 3) is preferable, and among them, 4,4'-methylenebis (2,6-di-tert-butylphenol) or 2,2'-methylenebis (4-methyl-6-tert-butylphenol) is more preferable, and 2,2'.
• -Methylenebis (4-methyl-6-tert-butylphenol) is more preferred.
• aromatic compound (b) having one phenolic hydroxyl group examples include 2,6-di-t-butyl-4- (4,6-bis (octylthio) -1,3,5-triazine-2-. Ilamino) phenol, octadecyl-3- (3,5-di-t-butyl-4-hydroxyphenyl) propionate, 3- (3,5-di-t-butyl-4-hydroxyphenyl) propionate octadecyl, octyl- Examples thereof include 3,5-di-tert-butyl-4-hydroxy-hydrosilicic acid, 4,6-bis [(dodecylthio) methyl] -6-methylphenol and the like.
• the molecular weight of the aromatic compound (b) having one phenolic hydroxyl group is preferably 350 to 600, more preferably 400 to 600, and even more preferably 450 to 600.
• an aromatic compound (b-1) having one phenolic hydroxyl group and one or more -NH- bonds is preferable.
• the aromatic compound (b-1) having one phenolic hydroxyl group and one or more -NH- bonds can make the obtained membrane molded product excellent in ozone deterioration resistance. ..
• the aromatic compound (b-1) having one phenolic hydroxyl group and one or more -NH- bonds is 2,6-di-t-butyl-4- (4,6-bis (4,6-bis) (4,6-bis). Octylthio) -1,3,5-triazine-2-ylamino) phenol is preferred.
• the quinoline-based antiaging agent is a heterocyclic aromatic compound having one or more quinoline structures (quinoline which may have a substituent) and has a molecular weight in the range of 300 to 600. good.
• examples of the quinoline-based antiaging agent include 2,2,4-trimethyl-1,2-dihydroquinoline polymers.
• the specific antioxidant used in the present invention preferably contains at least a phenolic antioxidant, more preferably one containing at least an aromatic compound (a) having two or more phenolic hydroxyl groups, and 2 phenolic hydroxyl groups.
• Those containing the aromatic compound (a) having one or more and the aromatic compound (b) having one phenolic hydroxyl group are more preferable, and the aromatic compound (a) having two or more phenolic hydroxyl groups and the phenolic compound (a) are phenolic.
• Those containing an aromatic compound (b-1) having one hydroxyl group and one or more -NH- bonds are particularly preferable, and an aromatic compound (a-) having two or more hindered phenol structures is particularly preferable.
• Those containing 1) and an aromatic compound (b-1) having one phenolic hydroxyl group and one or more -NH- bonds are particularly preferable, and have two or more hindered phenolic structures. Most preferably, it contains an aromatic compound (a-2) having a diphenylmethane skeleton and an aromatic compound (b-1) having one phenolic hydroxyl group and one or more -NH- bonds.
• the phenolic hydroxyl group is 2 Weight-based content ratio of the aromatic compound (a) having two or more and the aromatic compound (b) having one phenolic hydroxyl group (aromatic compound (a) having two or more phenolic hydroxyl groups: phenolic hydroxyl group)
• the aromatic compound (b) having one of the above is preferably 1:99 to 99: 1, more preferably 10:90 to 98: 2, more preferably 25:75 to 95: 5, and 55:45 to. 90:10 is particularly preferable.
• the molecular weight of the specific antiaging agent used in the present invention may be 300 to 600 and is not particularly limited. Further, two or more kinds of specific anti-aging agents may be used in combination as the specific anti-aging agent, and when the latex composition contains two or more kinds of specific anti-aging agents, the molecular weight of the specific anti-aging agent is , The weight average molecular weight of the two or more specified antiaging agents is adopted. That is, in the present invention, the weight average molecular weight of the specific antiaging agent contained in the latex composition is 300 to 600.
• the molecular weight of the specific antiaging agent used in the present invention is preferably 310 to 590, preferably 320 to 540, because it can further suppress a decrease in mechanical strength when the film molded product of the present invention is stored at a high temperature. More preferably, 330 to 440 is even more preferable.
• the content of the specific antioxidant in the latex composition is preferably 0.05 to 10 parts by weight, more preferably 0.1 to 5 parts by weight, based on 100 parts by weight of the conjugated diene polymer contained in the latex composition. By weight, more preferably 0.5 to 3 parts by weight.
• the latex composition used in the present invention may further contain an anti-aging agent other than the above-mentioned specified anti-aging agent, but preferably does not contain an anti-aging agent other than the above-mentioned specified anti-aging agent.
• the latex composition further contains various compounding agents such as a dispersant; a reinforcing agent such as carbon black, silica and talc; a filler such as calcium carbonate and clay; an ultraviolet absorber; a plasticizer; and the like, if necessary. Can be done.
• the method for mixing various compounding agents with the latex composition is not particularly limited, and is, for example, a composition containing a latex of a conjugated diene-based polymer, a sulfur-based vulcanization agent, a vulcanization accelerator, and the above-mentioned specific antiaging agent.
• a method of mixing various compounding agents to be blended as necessary with the obtained composition by using a disperser such as a ball mill, a kneader, or a disper can be mentioned.
• a disperser such as a ball mill, a kneader, or a disper
• at least a part of the various compounding agents may be compounded after aging, which will be described later.
• the solid content concentration of the latex composition used in the present invention is preferably 1 to 40% by weight, more preferably 3 to 35% by weight, still more preferably 5 to 30% by weight, and particularly preferably 10 to 20% by weight.
• the latex composition used in the present invention it is preferable that the latex composition is aged (pre-vulcanized) before being subjected to molding from the viewpoint of ensuring sufficient mechanical properties of the obtained film molded product.
• the aging (pre-vulcanization) time is not particularly limited, but is preferably 8 to 120 hours, more preferably 24-72 hours.
• the temperature of aging (pre-vulcanization) is not particularly limited, but is preferably 20 to 40 ° C.
• the aging (pre-vulcanization) conditions are maintained (the aging (pre-vulcanization) is continued).
• Dip molding and the like may be continuously performed, and in this case, the aging (pre-vulcanization) time and the aging (pre-vulcanization) temperature may be within the above ranges.
• the film-molded article of the present invention is a film-molded article having a thickness of 20 to 300 ⁇ m obtained by using the above-mentioned latex composition.
• the thickness of the film molded product of the present invention may be 20 to 300 ⁇ m, and is not particularly limited, but is preferably 50 to 280 ⁇ m, more preferably 100 to 260 ⁇ m, and particularly preferably 140 to 250 ⁇ m.
• the thickness of the film-molded body can be obtained, for example, by selecting five measurement points from the film-molded body, measuring the thickness of the selected five points, and calculating the arithmetic mean thereof.
• the film molded body of the present invention is not particularly limited, but a dip molded body obtained by dip molding the above-mentioned latex composition is preferable.
• Dip molding is a method in which a mold is dipped in a latex composition, the composition is deposited on the surface of the mold, then the mold is pulled up from the composition, and then the composition deposited on the surface of the mold is dried. be.
• the mold before being immersed in the latex composition may be preheated. Further, a coagulant can be used as needed before the mold is immersed in the latex composition or after the mold is pulled out of the latex composition.
• the method of using the coagulant include a method of immersing the mold before being immersed in the latex composition in a solution of the coagulant to attach the coagulant to the mold (anodic adhesion dipping method), and depositing the latex composition.
• anodic adhesion dipping method There is a method of immersing the formed mold in a coagulant solution (Teeg adhesion immersion method), but the anode adhesion immersion method is preferable in that a dip molded body having less uneven thickness can be obtained.
• coagulants include metal halides such as barium chloride, calcium chloride, magnesium chloride, zinc chloride and aluminum chloride; nitrates such as barium nitrate, calcium nitrate and zinc nitrate; acetic acid such as barium acetate, calcium acetate and zinc acetate. Salts; water-soluble polyvalent metal salts such as calcium sulfate, magnesium sulfate, sulfates such as aluminum sulfate; Among them, calcium salt is preferable, and calcium nitrate is more preferable. These water-soluble polyvalent metal salts can be used alone or in combination of two or more.
• the coagulant can usually be used as a solution of water, alcohol, or a mixture thereof, and is preferably used in the form of an aqueous solution.
• This aqueous solution may further contain a water-soluble organic solvent such as methanol or ethanol or a nonionic surfactant.
• the concentration of the coagulant varies depending on the type of the water-soluble polyvalent metal salt, but is preferably 5 to 50% by weight, more preferably 10 to 30% by weight.
• the mold out of the latex composition After pulling the mold out of the latex composition, it is usually heated to dry the deposits formed on the mold.
• the drying conditions may be appropriately selected.
• the obtained dip molded layer is heat-treated and crosslinked.
• the obtained dip molded layer is immersed in water, preferably warm water at 30 to 70 ° C. for about 1 to 60 minutes to remove water-soluble impurities (for example, excess emulsifier, coagulant, etc.). It may be removed.
• water-soluble impurities for example, excess emulsifier, coagulant, etc.
• the operation for removing water-soluble impurities may be performed after the dip molded layer has been heat-treated, but it is preferably performed before the heat treatment because the water-soluble impurities can be removed more efficiently.
• Crosslinking of the dip molded layer is usually carried out by subjecting the dip molded layer to a heat treatment at a temperature of 80 to 150 ° C., preferably 10 to 130 minutes.
• a heating method a method of external heating by infrared rays or heated air or internal heating by high frequency can be adopted. Of these, external heating with heated air is preferable.
• the dip molded body is obtained as a film-shaped film molded body.
• a desorption method a method of manually peeling from the molding die or a method of peeling by water pressure or compressed air pressure can be adopted. After desorption, heat treatment may be further performed at a temperature of 60 to 120 ° C. for 10 to 120 minutes.
• the film-molded article of the present invention can be any method as long as it can form the above-mentioned latex composition into a film (for example, a coating method). It may be obtained by the method of.
• the film-molded article of the present invention suppresses a decrease in mechanical strength when stored at a high temperature. Therefore, the film-molded article of the present invention is suitable as an article that is required to have mechanical properties such as tensile strength and tear strength and can be stored at a high temperature of about 70 ° C. or lower, or an article that can be stored at room temperature for a long period of time. Can be used.
• the film-molded article of the present invention can be particularly preferably used as a glove.
• gloves are made of inorganic fine particles such as talc and calcium carbonate or organic fine particles such as starch particles. It may be sprayed on the surface, an elastomer layer containing fine particles may be formed on the surface of the glove, or the surface layer of the glove may be chlorinated.
• the film-molded body of the present invention includes medical supplies such as baby bottle nipples, droplets, tubes, water pillows, balloon cots, catheters, and condoms; toys such as balloons, dolls, and balls; and pressurization.
• Medical products such as molding bags and gas storage bags; it can also be used for finger cots and the like.
• Degeneration rate (% by weight) (X / Y) x 100
• X represents the weight of the unit of the monomer having a carboxyl group in the carboxy-modified synthetic polyisoprene
• Y represents the weight of the carboxy-modified synthetic polyisoprene
• the ceramic mold was taken out from the coagulant aqueous solution, and the ceramic mold coated with the coagulant was dried in an oven at 70 ° C. for 20 minutes.
• a ceramic mold coated with a latex of carboxy group-modified synthetic polyisoprene was immersed in warm water at 60 ° C. for 2 minutes and then dried at room temperature for 6 hours. A ceramic mold coated with a film for measurement was obtained.
• ⁇ Thickness of dip molded body> Select 5 measurement points within 3 cm from the part of the dip molded body corresponding to the part where the contact time with the coagulant solution is the longest (tip of the glass mold) when the glass mold is immersed in the coagulant solution. did. Then, the thickness of the selected 5 points was measured, the arithmetic mean of the measured thicknesses of the 5 points was obtained, and the obtained value (unit: mm) was taken as the thickness of the dip molded body.
• the test piece was pulled by a Tensilon universal tester (trade name "RTG-1210", manufactured by Orientec Co., Ltd.) at a tensile speed of 500 mm / min, and the tensile strength (unit: MPa) immediately before breaking was measured.
• RMG-1210 manufactured by Orientec Co., Ltd.
• ⁇ Tear strength of dip molded product The dip molded body (dip molded body before aging) was heated at 70 ° C. for 7 days to obtain a dip molded body after aging. Based on ASTM D624-00, the pre-aged dip molded product and the post-aged dip molded product were left in a constant temperature and humidity chamber at 23 ° C. and a relative humidity of 50% for 24 hours or more, and then dumbbells (trade name “Die C”). , Manufactured by Dumbbell) to prepare a test piece for measuring tear strength.
• the test piece was pulled by a Tensilon universal tester (trade name "RTG-1210", manufactured by A & D Co., Ltd.) at a tensile speed of 500 mm / min, and the tear strength (unit: N / mm) was measured.
• RTG-1210 manufactured by A & D Co., Ltd.
• ⁇ Manufacturing example 1> Manufacture of Latex (A-1) of Carboxy-modified Synthetic Polyisoprene) Synthetic polyisoprene (trade name "NIPOL IR2200L", manufactured by Zeon Corporation) is mixed with n-hexane (boiling point: 69 ° C), and the temperature is raised to 60 ° C with stirring to dissolve the synthetic polyisoprene concentration 15. An n-hexane solution (a) of synthetic polyisoprene in% by weight was prepared.
• potassium rosinate was added to water, the temperature was raised to 60 ° C. and dissolved to prepare an emulsifier aqueous solution (b) having a concentration of 1.5% by weight.
• n-hexane solution (a) of the synthetic polyisoprene obtained above and the emulsified aqueous solution (b) were added to 100 parts of the synthetic polyisoprene in the n-hexane solution (a) of the synthetic polyisoprene. Then, mix using a mixer (product name "multi-line mixer MS26-MMR-5.5L", manufactured by Satake Chemical Machinery Co., Ltd.) so that the amount of potassium loginate in the aqueous emulsion solution (b) is 10 parts.
• a mixer product name "multi-line mixer MS26-MMR-5.5L", manufactured by Satake Chemical Machinery Co., Ltd.
• an emulsified dispersion (c) was obtained by mixing and emulsifying at a rotation speed of 4100 rpm using an emulsifying device (product name "Milder MDN310", manufactured by Pacific Kiko Co., Ltd.).
• the total feed flow velocity of the n-hexane solution (a) of the synthetic polyisoprene and the emulsifier aqueous solution (b) is 2,000 kg / hr
• the temperature is 60 ° C.
• the back pressure (gauge pressure) is 0.5 MPa. And said.
• the obtained emulsion dispersion (c) was heated to 80 ° C. under a reduced pressure of ⁇ 0.01 to ⁇ 0.09 MPa (gauge pressure), n-hexane was distilled off, and water of synthetic polyisoprene was added.
• the dispersion liquid (d) was obtained.
• a defoaming agent (trade name "SM5515", manufactured by Toray Dow Corning Co., Ltd.) was continuously added while spraying so as to have an amount of 300 wt ppm with respect to the synthetic polyisoprene in the emulsion dispersion (c). did.
• the emulsion dispersion (c) When distilling off n-hexane, the emulsion dispersion (c) is adjusted to be 70% by volume or less of the volume of the tank, and a three-stage inclined paddle blade is used as the stirring blade at 60 rpm. The stirring was carried out slowly in.
• the obtained aqueous dispersion (d) of synthetic polyisoprene is used in a continuous centrifuge (product name "SRG510", manufactured by Alfa Laval Co., Ltd.).
• the mixture was concentrated by centrifugation at 000 to 9,000 G to obtain a latex (e) of synthetic polyisoprene having a solid content concentration of 60% by weight as a light liquid.
• the conditions for centrifugation were as follows: the solid content concentration of the aqueous dispersion (d) before centrifugation was 8% by weight, the flow velocity during continuous centrifugation was 1300 kg / hr, and the back pressure (gauge pressure) of the centrifuge was 0. It was set to 1 MPa.
• the latex (e) of synthetic polyisoprene to which a dispersant was added was charged into a reaction vessel equipped with a stirrer substituted with nitrogen, and the temperature was heated to 30 ° C. while stirring. Further, using another container, 3 parts of methacrylic acid as a carboxyl group-containing compound and 16 parts of distilled water were mixed to prepare a diluted methacrylic acid solution. This diluted methacrylic acid solution was added to the reaction vessel kept at a temperature of 20 ° C. over 30 minutes.
• Example 1> (Preparation of aqueous dispersion of sulfur) Sulfur 0.5 parts, sodium salt of ⁇ -naphthalene sulfonic acid formalin condensate as an anionic surfactant (trade name "Demor T-45", manufactured by Kao Co., Ltd.) 0.03 parts (6. 0 parts), 0.004 parts of 5% potassium hydroxide aqueous solution, and 0.42 parts of water are mixed with a ball mill (trade name "Magnetic ball mill", manufactured by Nikko Kagaku Co., Ltd.) to perform crushing treatment. Then, an aqueous dispersion of sulfur was obtained.
• a ball mill trade name "Magnetic ball mill", manufactured by Nikko Kagaku Co., Ltd.
• a ceramic porcelain ball of ⁇ 10 mm to ⁇ 35 mm (a mixture of ⁇ 10 mm, ⁇ 15 mm, ⁇ 20 mm, ⁇ 25 mm, ⁇ 30 mm and ⁇ 35 mm ceramic porcelain balls) was used, and the mixing condition was 72 hours at 50 rpm. ..
• An aqueous dispersion of a xanthate compound was obtained by mixing 05 parts with a ball mill (trade name "porcelain ball mill", manufactured by Nikko Kagaku Co., Ltd.) to perform a crushing treatment.
• a ball mill trade name "porcelain ball mill", manufactured by Nikko Kagaku Co., Ltd.
• a ceramic porcelain ball of ⁇ 10 mm to ⁇ 35 mm (a mixture of ⁇ 10 mm, ⁇ 15 mm, ⁇ 20 mm, ⁇ 25 mm, ⁇ 30 mm and ⁇ 35 mm ceramic porcelain balls) was used, and the mixing condition was 72 hours at 50 rpm. ..
• Anti-aging agent which is an aromatic compound (a-3)) 1.5 parts, 6- (4-hydroxy-3,5-di-tert-butylanilino) -2,4-bis (octylthio) -1,3 5-Triazine (trade name "Irganox 565", manufactured by BASF, molecular weight 589, aging which is an aromatic compound (b-1) having one phenolic hydroxyl group and one or more -NH- bonds).
• Inhibitor Add an aqueous dispersion of each compound to 0.5 parts, and then aged for 48 hours (pre-sulfurization) in a constant temperature water bath adjusted to 25 ° C to obtain a latex composition. rice field.
• the hand mold coated with the coagulant was taken out from the oven and immersed in the 48-hour aged latex composition obtained above for 10 seconds.
• the hand mold was air-dried at room temperature for 10 minutes and then immersed in warm water at 60 ° C. for 5 minutes to elute water-soluble impurities to form a dip-molded layer on the hand mold.
• the dip molded layer formed in the hand mold was vulcanized by heating it in an oven at a temperature of 130 ° C. for 30 minutes, cooled to room temperature, sprayed with talc, and then peeled off from the hand mold.
• a glove-shaped dip molded body was obtained.
• the thickness, tensile strength and tear strength of the dip molded body were measured according to the above method. The results are shown in Table 1.
• Example 2 6- (4-Hydroxy-3,5-di-tert-butylanilino) -2,4-bis (octylthio) -1,3,5-triazine aqueous dispersion was not added and 2,2'-methylenebis (2,2'-methylenebis (The dip molded product was prepared in the same manner as in Example 1 except that the amount of the aqueous dispersion of 4-methyl-6-tert-butylphenol) was changed from 1.5 parts to 2.0 parts in terms of solid content. Obtained. Using the obtained dip molded product, the thickness, tensile strength and tear strength of the dip molded product were measured according to the above method. The results are shown in Table 1.
• Example 3 An aqueous dispersion of 2,2'-methylenebis (4-methyl-6-tert-butylphenol) and 6- (4-hydroxy-3,5-di-tert-butylanilino) -2,4-bis (octylthio) -1 , 3,5-Triazine aqueous dispersion is not added, instead, 4,4'-methylenebis (2,6-di-tert-butylphenol) (trade name "Ethanox 702", manufactured by Ethyl, molecular weight 425, An aqueous dispersion of an aromatic compound (a-3) having a hindered phenol structure (an antioxidant) was added to 100 parts of carboxy-modified synthetic polyisoprene in a mixture on each of the two benzene rings constituting the diphenylmethane skeleton.
• 4,4'-methylenebis (2,6-di-tert-butylphenol) trade name "Ethanox 702", manufactured by Ethyl,
• a dip-molded product was obtained in the same manner as in Example 1 except that it was added so as to be 2.0 parts in terms of solid content. Using the obtained dip molded product, the thickness, tensile strength and tear strength of the dip molded product were measured according to the above method. The results are shown in Table 1.
• Example 4 A dip molded product was obtained in the same manner as in Example 3 except that the latex (A-2) of the carboxy-modified synthetic polyisoprene was used instead of the latex (A-1) of the carboxy-modified synthetic polyisoprene. Using the obtained dip molded product, the thickness, tensile strength and tear strength of the dip molded product were measured according to the above method. The results are shown in Table 1.
• Example 5 A dip molded product was obtained in the same manner as in Example 3 except that the solid content concentration of the latex (A-1) of the carboxy-modified synthetic polyisoprene was changed from 40% by weight to 30% by weight. Using the obtained dip molded product, the thickness, tensile strength and tear strength of the dip molded product were measured according to the above method. The results are shown in Table 1.
• a dip molded product was obtained in the same manner as in Example 1 except that the aqueous dispersion was added to 100 parts of the carboxy-modified synthetic polyisoprene in the mixture so as to have a solid content of 2.0 parts.
• the thickness, tensile strength and tear strength of the dip molded product were measured according to the above method. The results are shown in Table 1.
• a thickness of 20 to 300 ⁇ m obtained by using a latex composition containing a latex of a conjugated diene polymer, a sulfur-based vulcanizing agent, a vulcanization accelerator, and an antiaging agent.
• the decrease in mechanical strength when stored at 70 ° C. was suppressed (Examples 1 to 5).
• the film molded product obtained by using the antiaging agent having a molecular weight of less than 300 or more than 600 had a large decrease in mechanical strength when stored at 70 ° C. (Comparative Examples 1, 3). 4).
• the film molded product obtained by using the antiaging agent having a molecular weight of more than 600 has a large decrease in mechanical strength when stored at 70 ° C. even when the thickness is more than 300 mm. There was (Comparative Example 2).

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