WO2006057392A1 - ディップ成形用組成物及びディップ成形品 - Google Patents
ディップ成形用組成物及びディップ成形品 Download PDFInfo
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- WO2006057392A1 WO2006057392A1 PCT/JP2005/021825 JP2005021825W WO2006057392A1 WO 2006057392 A1 WO2006057392 A1 WO 2006057392A1 JP 2005021825 W JP2005021825 W JP 2005021825W WO 2006057392 A1 WO2006057392 A1 WO 2006057392A1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/02—Direct processing of dispersions, e.g. latex, to articles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C41/00—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
- B29C41/02—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor for making articles of definite length, i.e. discrete articles
- B29C41/14—Dipping a core
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- 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
- C08K5/14—Peroxides
-
- 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
- C08J2313/00—Characterised by the use of rubbers containing carboxyl groups
- C08J2313/02—Latex
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2321/00—Characterised by the use of unspecified rubbers
Definitions
- the present invention relates to a dip-molding composition and a dip-molded product for producing rubber gloves and the like, and more specifically, a dip that provides a dip-molded product having high tensile strength and high bending fatigue resistance.
- the present invention relates to a molding composition and the dip-molded product. Further, the present invention relates to a dip-forming composition and the dip-molded product, which have a low surface electrical resistivity, a good texture, and are less likely to be colored even when worn and worked for a long time.
- Rubber gloves are used in a wide range of applications such as housework, food-related industry, precision industry, and medicine. Rubber gloves have a good texture by expanding and contracting following the movement of the fingers so that they do not get tired even if worn for a long time (300% tensile stress is small and elongation is large), and they are torn during work. Various characteristics are required, such as not to have (sufficient tensile strength), and to not deteriorate even if the oil is touched (being oil resistant).
- the above rubber gloves are usually used as a dip molding composition mainly composed of rubber latex after a coagulant such as calcium nitrate or salt calcium is adhered to the surface of a hand-shaped mold. It is manufactured by dipping and drawing the rubber latex adhering to the surface into a film by heating.
- a coagulant such as calcium nitrate or salt calcium
- Patent Document 2 discloses a rubber glove dip-molded using a dip-molding composition containing a carboxy-modified NBR latex, zinc oxide, sulfur and a vulcanization accelerator.
- this glove is excellent in texture, there is a concern that it may be broken during wearing due to insufficient tensile strength.
- dip-molding is performed with a dip-forming composition containing a specific amount of carboxyl-modified NBR latex containing a carboxyl group, a small amount of zinc oxide, a relatively large amount of sulfur and a vulcanization accelerator.
- Rubber gloves are disclosed. However, when this glove was worn and the work was continued, although it was relatively excellent in bending fatigue resistance, the glove itself was colored and its commercial value could be significantly reduced.
- Patent Document 4 describes a dip-molding composition in which dicumyl peroxide or dibutyl peroxide is mixed with natural rubber or synthetic rubber latex, and a chemically inert high temperature.
- a dip-molded product obtained by crosslinking reaction in a molten salt bath is disclosed.
- these rubber gloves have a good texture and sufficient tensile strength, they have coloring problems caused by exposure to high temperatures during production, and wear on the crotch of fingers for 2-3 hours. There is a problem inferior in bending fatigue resistance in which microcracks are generated.
- Patent Document 1 International Publication No. W097Z48765
- Patent Document 2 US Patent 5,014,362
- Patent Document 3 International Publication No. WO00Z21451
- Patent Document 4 International Publication No. WO01Z77210
- the present invention provides a dip-molded article that has a good texture, excellent tensile strength and bending fatigue resistance, and is capable of giving a dip-molded product that is less likely to be colored even when worn and worked for a long time. It is an object to provide a composition for use. Furthermore, even after washing with ultrapure water, the surface electrical resistivity is low, the texture is good, the tensile strength and the bending fatigue resistance are excellent, and the dip is less likely to cause coloration even after prolonged wearing. Another object of the present invention is to provide a dip molding composition that can give a molded product.
- the present inventors have mixed and ripened a specific organic peroxide together with a specific combination of dispersion stabilizers into a conjugated gen rubber latex.
- the present inventors have found that the above object can be achieved by a composition, and based on this finding, completed the present invention.
- Organic peroxides that are solid at normal pressure and 30 ° C are made into aqueous dispersions in the presence of surfactants and polymer protective colloids, which are added to conjugated rubber rubber latex to age the force.
- Dip-molding according to 1 above which is a latex of a copolymer of a conjugated gen monomer, a carboxyl group-containing ethylenically unsaturated monomer, and a monomer copolymerizable therewith. Composition.
- composition for dip molding as described in 1 above, comprising 05 to 5 parts by weight and 0.1 to 20 parts by weight of polymer protective colloid.
- a dip-forming composition comprising the dip-forming composition according to any one of 1 to 8 above, comprising a quaternary ammonium salt having a hydrocarbon group containing a carbon-carbon unsaturated bond. .
- composition according to 8 above containing 0.1 to 10 parts by weight of a quaternary ammonium salt having a hydrocarbon group containing a carbon-carbon unsaturated bond based on 100 parts by weight of the solid content of the conjugated rubber rubber latex. Dip molding composition.
- the texture is good, the tensile strength and the bending fatigue resistance are excellent, and a long time
- a dip-forming composition that can give a dip-molded product that hardly causes coloring even when worn and worked. Also provided is a dip-forming composition having a low surface electrical resistivity even after washing with ultrapure water.
- the dip molding composition of the present invention uses an organic peroxide that is solid at normal pressure and 30 ° C as an aqueous dispersion in the presence of a surfactant and a protective polymer colloid. Is added to the conjugated gen rubber latex to age the force.
- conjugated diene rubber latex used in the present invention compositions Do limited as long as latex rubber containing conjugated diene monomer units 30 wt 0/0 or more molecular structures.
- Synthetic rubber latex includes synthetic rubber latex and natural rubber latex. Synthetic rubber latex is preferred because various properties of dip-molded products can be adjusted arbitrarily.
- the synthetic rubber latex is produced by polymerizing a conjugated diene monomer, or by copolymerizing a conjugated diene monomer and a monomer copolymerizable therewith.
- the polymerization method is not particularly limited, but radical polymerization by an emulsion polymerization method is preferably employed.
- the use of an ethylenically unsaturated acid monomer is preferable because a dip-molded product having excellent tensile strength can be obtained.
- the conjugation monomer is not limited as long as it is a compound having 4 to 12 carbon atoms and containing conjugation.
- Examples of strong conjugation monomers include 1,3 butadiene, isoprene, 2,3 dimethyl-1,3 butadiene, 2 ethyl-1,3 butadiene, 1,3 pentagene, and black mouthplane. Of these, 1,3 butadiene and isoprene are preferred. These conjugation monomers can be used alone or in combination of two or more.
- the amount of the conjugation monomer used is preferably 30 to: LOO% by weight, more preferably 50 to 84% by weight, particularly preferably 55 to 81% by weight, based on all monomers. If this amount is too small, the texture tends to be inferior, and conversely if too large, the bow I tension strength tends to be inferior.
- the ethylenically unsaturated acid monomer has one carbon-carbon double bond and contains 1 to 4 carboxyl groups, sulfonic acid groups, phosphoric acid groups or sulfuric acid groups, and has 3 to 12 carbon atoms. It is not limited as long as it is a compound.
- Examples of powerful ethylenically unsaturated acid monomers include carboxyl Examples thereof include a group-containing ethylenically unsaturated monomer, a sulfonic acid group-containing ethylenically unsaturated monomer, and a phosphate group-containing ethylenically unsaturated monomer.
- Examples of the carboxyl group-containing ethylenically unsaturated monomer include ethylenically unsaturated monocarboxylic acids such as acrylic acid, methacrylic acid, and crotonic acid; fumaric acid, maleic acid, itaconic acid, and maleic anhydride. And ethylenically unsaturated polyvalent carboxylic acids such as itaconic anhydride and anhydrides thereof; and partial esters of ethylenically unsaturated polyvalent carboxylic acids such as methyl maleate and methyl itaconic acid.
- monocarboxylic acids such as acrylic acid, methacrylic acid, and crotonic acid
- fumaric acid, maleic acid, itaconic acid, and maleic anhydride ethylenically unsaturated polyvalent carboxylic acids
- polyvalent carboxylic acids such as itaconic anhydride and anhydrides thereof
- partial esters of ethylenically unsaturated polyvalent carboxylic acids
- Examples of the sulfonic acid group-containing ethylenically unsaturated monomer include vinyl sulfonic acid, methyl vinyl sulfonic acid, styrene sulfonic acid, (meth) aryl sulfonic acid, (meth) allylic acid 2-ethyl sulfonate, 2-acrylamide.
- Examples include 2-hydroxypropanesulfonic acid.
- Examples of phosphoric acid group-containing ethylenically unsaturated monomers include (meth) acrylic acid-3-chloro-2-propyl phosphate, (meth) acrylic acid-2-ethyl phosphate, 3-alkyloxy-2-hydroxypropane phosphorus An acid etc. are mentioned.
- ethylenically unsaturated acid monomers can be used alone or in combination of two or more, and can also be used as an alkali metal salt or an ammonium salt.
- methacrylic acid which is preferably an ethylenically unsaturated monocarboxylic acid, which is preferably a carboxyl group-containing ethylenically unsaturated monomer, can be particularly preferably used.
- the amount of the ethylenically unsaturated acid monomer used is preferably 0.5 to 10% by weight, more preferably 1 to 9% by weight, particularly preferably 2 to 8% by weight based on the total amount of monomers. %. If this amount is too small, the bow I tension tends to be inferior, and conversely if too large, it tends to be inferior to the texture.
- Monomers that can be copolymerized with a conjugation monomer and an ethylenically unsaturated acid monomer are particularly limited.
- ethylenically unsaturated-tolyl monomers such as acrylonitrile, meta-tali-to-tolyl, 2-chloro-propene nitrile, 2-butene nitrile; styrene, ⁇ -methyl styrene, monochloro styrene, Aromatic butyl monomers such as dichlorostyrene, trichlorostyrene, monomethylstyrene, dimethylstyrene, trimethylstyrene, hydroxymethylstyrene; Ethyl methacrylate unsaturated carboxylic acid amide monomers such as N, N-dimethylacrylamide, N-methylolacrylamide; methyl (meth) acrylate,
- butyl ether monomers such as redene, fluorinated vinyl and vinylidene fluoride; olefin monomers such as ethylene, propylene, 1-butene and isobutene; methyl vinyl ether, n-propyl vinyl ether, isobutyl vinyl ether, dodecyl
- examples include butyl ether monomers such as vinyl ether; (meth) aryl compounds such as allyl acetate, methallyl acetate, allyl chloride, methallyl chloride; butyl silyl compounds such as butyltrimethoxysilane; burpyridine, N-vinyl pyrrolidone . These can be used alone or in combination of two or more.
- ethylenically unsaturated-tolyl monomers aromatic vinyl monomers and ethylenically unsaturated carboxylic acid alkyl ester monomers are preferred, and ethylenically unsaturated-tolyl monomers.
- a monomer can be used more preferably. In terms of obtaining a dip-molded product with superior tensile strength, aromatic vinyl monomers and ethylenically unsaturated-tolyl monomers are preferred, and in addition, dip-molded products with excellent oil resistance can be obtained. More preferably, ethylenically unsaturated-tolyl monomer can be used.
- the amount of the other monomer used is preferably 0 to 69.5% by weight, more preferably 7 to 49% by weight, and particularly preferably 11 to 43% by weight based on the total monomers. It is. Within this amount range, the tensile strength, oil resistance and texture can be maintained well.
- Examples of the monomer addition method include, for example, a method in which the monomers used in the reaction vessel are added all at once, a method in which the monomers are added continuously or intermittently as the polymerization progresses, and one monomer. Examples include a method in which a part is added to react to a specific conversion rate, and then the remaining monomer is added continuously or intermittently for polymerization, and any method may be adopted.
- the composition of the mixture may be constant or may vary.
- each monomer is added to the reaction vessel after mixing various monomers to be used in advance. Alternatively, it may be added separately to the reaction vessel.
- polymerization auxiliary materials such as an emulsifier, a polymerization initiator, and a molecular weight modifier can be used.
- the method for adding these polymerization auxiliary materials is not particularly limited, and any method such as an initial batch addition method, a divided addition method, or a continuous addition method can be employed.
- the emulsifier is not particularly limited, and examples thereof include alkylbenzene sulfonates, aliphatic sulfonates, sulfates of higher alcohols, OC-olefin sulfonates, and alkyl ether sulfates.
- Nonionic surfactants such as polyethylene glycol alkyl ethers, polyethylene glycol alkyl esters, polyethylene glycol alkylphenol ethers; alkyl diamine salts
- Cationic surfactants such as tetraalkyl ammonium salts; carbonates, sulfates, sulfonates, phosphates or phosphates as amine moieties and amines as cationic moieties
- Examples include amphoteric surfactants having a salt or a quaternary ammonium salt. Of these, a ionic surfactant can be preferably used.
- the amount of the emulsifier used is preferably 0.5 to: L0 parts by weight, more preferably 1 to 8 parts by weight with respect to 100 parts by weight of the total monomers.
- the polymerization initiator is not particularly limited as long as it is a radical initiator, and examples thereof include sodium persulfate, potassium persulfate, ammonium persulfate, potassium perphosphate, and hydrogen peroxide.
- Inorganic peroxides t-butyl peroxide, tamenoxide mouth peroxide, p-menthane hydride peroxide, di-t-butyl peroxide, t-butyl tamil baroxide, acetyl-peroxide, isobutyryl peroxide , Organic peroxides such as otatanyl baroxide, dibenzoyl peroxide, 3, 5, 5-trimethylhexanoyl peroxide, t-butylperoxyisobutyrate; azobisisobutyrate-tolyl, azobis 2, 4 Diazoles such as dimethylvaleronitrile, azobiscyclohexanecarbonitryl, methyl azobis
- polymerization initiators can be used alone or in combination of two or more.
- Peroxides can also be used as redox polymerization initiators in combination with reducing agents such as sodium bisulfite and ferrous sulfate.
- reducing agents such as sodium bisulfite and ferrous sulfate.
- inorganic or organic peroxides are preferred.
- Persulfates which are more preferred for inorganic peracids, are particularly preferred.
- the amount of the polymerization initiator used is preferably 0.01 to 2 parts by weight, more preferably 0.05 to 5 parts by weight with respect to 100 parts by weight of all monomers.
- the molecular weight modifier is not particularly limited, and examples thereof include ⁇ -methylstyrene dimer; mercaptans such as t-dodecyl mercaptan, n-dodecyl mercaptan, octyl mercaptan; tetrasalt carbon, methylene chloride, bromide Halogenated hydrocarbons such as methylene; sulfur-containing compounds such as tetraethylthiuramdiasulfide, dipentamethylenethiuramsulfide, diisopropylxanthogen disulfide and the like. These can be used alone or in combination of two or more. Of these, mercabtans are preferable, and t-dodecyl mercabtan can be more preferably used.
- the amount of the molecular weight modifier used varies depending on the type, but is preferably 0.1 to 0.8 parts by weight, more preferably 0.2 to 0.7 parts by weight with respect to 100 parts by weight of the total monomers. Range.
- Emulsion polymerization is usually carried out in water.
- the amount of water used is preferably 80 to 500 parts by weight, more preferably 100 to 200 parts by weight with respect to 100 parts by weight of the total monomers.
- polymerization auxiliary materials such as a chelating agent, a dispersing agent, a pH adjuster, a deoxygenating agent, and a particle size adjusting agent can be used, and these are not particularly limited in terms of type and amount used.
- the polymerization temperature is not particularly limited, but is usually 0 to 95 ° C, preferably 5 to 70 ° C.
- the unreacted monomer is removed if desired, and the conjugated gen rubber latex is obtained by adjusting the solid content concentration and PH .
- An anti-aging agent an antiseptic, an antibacterial agent, an ultraviolet absorber, a pH adjuster, and the like may be appropriately added to the conjugated rubber rubber latex used in the composition of the present invention as necessary.
- the organic peroxide used in the composition of the present invention is a compound that contains —OO— in the molecular structure and generates free radicals upon heating at least at 100 ° C., and at atmospheric pressure, 30 It must be solid at ° C.
- Examples of compounds that contain -OO- in the molecular structure and generate free radicals when heated to at least 100 ° C include 1, 1-bis (t-hexyloxy) for peroxyketals 3, 3, 5-trimethylcyclohexane, 1,1-bis (t-hexyloxy) cyclohexane, 1,1-bis (t-butylperoxy) 3,3,5-trimethylcyclohexane, 1,1-bis ( t-Butylperoxy) cyclohexane, 1,1-bis (t-butylperoxy) cyclododecane, 2,2-bis (4,4-di-butylperoxycyclohexyl) propane, etc .; a, a'-bis (t-butylperoxy-m-isopropyl) benzene, dicumyl peroxide, 2,5-dimethyl-2,5-bis (t-butylperoxy) hexane, t-butyltamyl peroxid
- disilver oxides diisobutyryl peroxide, di-2,4-dichlorobenzoyl peroxide, di-3,5,5-trimethylhexanoyl peroxide, diocta noyl peroxide, dilauroyl Peroxide, distearoyl peroxide, dissuccinic acid peroxide, di-m-toluoyl peroxide, dibenzoyl peroxide, etc .; for peroxydicarbonates, di-n-propylperoxydicarbonate, di-isopropylperoxide Oxydicarbonate, bis- (4-t-butylcyclohexyl) peroxydicarbonate, di-2-ethoxyethylbaxy oxydicarbonate, di-2-ethylhexyloxydicarbonate, di-2-methoxy Butyl peroxide dicarbonate, di (3-methyl-3-methoxy Chill) Par O
- the organic acid oxide used in the composition of the present invention is a solid property at normal pressure and 30 ° C.
- the 10-hour half-life temperature of the organic peroxide is preferably 120 ° C or lower, more preferably 100 ° C or lower.
- Examples of strong organic peroxides include dibenzoyl peroxide, benzoyl (3-methylbenzoyl) peroxide, di (4 methylbenzol) peroxide, dilauroyl peroxide, distearoyl peroxide, G- ⁇ Tamil peroxide 1, 1 bis (t-butylperoxy) cyclododecane, succinic acid peroxide, bis (4-tert-butylcyclohexyl) peroxydicarbonate, t-butylperoxymaleic acid, and the like.
- the organic peroxides can be used alone or in combination of two or more.
- dibenzoyl peroxide and dilauroyl peroxide can be preferably used in terms of excellent physical property balance of the obtained dip-molded product.
- the organic peroxide can be used in the form of powder or in the form of an organic solvent solution having a concentration of 1 to 60% by weight.
- the average particle size of the powder is 50% by weight equivalent to the cumulative particle size distribution by analysis using a JIS standard sieve, preferably 0.01 to 200 / ⁇ ⁇ , more preferably 0.1 to 150 111, particularly preferably 0.1 to: LOO / zm. If the average particle size force S of the organic peroxide is too small, it tends to float on the latex surface, and conversely, if it is too large, it tends to precipitate.
- the organic solvent for dissolving the organic peroxide is not particularly limited as long as it can dissolve the organic peroxide.
- the organic peroxide when the organic peroxide is dissolved in the organic solvent, the organic peroxide can be heated if it is within a range in which decomposition of the organic peroxide does not occur rapidly.
- the concentration at which the organic peroxide is dissolved in the organic solvent is not particularly limited, but is usually preferably 5 to 60% by weight, more preferably 8 to 50% by weight. If this concentration is too low, it is difficult to remove the organic solvent from the obtained dip-molded product, and it tends to remain in the molded product in a large amount and lower the tensile strength. On the other hand, it is difficult to prepare a solution having a concentration that is too high.
- the content of the organic peroxide in the composition of the present invention is preferably 0.01 to 5 parts by weight, more preferably 0.05 with respect to 100 parts by weight of the solid content of the conjugated gum rubber latex. -3 parts by weight, particularly preferably 0.1-2 parts by weight. If the content of the organic peroxide is too small, the molded article tends to have low bending fatigue resistance. Conversely, if the content is too large, the texture and tensile strength tend to be inferior.
- the surfactant used in the composition of the present invention is a general surfactant such as a cationic surfactant, a nonionic surfactant, a cationic surfactant or an amphoteric surfactant. Not limited!
- polyethylene glycol alkyl ether sulfate polyethylene glycol alcohol
- Key-on surfactants such as kill ether acetate, monoalkyl phosphate, naphthalene sulfonate formalin condensate
- polyethylene glycol polyethylene glycol
- examples include non-ionic surfactants such as difatty acid esters, glycerin fatty acid esters, sorbitan alkyl esters, polyhydric alcohol alkyl esters, polyethylene glycol sorbitan alkyl esters, polyoxyethylene sorbitol fatty acid esters, among others.
- Anionic surfactants and nonionic surfactants are preferred.
- ionic surfactants polyethylene glycol alkyl ether sulfate and naphthalene sulfonate formalin condensate.
- ionic surfactants polyethylene glycol sorbitan alkyl esters. And polyethylene glycol alkyl ethers are more preferred.
- the content of the surfactant in the composition of the present invention is preferably 0.05 to 20 parts by weight, more preferably 0.1 to L0 based on 100 parts by weight of the solid content of the organic peroxide. Part by weight, particularly preferably 0.2 to 5 parts by weight. If the content of the surfactant is too small, the dispersion stability of the organic peroxide tends to decrease and tends to settle, and conversely, if the content is too large, the physical properties of the dip-molded product tend to decrease. There is.
- the polymer protective colloid used in the composition of the present invention is not limited as long as it is a high molecular weight dispersion stabilizer having a molecular weight of 10,000 or more.
- strong polymer protective colloids include gelatin; polyvinyl alcohol; fibrin derivatives such as methyl cellulose, hydroxyalkyl cellulose, hydroxypropoxymethyl cellulose, carboxymethyl cellulose, and microcrystalline cellulose. These polymer protective colloids can be used alone or in combination of two or more. Of these, microcrystalline cellulose, which is preferably microcrystalline cellulose, hydroxyalkyl cellulose, and polybulal alcohol, can be used more preferably.
- the microcrystalline cellulose has a crystallinity of preferably 90% or more, more preferably 95% or more, and an average particle size of preferably 20 ⁇ m or less, more preferably 10 ⁇ m or less.
- Hydroxyalkyl cellulose is preferably an alkyl group or a cetyl group.
- the average molecular weight is preferably 10,000 to 5,000,000, more preferably ⁇ 20,000 to 3,000,000, particularly preferably ⁇ 50,000 to 2,000,000.
- the poly Bulle alcohol ⁇ degree preferably 60 to 99%, more preferably 70-9 9%, particularly preferably ⁇ or 80 to 99 0/0, average molecular weight force S preferably ⁇ or 10, 000 500, 00 0, more preferred ⁇ is 20,000-300,000.
- the content of the polymer protective colloid in the composition of the present invention is preferably 0.1 to 20 parts by weight, more preferably 0.5 to 15 parts by weight with respect to 100 parts by weight of the organic peroxide. Particularly preferred is 1 to 10 parts by weight. If the content of the polymer protective colloid is too small, the dispersion stability of the organic peroxide tends to decrease and tends to settle. Conversely, if it is too large, the physical properties of the molded product tend to decrease. .
- the composition of the present invention may contain a quaternary ammonium salt having a hydrocarbon group containing a carbon-carbon unsaturated bond.
- the quaternary ammonium salt having a carbon-carbon unsaturated bond-containing hydrocarbon group used in the composition of the present invention has a chemical structure represented by the following formula (1).
- R 1 and IT are hydrocarbon groups having 2 to 8 carbon atoms which may contain a substituent, and at least one of them has one or more carbon-carbon unsaturated bonds.
- R 3 and R 4 are , A hydrogen atom or a saturated hydrocarbon group having 1 to 4 carbon atoms, X is a halogen atom.
- the hydrocarbon group containing a carbon-carbon unsaturated bond carbon-carbon unsaturated bond-containing hydrocarbon group
- both of R 1 and R 2 are preferably aryl groups. More specifically, as the quaternary ammonium salt having a carbon-carbon unsaturated bond-containing hydrocarbon group used in the composition of the present invention, a diallyl dialkyl ammonium salt is most preferable.
- quaternary ammonium salt in the composition of the present invention.
- Content is 100 weights of solid content of the conjugated rubber rubber latex.
- the amount is preferably 0.1 to: part by weight of LO, more preferably 0.2 to 7 parts by weight, and particularly preferably 0.5 to 5 parts by weight. If the content of the quaternary ammonium salt (1) is too small, the dispersion stability of the organic peroxide is lowered and the sedimentation tends to settle, and the tensile strength and resistance of the resulting dip-formed product are reduced. Flexural fatigue may be reduced, and conversely if too much, the stability of the lattice may be reduced.
- a quaternary ammonium salt having a hydrocarbon group containing a carbon-carbon unsaturated bond, an organic peroxide, a surfactant, and Z or a polymer protective colloid are mixed in a conjugated gen rubber latex.
- a dip-molded product is obtained by using a dip-molding composition, it contains the above-described molecular structure of 0-0- as an organic oxide, and generates free radicals by heating at least 100 ° C. If the compound to be used is used, the same effect as the present application is achieved.
- composition of the present invention is prepared by preparing a dispersion in which an organic peroxide is dispersed in an aqueous medium in the presence of a surfactant and a water-soluble polymer, and then adding the dispersion to a conjugated rubber rubber latex. And mix.
- the dispersion is preferably added to a conjugated gen rubber latex placed in a stirred state.
- an aqueous quaternary ammonium salt solution is added to the conjugated rubber rubber latex.
- a quaternary ammonium salt-added latex was prepared by mixing, and an organic peroxide was separately dispersed in an aqueous medium using a surfactant and Z or a polymer protective colloid to separate the organic peroxide. It is preferable to prepare a substance dispersion water and add the organic peroxide dispersion water to the quaternary ammonium salt-added latus status and mix.
- the method for preparing the aqueous dispersion of the organic peroxide is not particularly limited.
- the powdered organic peroxide is a surfactant and Z or a polymer protective colloid.
- the solution dissolved in the solution is added to an aqueous medium in which the surfactant and Z or polymer protective colloid are dissolved, and the mixture is vigorously stirred to precipitate an organic peroxy acid compound from the organic solvent phase to the aqueous medium.
- Disperse and finally disperse the organic peroxide with both surfactant and polymer protective colloid There are a method of stabilizing, (3) a method of dispersing an organic peroxide in an aqueous medium by a method of distilling off the organic solvent following (2), and the like.
- a homomixer, a stirring homogenizer, and the like are preferable.
- the concentration of the organic peroxide aqueous dispersion is preferably 1 to 50% by weight, more preferably 2 to 45% by weight, and particularly preferably 5 to 40%. If the concentration is too low, it may be uneconomical and the amount of handling work may be large. On the other hand, if the concentration is too high, the fluidity of the dispersion may be lowered and the operability may be deteriorated.
- the pH of the conjugated gen rubber latex is 8.5 or more in order to prevent the formation of coarse aggregates. I like it.
- the composition for dip molding of the present invention contains the above-mentioned organic peroxide as a cross-linking agent for conjugated rubber, sulfur and Z or vulcanization usually used in the composition is included.
- an accelerator for example, zinc dibutyldithiocarbamate, 2-mercaptobenzobenzothiazol, etc.
- the amount of sulfur in the case where sulfur is added in addition to the organic peroxide is 0.5 parts by weight or less with respect to 100 parts by weight of the solid content of the conjugated gen rubber latex. More preferably, it is 3 parts by weight or less.
- the blending amount of the vulcanization accelerator may be 0.3 parts by weight or less with respect to 100 parts by weight of the solid content of the conjugate rubber rubber. Preferred 0.1% by weight or less is more preferred. Considering the balance of physical properties of dip-molded products, it is most preferable not to add sulfur and vulcanization accelerators.
- the carboxyl group is ionically cross-linked so that the effect of the present invention is not substantially inhibited.
- Zinc can be blended.
- the blending amount of zinc oxide is preferably 2 parts by weight or less, more preferably 1 part by weight or less, with respect to 100 parts by weight of the solid content of the conjugated yarn rubber latex. It is particularly preferable that the amount is not more than parts.
- an inorganic pigment inorganic pigment, a colorant, a dispersant, a PH adjuster, a wetting agent, an antiseptic, an antibacterial agent, a wax, a sizing agent, etc.
- Attachment Additives can be included as appropriate.
- the optional composition such as sulfur, vulcanization accelerator, zinc oxide, additive and the like is blended with the composition of the present invention
- all or a part of the pH adjuster is preliminarily added to the conjugated rubber rubber latex.
- the others are preferably added after mixing the organic peroxide, surfactant, and polymer protective colloid with the conjugated rubber rubber latex.
- the solid concentration of the composition of the present invention is preferably 20 to 40% by weight, more preferably 25 to 35% by weight.
- the pH of the composition of the present invention is preferably 8.5 or more, more preferably in the range of 9 to L 1.
- composition of the present invention having a solid content concentration or pH in the above range is used, a dip-formed product having a uniform film thickness is easily produced.
- the composition of the present invention needs to be aged after the conjugated gen rubber latex is mixed with the above-mentioned organic peroxide dispersion and optional components blended as necessary.
- the maturation condition is that the temperature is preferably 10 to 50 ° C, more preferably 15 to 45 ° C, particularly preferably 20 to 30 ° C, preferably 1 hour or more, more preferably 1 hour to 2 weeks. Particularly preferred is stirring for 1 hour to 1 week.
- the time is selected from the above range in consideration of the temperature. When aging is insufficient, the conjugated rubber rubber force organic peroxide tends to separate and settle.
- the dip-molded product of the present invention is attached to the surface after the dip-molding mold and the object to be coated (hereinafter represented by the dip-molding mold) are dipped in the dip-molding composition of the present invention and pulled up. It can be obtained by performing a dip molding method in which the dip molded layer is heated to form a film.
- a conventionally known dip forming method can be adopted, and examples thereof include a direct dipping method, an anode adhesion dipping method, and a teag adhesion dipping method.
- the anode coagulation dipping method is preferable because a dip-molded product having a uniform thickness is easily obtained.
- the dip mold is immersed in a coagulant solution to adhere the coagulant to the surface of the dip mold, and then the dip mold is used for dip molding.
- a dipping layer is formed on the surface of the dip mold by dipping in the composition.
- the dip mold various materials such as porcelain, glass, metal and plastic can be used.
- the shape of the mold should match the shape of the final dip molded product.
- the shape of the dip-molding die can be of various shapes such as a shape from the wrist to the fingertips and a shape from the elbow strength to the fingertips.
- the surface of the dip molding die may be subjected to surface processing such as gloss processing, semi-gloss processing, non-gloss processing, and woven pattern processing, for example, on the entire mold surface or partially.
- a salting-out agent for example, a halogenated metal such as barium chloride, salted calcium, salted magnesium, zinc chloride, salted aluminum; barium nitrate, calcium nitrate, Examples thereof include nitrates such as zinc nitrate; acetates such as barium acetate, calcium acetate, and zinc acetate; sulfates such as calcium sulfate, magnesium sulfate, and aluminum sulfate. Of these, calcium chloride and calcium nitrate are preferred.
- the coagulant is usually used by dissolving in water, alcohol or a mixture thereof.
- the coagulant concentration is preferably 5 to 70% by weight, more preferably 10 to 50% by weight.
- Di Tsu Bruno purposes cissing preventing flop mold strength coagulant -..
- the on surfactant 0.001 to 1 0 weight 0/0, more preferably 0.01 to 0 concentration of 5 wt% You may add it so that
- the obtained dip-molded layer is heated to proceed to a crosslinking step of crosslinking the conjugated rubber, and before that, it is performed in water, preferably 20 to 80 ° C in warm water for 0.5 to 60 minutes. It may be soaked to a certain extent and subjected to a leaching process for removing water-soluble impurities (emulsifier, water-soluble polymer, coagulant, etc.). This operation may be performed after heat-treating the dip-formed layer, but it is preferable to perform it before the heat-treatment because it can remove water-soluble impurities more efficiently! /. In addition, when the dip-molded layer contains a large amount of moisture, a drying step at 40 to 100 ° C. for 1 to 60 minutes can be added before the crosslinking step.
- a drying step at 40 to 100 ° C. for 1 to 60 minutes can be added before the crosslinking step.
- the temperature of the heat treatment of the dip-formed layer is preferably 60 to 160 ° C, more preferably 80 to 150 ° C. If this temperature is too low, the cross-linking reaction takes a long time and the productivity may be reduced. Conversely, if it is too high, the oxidative degradation of the conjugated rubber is promoted. The physical properties of the product may be reduced.
- the time for the heat treatment conditions is selected in relation to the heat treatment temperature, but is generally 5 minutes or more and 2 hours or less.
- heating method external heating using infrared rays or hot air or internal heating using high frequency can be employed. Of these, heating with hot air is preferred.
- a dip-molded product By detaching the crosslinked dip-molded layer from the dip-molding die (if the object to be coated is dip-molded, a dip-molded product is obtained).
- methods such as peeling from the mold by hand or peeling by water pressure or compressed air pressure can be employed.
- a heat treatment may be performed at a temperature of 60 to 120 ° C for 10 to 120 minutes.
- a surface treatment layer by chlorination treatment or coating treatment may be formed on the inside and Z or outside surfaces of the dip-formed product.
- the dip-molded product of the present invention preferably has a thickness of about 0.05 to about 3 mm, more preferably 0.
- a thin film of 05 to 0.3 mm can be realized, the texture is good, the tensile strength and the bending fatigue resistance are excellent, and the strength is not easily colored.
- dip-molded article of the present invention include medical supplies such as nipples for baby bottles, syringes, conduits, and water pillows; toys and exercise tools such as balloons, dolls, balls, etc .; pressure forming bags, gas storage bags Industrial articles such as; surgical, household, agricultural, fishery and industrial gloves; finger sack; and the like. In the case of gloves, it may be a support type or an unsupport type. Among the above, thin surgical gloves are a good example.
- the present invention is not limited to the above-described embodiment.
- the above embodiment is an exemplification, and the present invention has the same configuration as the technical idea described in the scope of claims of the present invention, and any device that exhibits the same function and effect is the present embodiment. It is included in the technical scope of the invention.
- a quaternary ammonium salt having a hydrocarbon group containing a carbon-carbon unsaturated bond, an organic peroxide, a surfactant, and Z or a polymer protective colloid are mixed in a conjugated rubber rubber latex.
- a dip molding composition is also included.
- the obtained rubber glove strength sample is precisely weighed out to approximately 5 mm square. This is placed in an 80 mesh JIS standard sieve and immersed in 80 ml of methyl ethyl ketone (MEK) for 24 hours. Remove the sieve with MEK force, air dry for 1 hour and then dry at 105 ° C for 1 hour. The whole sieve was weighed again, and the weight (% by weight) of the gel held on the sieve was determined as the gel content. Next, the rate of increase was determined by comparing this value with this value in Comparative Example 1 (in the case where no organic peroxide was added).
- MEK methyl ethyl ketone
- a dumbbell-shaped test piece was produced from the obtained rubber gloves using dumbbell deformation No. 2 (small).
- the specimen was pulled at a tensile speed of 500 mmZ, and the tensile stress (MPa) when the elongation was 300%, the tensile strength at break (MPa), and the elongation at break (%) were measured.
- the obtained rubber gloves were immersed in a 3% aqueous solution of copper sulfate for 30 seconds, and the degree of color change of the rubber gloves after 1 hour was visually determined. Rubber gloves that show discoloration in the above test are judged to be easily colored when worn over a long period of time.
- the resulting copolymer latex power After removing unreacted monomers, the pH and solid content of the latex were adjusted to give a conjugated gen rubber latex A (carboxy-modified NBR latex) with a solid content of 40% by weight and pH 8. Got.
- the resulting copolymer latex power After removing unreacted monomers, the pH and solid content of the latex are adjusted, and the conjugated gen rubber latex B (carboxy-modified SBR latex) with a solid content of 40 wt% and pH 8 is used. Got.
- the glove mold was immersed for 5 seconds in a coagulant solution mixed with 20 parts of calcium nitrate, 0.05 part of polyethylene glycol octal ether and 80 parts of water, pulled up, and then dried at 50 ° C for 10 minutes. Then, a coagulant was attached to the glove mold. Next, the glove mold to which the coagulant is attached is immersed in the above dip molding composition for 6 seconds, pulled up and dried at 50 ° C for 10 minutes, and then immersed in warm water at 40 ° C for 3 minutes to dissolve in water. Sex impurities were eluted.
- the glove mold was then dried at 70 ° C. for 10 minutes, followed by heat treatment at 120 ° C. for 20 minutes to crosslink the dip-formed layer.
- the dip-molded layer cross-linked with heel was peeled off from the glove mold to obtain a rubber glove having a thickness of 0.1 mm.
- Table 1 shows the results of testing and evaluation of rubber gloves.
- Example 1 except that the amount of dibenzoyl peroxide added to conjugated gen rubber latex A was changed to 1 part (converted to pure content) with respect to 100 parts of latex solids in Example 1. In the same manner, rubber gloves were obtained. Table 1 shows the results of testing and evaluation of rubber gloves.
- Example 2 rubber gloves were obtained in the same manner as in Example 2 except that the pure amount of dilauroyl peroxide was used instead of dibenzoyl peroxide. Table 1 shows the results of testing and evaluation of rubber gloves.
- Example 1 rubber gloves were obtained in the same manner as in Example 1 except that conjugated gen rubber latex B was used instead of conjugated gen rubber latex A. Table 1 shows the results of testing and evaluation of rubber gloves.
- Example 1 rubber gloves were obtained in the same manner as in Example 1 except that conjugated gen rubber latex C was used instead of conjugated gen rubber latex A. Table 1 shows the results of testing and evaluation of rubber gloves.
- Example 2 Rubber gloves were obtained in the same manner as in Example 1 except that instead of dibenzoyl peroxide, potassium persulfate having a pure weight part was used. Table 1 shows the results of rubber glove testing and evaluation. [0081] (Comparative Example 2)
- Example 1 when preparing the dispersion of dibenzoyl peroxide, microcrystalline cellulose was not used, but a polyethylene glycol alkyl ether (Emulgen 105, manufactured by Kao Corporation) in an amount by weight was added. An organic peroxide dispersion that settled immediately after the stirring was stopped and was stable for a long time was not obtained. Therefore, the dip molding experiment was canceled.
- a polyethylene glycol alkyl ether (Emulgen 105, manufactured by Kao Corporation) in an amount by weight was added.
- An organic peroxide dispersion that settled immediately after the stirring was stopped and was stable for a long time was not obtained. Therefore, the dip molding experiment was canceled.
- Example 1 when preparing a dispersion of dibenzoyl peroxide, a polyethylene glycol alkyl ether was not used, but a part by weight of microcrystalline cellulose was added. A long-term stable organic peroxide dispersion could not be obtained. Therefore, the dip molding experiment was canceled.
- Example 1 a rubber glove was obtained in the same manner as in Example 1 except that the composition for dip molding was not aged and was subjected to dip forming after stirring for 0.5 hour. Table 1 shows the results of testing and evaluation of rubber gloves.
- Composition crosslinking agent amount (parts) 0.5 1 1 0.5 0.5 0.5 0.5 0.5 0.5 0.5 1 1
- the dip-molded products obtained by dip-molding using the composition of the present invention all have tensile strength, elongation, and resistance to bending that increase the degree of crosslinking and increase the gel increase rate. Since it is excellent in bending fatigue, it is judged that the texture is good, and since there is no discoloration due to copper ions, it is judged that coloring does not easily occur even after wearing for a long time (Example 15).
- composition for dip molding is used without aging, precipitation of microcrystals of organic peroxide occurs, so the degree of cross-linking decreases and the gel increase rate decreases, and the resulting dip-molded product is resistant to bending fatigue. It was inferior (Comparative Example 5).
- sulfur and its vulcanization accelerator are used as a crosslinking agent for conjugated gen rubber, the resulting dip-molded product is judged to be inferior in texture because of its high tensile stress and low elongation, and it is discolored by copper ions. It was judged that the color changed over time (Comparative Example 6)
- Diallyldimethylammonium chloride (New Frontier C-1615, manufactured by Daiichi Kogyo Seiyaku Co., Ltd.) represented by the following formula (2) is added to a solid content of 100 parts of conjugated Gen rubber latex A Diaryldimethylammonium chloride was added at a ratio of 1 part and mixed uniformly.
- the glove mold to which the coagulant is adhered is immersed in the above dip molding composition for 6 seconds, pulled up and dried at 50 ° C for 10 minutes, and then immersed in warm water at 40 ° C for 3 minutes. Thus, water-soluble impurities were eluted.
- the glove mold was dried at 70 ° C. for 10 minutes, and subsequently heat-treated at 120 ° C. for 20 minutes to crosslink the dip-formed layer.
- the dip-molded layer cross-linked with the armpit was peeled off from the glove mold to obtain a rubber glove having a thickness of 0.1 mm.
- Table 2 shows the results of testing and evaluation of rubber gloves.
- Example 6 rubber gloves were obtained in the same manner as in Example 6 except that instead of dibenzoyl peroxide, the pure weight of dilauxyl peroxide was used. Table 2 shows the results of testing and evaluation of rubber bags.
- Example 6 rubber gloves were obtained in the same manner as in Example 6 except that conjugated gen rubber latex B was used instead of conjugated gen rubber latex A. Table 2 shows the results of testing and evaluation of rubber gloves.
- Example 6 rubber gloves were obtained in the same manner as in Example 6 except that conjugated gen rubber latex C was used instead of conjugated gen rubber latex A. Table 2 shows the results of testing and evaluation of rubber gloves.
- Example 6 instead of diallyldimethylammonium chloride, cetyltrimethyl was used.
- a rubber glove was obtained in the same manner as in Example 6 except that Ruammo-um chloride (Cotamin 60W, manufactured by Kao Corporation, the following formula (3)) was used. Table 2 shows the results of testing and evaluation of rubber gloves.
- a rubber glove was obtained in the same manner as in Example 6 except that 1 part of sodium lauryl sulfate was used instead of 1 part of diallyldimethylammonium chloride. Table 2 shows the results of testing and evaluation of rubber gloves.
- Example 6 the same procedure as in Example 6 was carried out except that a dibenzoyl peroxide dispersion was not added to the conjugated gem latex A supplemented with diallyldimethylammonium chloride. Rubber gloves were obtained. Table 2 shows the results of testing and evaluation of rubber gloves.
- Example 6 a rubber glove was obtained in the same manner as in Example 6 except that the above composition was used as the dip molding composition. Table 2 shows the results of testing and evaluation of rubber gloves.
- the dip-molded product obtained by dip molding using the composition of the present invention using a salt of salt has a small surface electrical resistance value for V and deviation (Examples 6 to 9).
- the dip-molded products obtained by dip molding using the composition of the present invention all show an increase in gel, the tensile strength and elongation are sufficiently large, and the 300% tensile stress is sufficiently small. Judged to be good. Furthermore, since there is no discoloration due to copper ions, it is judged that coloring does not easily occur even after a long wearing operation (Examples 6 to 11).
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Abstract
Description
Claims
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
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US11/791,662 US20080051498A1 (en) | 2004-11-29 | 2005-11-28 | Dip-Forming Composition and Dip-Formed Article |
EP05809522A EP1826236A4 (en) | 2004-11-29 | 2005-11-28 | COMPOSITION FOR DIVE FORM AND FORM BODY RECEIVED BY DIVE FORMS |
JP2006547918A JP4840143B2 (ja) | 2004-11-29 | 2005-11-28 | ディップ成形用組成物及びディップ成形品 |
US12/504,442 US20090278284A1 (en) | 2004-11-29 | 2009-07-16 | Process for making a dip-forming composition and a dip-formed article |
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JP2004344877 | 2004-11-29 | ||
JP2004-344877 | 2004-11-29 | ||
JP2004-347831 | 2004-11-30 | ||
JP2004347831 | 2004-11-30 |
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US12/504,442 Division US20090278284A1 (en) | 2004-11-29 | 2009-07-16 | Process for making a dip-forming composition and a dip-formed article |
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WO2006057392A1 true WO2006057392A1 (ja) | 2006-06-01 |
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PCT/JP2005/021825 WO2006057392A1 (ja) | 2004-11-29 | 2005-11-28 | ディップ成形用組成物及びディップ成形品 |
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US (2) | US20080051498A1 (ja) |
EP (1) | EP1826236A4 (ja) |
JP (1) | JP4840143B2 (ja) |
WO (1) | WO2006057392A1 (ja) |
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Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH09124847A (ja) * | 1995-10-31 | 1997-05-13 | Nippon Zeon Co Ltd | ニトリル基含有高飽和共重合体ゴムとエチレン−α−オレフイン系共重合体ゴムとからなるゴム組成物 |
JPH1095963A (ja) * | 1997-09-25 | 1998-04-14 | Mitsuboshi Belting Ltd | 繊維材料に加硫接着良好なゴム接着剤と接着方法 |
JP2003165870A (ja) * | 2001-11-28 | 2003-06-10 | Nippon Zeon Co Ltd | ディップ成形用組成物、ディップ成形品およびその製造方法 |
JP2003252935A (ja) * | 2002-02-28 | 2003-09-10 | Nippon Zeon Co Ltd | ディップ成形用ラテックス、ディップ成形用組成物およびディップ成形物 |
JP2003530255A (ja) * | 2000-04-11 | 2003-10-14 | アペックス メディカル テクノロジーズ、インコーポレイテッド | 溶融媒体浴を用いるディップ成形ゴム物品の硫化 |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3696169A (en) * | 1970-10-16 | 1972-10-03 | Dart Ind Inc | Modified polyolefin containing reaction product of unsaturated oxirane in the presence of the polyolefin and peroxide |
JPS5968303A (ja) * | 1982-10-12 | 1984-04-18 | Nippon Oil & Fats Co Ltd | 固体の有機過酸化物の水性懸濁液の製造方法 |
US5014362A (en) * | 1990-05-11 | 1991-05-14 | Tillotson Corporation | Elastomeric covering material and hand glove made therewith |
US6878766B2 (en) * | 2000-01-24 | 2005-04-12 | Zeon Corporation | Composition for dip forming, dip-formed object, and process for producing the same |
US6870019B2 (en) * | 2000-12-12 | 2005-03-22 | Nippon A & L Inc. | Latex for dip molding and a dip molded product |
EP1478672B1 (en) * | 2002-02-28 | 2015-03-25 | Zeon Corporation | Dip-forming latex, dip-forming composition and dip-formed article |
WO2004069902A1 (ja) * | 2003-02-05 | 2004-08-19 | Zeon Corporation | 低表面抵抗率のディップ成形品 |
EP1634894A1 (en) * | 2004-09-09 | 2006-03-15 | PolymerLatex GmbH | Polymer latex suitable for the preparation of dip-molded articles |
-
2005
- 2005-11-28 WO PCT/JP2005/021825 patent/WO2006057392A1/ja active Application Filing
- 2005-11-28 JP JP2006547918A patent/JP4840143B2/ja not_active Expired - Fee Related
- 2005-11-28 US US11/791,662 patent/US20080051498A1/en not_active Abandoned
- 2005-11-28 EP EP05809522A patent/EP1826236A4/en not_active Withdrawn
-
2009
- 2009-07-16 US US12/504,442 patent/US20090278284A1/en not_active Abandoned
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH09124847A (ja) * | 1995-10-31 | 1997-05-13 | Nippon Zeon Co Ltd | ニトリル基含有高飽和共重合体ゴムとエチレン−α−オレフイン系共重合体ゴムとからなるゴム組成物 |
JPH1095963A (ja) * | 1997-09-25 | 1998-04-14 | Mitsuboshi Belting Ltd | 繊維材料に加硫接着良好なゴム接着剤と接着方法 |
JP2003530255A (ja) * | 2000-04-11 | 2003-10-14 | アペックス メディカル テクノロジーズ、インコーポレイテッド | 溶融媒体浴を用いるディップ成形ゴム物品の硫化 |
JP2003165870A (ja) * | 2001-11-28 | 2003-06-10 | Nippon Zeon Co Ltd | ディップ成形用組成物、ディップ成形品およびその製造方法 |
JP2003252935A (ja) * | 2002-02-28 | 2003-09-10 | Nippon Zeon Co Ltd | ディップ成形用ラテックス、ディップ成形用組成物およびディップ成形物 |
Non-Patent Citations (1)
Title |
---|
See also references of EP1826236A4 * |
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JP2010059441A (ja) * | 2006-06-30 | 2010-03-18 | Four Road Research Ltd | 架橋剤を含むラテックス組成物およびその架橋成形体 |
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JPWO2013099501A1 (ja) * | 2011-12-27 | 2015-04-30 | 日本ゼオン株式会社 | ラテックス、ディップ成形用組成物およびディップ成形体 |
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JP2017171764A (ja) * | 2016-03-23 | 2017-09-28 | 日本ゼオン株式会社 | ラテックス組成物 |
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JP2019014864A (ja) * | 2016-12-28 | 2019-01-31 | 旭化成株式会社 | セルロースを含む樹脂組成物 |
US11390728B2 (en) | 2016-12-28 | 2022-07-19 | Asahi Kasei Kabushiki Kaisha | Cellulose-containing resin composition and cellulosic ingredient |
WO2019058807A1 (ja) * | 2017-09-22 | 2019-03-28 | 日本ゼオン株式会社 | ラテックス組成物の製造方法 |
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JP2019195623A (ja) * | 2018-05-08 | 2019-11-14 | ウユン ソン | 液体内で模型金型を用いて玩具を製造する方法、及びその方法を実現するための装置 |
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EP1826236A1 (en) | 2007-08-29 |
US20080051498A1 (en) | 2008-02-28 |
JP4840143B2 (ja) | 2011-12-21 |
US20090278284A1 (en) | 2009-11-12 |
JPWO2006057392A1 (ja) | 2008-06-05 |
EP1826236A4 (en) | 2009-04-22 |
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