WO2005012375A1 - ディップ成形用の共重合体ラテックス - Google Patents
ディップ成形用の共重合体ラテックス Download PDFInfo
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- WO2005012375A1 WO2005012375A1 PCT/JP2004/011194 JP2004011194W WO2005012375A1 WO 2005012375 A1 WO2005012375 A1 WO 2005012375A1 JP 2004011194 W JP2004011194 W JP 2004011194W WO 2005012375 A1 WO2005012375 A1 WO 2005012375A1
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- weight
- monomer
- ethylenically unsaturated
- dip
- parts
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Classifications
-
- 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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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C41/00—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
- B29C41/003—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor characterised by the choice of material
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F236/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds
- C08F236/02—Copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds the radical having only two carbon-to-carbon double bonds
- C08F236/04—Copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds the radical having only two carbon-to-carbon double bonds conjugated
- C08F236/14—Copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds the radical having only two carbon-to-carbon double bonds conjugated containing elements other than carbon and hydrogen
- C08F236/16—Copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds the radical having only two carbon-to-carbon double bonds conjugated containing elements other than carbon and hydrogen containing halogen
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L13/00—Compositions of rubbers containing carboxyl groups
- C08L13/02—Latex
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
- B29K2105/0058—Liquid or visquous
- B29K2105/0064—Latex, emulsion or dispersion
Definitions
- the present invention relates to a copolymer latex for dip molding, a composition for dip molding, and a dip molded product. More specifically, the present invention has excellent organic solvent resistance and texture, has sufficient tensile strength, and has a close contact state.
- the present invention relates to a dip-formed product having excellent durability, a dip-forming composition for providing the dip-formed product, and a dip-forming copolymer latex used in the dip-forming composition.
- Rubber gloves are widely used in various industrial and medical applications (especially for surgery), such as in the household, food and electronic component industries. Rubber gloves should allow the gloves to follow the stretch with less force in accordance with the movement of the fingers (good texture) so that they do not get tired even if they are worn for a long time. It is difficult to be torn (has a sufficiently high tensile strength). Even if the glove is deformed in accordance with the movement of the finger, there is little occurrence of sagging or wrinkling, and it can be kept in close contact. ) Are required.
- U.S. Pat. No. 5,014,362 discloses that a composition comprising a carboxy-modified atarilonitrile trirubutadiene copolymer lattetus, a small amount of zinc oxide, sulfur and a vulcanization accelerator is dip-formed.
- a glove that has a property that the ratio of the stress immediately after the elongation to the stress immediately after the elongation at the time of 100% elongation (stress retention ratio) 6 minutes after the elongation is almost zero.
- such gloves Good texture but poor persistence of adhesion.
- International Publication WO 00/214145 discloses a composition comprising an acrylonitrile-butadiene copolymer latex containing a specific amount of carboxyl group, a small amount of zinc oxide, sulfur and a vulcanization accelerator.
- a glove having a stress retention in the range of 50 to 70% obtained by dip-forming an object is disclosed. While such gloves have good persistence of the adherence, they may have poor texture and tensile strength balance.
- gloves obtained using the carboxy-modified acrylonitrile-butadiene copolymer latex as described above sometimes have insufficient resistance to organic solvents.
- an object of the present invention is to provide a dip molded article having excellent organic solvent resistance and texture, having sufficient tensile strength, and having excellent persistence of an adhered state, and a dip molded article which provides the dip molded article.
- An object of the present invention is to provide a composition and a copolymer latex for dip molding used in the dip molding composition.
- the present inventors have conducted intensive studies to solve the above-mentioned problems, and as a result, when copolymerizing a monomer mixture containing 1,3-butadiene, acrylonitrile, and methacrylic acid, one of acrylic nitriles was obtained.
- Part of methacrylic acid and a part of methacrylic acid are added to the polymerization reaction system after the initiation of polymerization and copolymerized, and a carboxy-modified acrylonitrile-butadiene copolymer consisting of a copolymer having a high content of methyl ethyl ketone insoluble matter
- a copolymer latex for dip molding satisfying the following (1) to (3).
- (1) 45 to 85 parts by weight of a conjugated diene monomer, 10 to 40 parts by weight of an ethylenically unsaturated nitrile monomer, and 5 to 15 parts by weight of an ethylenically unsaturated acid monomer
- (2) copolymerizable ethylenically unsaturated monomers
- Monomer mixture consisting of 0 to 20 parts by weight
- (A) must be obtained by copolymerizing 100 parts by weight
- Methyl ethyl ketone insoluble content of the copolymer is 60 to 95% by weight.
- Step 1 In each component of the monomer mixture (A), at least 80% by weight of the conjugated diene monomer, 50 to 90% by weight of the ethylenically unsaturated nitrile monomer, Copolymerization using a monomer mixture (a) consisting of 40 to 90% by weight of a saturated acid monomer and 80% by weight or more of other ethylenically unsaturated monomers copolymerizable therewith. Steps to start the reaction
- Step 2 The remaining ethylenically unsaturated nitrile monomer and the remaining ethylenically unsaturated acid monomer in the monomer mixture (A) that were not contained in the monomer mixture (a) were A step of adding when the polymerization conversion of the monomer mixture (a) is in the range of 5 to 95% by weight; step 3: the remaining conjugated diene monomer and other ethylene copolymerizable therewith. Of adding unsaturated unsaturated monomer by the time the copolymerization reaction is stopped
- a dip molding composition comprising the copolymer latex for dip molding, a vulcanizing agent and a vulcanization accelerator.
- a dip molded product obtained by dip molding the composition for dip molding.
- a dip-forming latex obtained by copolymerizing 100 parts by weight of a monomer mixture consisting of 0 to 20 parts by weight of other polymerizable ethylenically unsaturated monomers.
- the monomers at least 80% by weight of the conjugated diene monomer, 50 to 90% by weight of the ethylenically unsaturated nitrile monomer, and 40 to 90% of the ethylenically unsaturated acid monomer
- the polymerization is started using a monomer mixture containing 80% by weight or more of the other ethylenically unsaturated monomers copolymerizable with these monomers, and then all the monomers in the polymerization reaction system are started.
- the dip molded article which is excellent in organic solvent resistance and a hand, has sufficient tensile strength, and is excellent in persistence of an adhesion state, a dip molding composition which provides the dip molded article, Further, there is provided a copolymer latex for dip molding which can be suitably used for the dip molding composition.
- the copolymer latex for dip molding of the present invention comprises 45 to 85 parts by weight of a conjugated diene monomer, 10 to 40 parts by weight of an ethylenically unsaturated-tolyl monomer, and a monoethylenically unsaturated acid. Obtained by copolymerizing 100 parts by weight of a monomer mixture consisting of 5 to 15 parts by weight of a monomer and 0 to 20 parts by weight of another ethylenically unsaturated monomer copolymerizable therewith.
- a copolymer latex for dip molding of which at least 80% by weight of a conjugated diene monomer and 50 to 9 of an ethylenically unsaturated nitrile monomer among all monomers used for polymerization.
- Monomer mixture containing 0% by weight, 40 to 90% by weight of an ethylenically unsaturated acid monomer and 80% by weight or more of other ethylenically unsaturated monomers copolymerizable therewith.
- the polymerization is started using, and then the polymerization conversion of all monomers in the polymerization reaction system is in the range of 5 to 95% by weight.
- the remaining ethylenically unsaturated nitrile monomer and the remaining ethylenically unsaturated acid monomer are added to the mixture, and the remaining conjugated dimer is added to another ethylenically unsaturated monomer copolymerizable therewith.
- the addition of the saturated monomer is completed by the time the polymerization reaction is stopped, and the copolymer is copolymerized, and the obtained copolymer has a methylethylketone-insoluble content of 60 to 95% by weight. .
- conjugated diene monomer examples include 1,3-butadiene, isoprene, 2,3-dimethynole-1,3-butadiene, 2-ethyl-1,3-butadiene, 1,3-pentadiene, and chloroprene. . Above all, 1,3 Genoprene isoprene is preferred, and 1,3-butadiene is more preferred.
- These conjugated diene monomers can be used alone or in combination of two or more.
- the amount of the conjugated diene monomer to be used is 45 to 85 parts by weight, preferably 58 to 75 parts by weight, based on 100 parts by weight of all the monomers. If the amount is too small, the texture will be poor, and if it is too large, the tensile strength and the organic solvent resistance will be poor.
- the ethylenically unsaturated nitrile monomers such as acrylonitrile, methacrylonitrile Tarironitoriru, fumaronitrile, alpha - black port acrylonitrile, alpha - like Shianoe chill ⁇ methacrylonitrile and the like. Of these, acrylonitrile and methacrylo-tolyl are preferred, and acrylonitrile is more preferred.
- acrylonitrile and methacrylo-tolyl are preferred, and acrylonitrile is more preferred.
- These ethylenically unsaturated nitrile monomers can be used alone or in combination of two or more.
- the amount of the ethylenically unsaturated nitrile monomer to be used is 10 to 40 parts by weight, preferably 18 to 30 parts by weight, based on 100 parts by weight of all the monomers. If the amount is too small, the bow I tensile strength and the resistance to organic solvents are inferior, and if it is too large, the feeling is poor.
- the ethylenically unsaturated acid monomer is not particularly limited as long as it is an ethylenically unsaturated monomer containing an acidic group such as a carboxyl group, a sulfonic acid group, and an acid anhydride group.
- acrylic acid Ethylenically unsaturated monocarboxylic acid monomers such as methacrylic acid; ethylenically unsaturated polycarboxylic acid monomers such as itaconic acid, maleic acid and fumaric acid; ethylenically unsaturated monomers such as maleic anhydride and citraconic anhydride
- Polyhydric carboxylic anhydride ethylenically unsaturated sulfonic acid monomer such as styrene sulfonic acid
- ethylenically unsaturated polycarboxylic acid such as monobutyl fumarate, monobutyl maleate, mono-2-hydroxypropyl maleate Partial ester monomers; and the like.
- ethylenically unsaturated carboxylic acids are preferred, ethylenically unsaturated monocarboxylic acids are more preferred, and methacrylic acid is particularly preferred.
- These ethylenically unsaturated acid monomers can also be used as alkali metal salts or ammonium salts. These ethylenically unsaturated acid monomers can be used alone or in combination of two or more.
- the amount of the ethylenically unsaturated acid monomer to be used is 5 to 15 parts by weight, preferably 7 to 12 parts by weight, based on 100 parts by weight of all the monomers. If this amount is too small, the tensile strength On the other hand, if the amount is too large, the texture and the durability of the adhesion state are poor.
- ethylenically unsaturated monomers copolymerizable therewith include, for example, vinyl aromatic monomers such as styrene, alkyl styrene, and vinyl naphthalene; and fluorene benzoquinones such as fluorethyl ether.
- ethylenically unsaturated monomers can be used alone or in combination of two or more.
- the amount of the other ethylenically unsaturated monomer to be used is at most 20 parts by weight, preferably at most 10 parts by weight, based on 100 parts by weight of all the monomers. If this amount is too large, the balance between feel and tensile strength is poor.
- the copolymer latex for dip molding of the present invention is obtained by copolymerizing the above monomer mixture, preferably by emulsion copolymerization. These are obtained by the following steps. In copolymerizing 100 parts by weight of the monomer mixture, at least 80% by weight of the conjugated diene monomer and 50 to 50% of the ethylenically unsaturated nitrile monomer among the monomers used for the polymerization. A monomer mixture containing 90% by weight, 40 to 90% by weight of an ethylenically unsaturated acid monomer and 80% by weight or more of other ethylenically unsaturated monomers copolymerizable therewith. First, polymerization is started using (Step 1).
- Step 2 the remaining ethylenically unsaturated nitrile monomer and the remaining ethylenically unsaturated acid
- Step 3 the remaining conjugated diene monomers and other ethylenically unsaturated monomers copolymerizable therewith are completely added until the polymerization reaction is stopped.
- the ethylenically unsaturated nitrile monomer is used in an amount of 50 to 90% by weight, preferably 55 to 85% by weight of the ethylenically unsaturated nitrile monomer used in the polymerization. More preferably, 60 to 85% by weight is charged into a polymerization reactor to start polymerization, and thereafter, the remaining ethylenically unsaturated nitrile monomer is added to the polymerization reaction system. If the proportion of the ethylenically unsaturated-tolyl monomer charged in the polymerization reactor is small, the tensile strength is poor, and if it is too large, the feeling and bow I tension strength are poor.
- the polymerization conversion rate of all monomers in the polymerization reaction system is in the range of 5 to 95% by weight, more preferably 10 to 90% by weight, and particularly preferably 20 to 90% by weight. At times, the remaining ethylenically unsaturated nitrile monomer is added to the polymerization reaction system. If the polymerization conversion is low, the feel and tensile strength are poor, and if it is high, the tensile strength is poor.
- the remaining ethylenically unsaturated nitrile monomer has a polymerization conversion of the ethylenically unsaturated nitrile monomer in the polymerization reaction system of 40 to 95% by weight, more preferably 45 to 92%. % By weight, particularly preferably in the range of 45 to 85% by weight, is preferably added to the polymerization reaction system. When added in this range, the tensile strength is further improved.
- the remaining ethylenically unsaturated nitrile monomer may be added to the polymerization reaction system all at once or separately.
- the remaining ethylenically unsaturated nitrile monomer is divided and added to the polymerization reaction system, the remaining ethylenically unsaturated nitrile monomer is equally divided according to the number of divisions, and the polymerization reaction system is divided. , Or may be added in a variable amount to the polymerization reaction system. Further, the number of divisions may be infinite, that is, a method of adding continuously may be adopted.
- the ethylenically unsaturated acid monomer is used for polymerization.
- the polymerization conversion of all the monomers in the polymerization reaction system is 5 to 95% by weight, preferably 10 to 90% by weight. %, More preferably from 20 to 80% by weight. /. Particularly preferred is when it is in the range of 40 to 70% by weight. By adding in this range, the tensile strength and the texture and the balance of the close contact state are further improved.
- a method of adding the remaining ethylenically unsaturated acid monomer to the polymerization reaction system for example, a method of adding it collectively, dividedly or continuously can be adopted. Among them, the method of adding all at once is preferable.
- the conjugated diene monomer is preferably charged to the polymerization reactor in an amount of preferably at least 80% by weight, more preferably at least 90% by weight, of the conjugated diene monomer used in the polymerization, and the polymerization was started. The addition of the conjugated diene monomer is completed before the polymerization reaction is stopped. It is particularly preferable to charge the entire amount of the conjugated diene monomer used for the polymerization to the polymerization reactor and start the polymerization.
- ethylenically unsaturated monomers copolymerizable with conjugated diene monomers, ethylenically unsaturated nitrile monomers and ethylenically unsaturated acid monomers are the other ethylenically unsaturated monomers used in the polymerization.
- the above is charged into a polymerization reactor, polymerization is started, and then the remaining other ethylenically unsaturated monomers are added by the time the polymerization reaction is stopped. It is particularly preferable that the entire amount of the other ethylenically unsaturated monomers used in the polymerization is charged into a polymerization reactor to start the polymerization.
- a usual method may be used except for the method of adding the monomer.
- a monomer mixture is polymerized with a polymerization initiator in the presence of water and an emulsifier, and a polymerization terminator is added at a predetermined polymerization conversion to terminate the polymerization reaction.
- the emulsifier is not particularly limited, for example, polyoxyethylene alkyl ether
- Nonionic emulsifiers such as nore, polyoxyethylene alkylphenol ether, polyoxyethylene phenol alkyl ester, and polyoxyethylene sorbitan alkyl ester; salts of fatty acids such as myristic acid, palmitic acid, oleic acid and linolenic acid;
- Anionic emulsifiers such as alkylbenzenesulfonic acid salts such as sodium dodecylbenzenesulfonic acid, higher alcohol sulfates, and alkylsulfosuccinates; alkyltrimethylammonium chloride, dialkylammonium chloride, benzylammonium chloride
- cationic emulsifiers such as ⁇ , — unsaturated carboxylic acid sulfoesters, ⁇ , ⁇ 3-unsaturated carboxylic acid sulfate esters,
- an anionic emulsifier is preferably used. These emulsifiers can be used alone or in combination of two or more. The amount of the emulsifier used is from 1 to 10 parts by weight based on 100 parts by weight of the monomer mixture.
- the amount of water to be used is 80 to 500 parts by weight, preferably 100 to 300 parts by weight, based on 100 parts by weight of the monomer mixture.
- the polymerization initiator is not particularly limited, and specific examples thereof include inorganic peroxides such as sodium persulfate, potassium persulfate, ammonium persulfate, potassium perphosphate, and hydrogen peroxide; disopropylbenzene hydroperoxide; Oxide, cumene hydroperoxide, t-butyl peroxide peroxide, 1,1,3,3-tetramethyl butyl hydride peroxide, 2,5-dimethylhexane-1,2,5-dihydroxide Organic peroxides such as tert-butyl peroxide, ze-CK, tamyl peroxide, acetyl-peroxide, isoptyryl peroxide, benzoyl peroxide, etc .; azobis-disoptyronitrile, azo-bis Azo compounds such as 2,4-dimethylvaleronitrile and methyl azobisisobutyrate; Can do.
- inorganic peroxides such
- polymerization initiators can be used alone or in combination of two or more.
- the peroxide initiator is preferably used because a latex can be stably produced, and a dip-molded product having a high tensile strength and a soft texture can be obtained.
- the amount of the polymerization initiator to be used is preferably 0.01 to 1.0 part by weight based on 100 parts by weight of the monomer mixture.
- the peroxide initiator is combined with a reducing agent to form a redox polymerization initiator. Can be used.
- the reducing agent examples include, but are not particularly limited to, compounds containing metal ions in a reduced state such as ferrous sulfate and cuprous naphthenate; sulfonic acid compounds such as sodium methanesulfonate; amines such as dimethylaniline; Compounds; and the like. These reducing agents can be used alone or in combination of two or more.
- the amount of the reducing agent to be used is preferably from 0.3 to 10 parts by weight per 1 part by weight of the peroxide.
- the copolymer latex for dip molding of the present invention is obtained by copolymerizing the monomer mixture as described above, and the methylethylketone insoluble portion (hereinafter abbreviated as “MEK insoluble portion”) of the copolymer obtained. ) Is 60 to 95% by weight.
- the MEK insoluble matter is preferably 70 to 90% by weight. If the MEK insoluble content is low, a dip molded product having poor organic solvent resistance and poor durability of the adhesion state will be obtained, and if it is high, a dip molded product having poor texture and tensile strength will be obtained.
- the molecular weight modifier examples include, for example, mercaptans such as n-butyl mercaptan, n-dodecyl mercaptan, t-dodecyl mercaptan; , ⁇ -methylstyrene dimer, tetrachlorocarbon, and the like. Among them, mercaptans are preferred, and t-dodecyl mercaptan is more preferred. These can be used-or in combination of two or more.
- the amount of the molecular weight modifier to be used may be appropriately determined so that the MEK-insoluble content of the copolymer falls within a desired range, but is preferably 0.05 to 100 parts by weight of the monomer mixture. It is 0.5 to 0.5 parts by weight, more preferably 0.1 to 0.4 parts by weight.
- polymerization terminator examples include hydroxyylamine, hydroxyamine sulfate, getyl hydroxyxamine, hydroxyamine sulfonic acid and its metal salts, sodium dimethyldithiocarbamate, hydroquinone derivatives, catechol derivatives, and Aromatic hydroxydithiocarboxylic acids such as hydroxydimethylbenzenethiocarboxylic acid, hydroxysiethyl benzenebenzenethiocarboxylic acid, and hydroxydibutylbenzenedithiocarboxylic acid, and alkali metals thereof Salts; and the like.
- the amount of the polymerization terminator used is not particularly limited, but is usually 0.1 to 2 parts by weight based on 100 parts by weight of all monomers.
- auxiliary polymerization materials such as a particle size regulator, a chelating agent, and an oxygen scavenger can be used.
- the polymerization temperature is not particularly limited, but is usually 0 to 95 ° C, preferably 35 to 70 ° C.
- the polymerization conversion when terminating the polymerization reaction is preferably 90% by weight or more, more preferably 93% by weight or more.
- Antioxidants, preservatives, antibacterial agents, dispersants, and the like can be added to the latex as needed.
- the number average particle size of the latex is preferably from 60 to 300 nm, more preferably from 80 to 150 nm.
- the particle size can be adjusted to a desired value by adjusting the amounts of the emulsifier and the polymerization initiator.
- composition for dip molding of the present invention comprises the above-described copolymer latex for dip molding, a vulcanizing agent and a vulcanization accelerator.
- the vulcanizing agent those usually used in dip molding can be used.
- sulfur such as powdered sulfur, sulfur, precipitated sulfur, colloidal sulfur, surface-treated sulfur and insoluble sulfur; hexamethylenediamine, trisulfur Polyamines such as ethylenetetramine and tetraethylenepentamine; and the like.
- sulfur is preferred.
- the amount of the vulcanizing agent to be used is preferably 0.1 to 5 parts by weight, more preferably 0.2 to 2 parts by weight, and particularly preferably 0.5 to 1.0 part by weight, based on 100 parts by weight of the solid content of the latex. 5 parts by weight. If the amount of the vulcanizing agent is too small, the tensile strength and the continuity of the adhesion state tend to be inferior. If the amount is too large, the hand tends to be inferior.
- vulcanization accelerator those usually used in dip molding can be used, and examples thereof include getyldithiocarbamic acid, dibutyldithiocarbamic acid, di-12-ethylhexyldithiocarbamic acid, and dihexylhexyldiylcarboxylate.
- Dithio powers such as thiocarbamic acid, diphenyldithiocarbamic acid, and dibenzyldithiolrubamic acid Bamic acids and their zinc salts; 2-mercaptobenzothiazole, 2-mercuff.
- zinc getyldithiocarbamate zinc dibutyldithiocarbamate, 2-mercaptobenzothiazole, and zinc 2-mercaptobenzothiazole are preferred.
- These vulcanization accelerators can be used alone or in combination of two or more.
- the amount of the vulcanization accelerator to be used is preferably 0.1 to 5 parts by weight, more preferably 0.1 to 1 part by weight, particularly preferably 0.2 to 1 part by weight, based on 100 parts by weight of the solid content of the latex. 0.9 parts by weight. If the amount of the vulcanization accelerator is too small, the tensile strength and the durability of the adhesion state tend to be inferior, and if it is too large, the hand tends to be inferior.
- the composition for dip molding of the present invention may further contain zinc oxide.
- the amount of zinc oxide used is preferably 10 parts by weight or less, preferably 0.2 to 2 parts by weight, more preferably 0.3 to 1.5 parts by weight, based on 100 parts by weight of the solid content of the latex. It is. When zinc oxide is blended in the above range, a dip molded product having an excellent balance of tensile strength, texture, and durability of adhesion can be obtained.
- the dip molding composition of the present invention may further contain, if desired, a pH adjuster, a thickener, an antioxidant, a dispersant, a pigment, a filler, a softener, and the like, which are usually added.
- a pH adjuster e.g., sodium bicarbonate
- a thickener e.g., sodium bicarbonate
- an antioxidant e.g., sodium bicarbonate
- a dispersant e.g., sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bi
- the solid content concentration of the composition for dip molding of the present invention is preferably 20 to 40% by weight, and more preferably 25 to 35% by weight.
- the pH of the dip-forming composition of the present invention is preferably in the range of 8 to 10, more preferably 8.5 to 9.
- the pH of the dip molding composition is within the above range, a dip molded product excellent in balance between the tensile strength and the persistence of the adhesion state can be obtained.
- the composition for dip molding is preferably aged before dip molding.
- the ripening conditions can be appropriately selected, but are usually 25 to 40, and are 12 hours to 3 days.
- the dip-formed product of the present invention is obtained by dip-forming the dip-forming composition.
- the dip molding method an ordinary method may be adopted.
- the dip forming method include a direct immersion method, an anodic adhesion immersion method, and a teag adhesion immersion method.
- the anode coagulation immersion method is preferred because a dip molded product having a uniform thickness is easily obtained.
- a dip molding die is immersed in a coagulant solution, and a coagulant is attached to the surface of the die. To form a dip molding layer.
- the coagulant examples 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; barium acetate, calcium acetate, and zinc acetate. Acetate; sulfates such as calcium sulfate, magnesium sulfate, and aluminum sulfate. Among them, calcium salt and calcium nitrate are preferred.
- the coagulant is usually used as a solution in water, alcohol, or a mixture thereof.
- the coagulant concentration is usually 5 to 70% by weight, preferably 20 to 50% by weight.
- the obtained dip molding layer is usually subjected to a heat treatment and vulcanized.
- the heat treatment Before the heat treatment, it is immersed in water, preferably 30 to 70 ° C. for about 1 to 60 minutes to remove water-soluble impurities (for example, excess emulsifier and coagulant). Good.
- This operation may be performed after heat treatment of the dip-formed layer, but is preferably performed before the heat treatment because water-soluble impurities can be removed more efficiently.
- the dip-formed layer thus obtained is subjected to a heat treatment at 100 to 150 ° C. for 10 to 120 minutes and vulcanized.
- a heating method an external heating method using infrared rays or hot air or an internal heating method using high frequency can be adopted. Of these, heating with hot air is preferred.
- a dip molded product is obtained by detaching the vulcanized dip molding layer from the dip molding die.
- the detaching method may be a method of peeling off from the molding die by hand, or a method of peeling off by water pressure or compressed air pressure.
- a heat treatment at a temperature of 60 to 120 ° C. for 10 to 120 minutes may be further performed.
- the dip-molded article can further form a surface treatment layer on its inner and / or outer surface.
- the dip-formed product of the present invention has a stress at 300% elongation of 3 MPa or less, a tensile strength of 2 OMPa or more, and a stress retention of 50% after 6 minutes from 100% elongation. Are easily obtained.
- the dip-formed product of the present invention can be manufactured to have a thickness of about 0.1 to about 3 mm, and can be suitably used particularly for a thin product having a thickness of 0.1 to 0.3 mm.
- medical supplies such as nipples for baby bottles, eye drops, conduits, water pillows; toys and sports equipment such as balloons, dolls, and poles; industrial supplies such as pressurized bags and gas storage bags; , Household, agricultural, fishing and industrial gloves;
- gloves it may be either a support type or an unsupport type. Among the above, it is suitable for thin surgical gloves.
- Copolymerization adjusted to pH 8.5 and solid content to 30% with 5% aqueous ammonia
- the body latex was cast on a glass plate with a frame and left at a temperature of 23 ° C and a relative humidity of 50% for 48 hours to obtain a dry film having a thickness of 1 mm.
- 0.3 g of the dried film was placed in an 80-mesh wire net and immersed in 100 ml of methyl ethyl ketone at 20 ° C for 48 hours.
- the film remaining in the basket of the wire mesh was dried under reduced pressure at 10 ° C., and the residual ratio was calculated to determine the methylethyl ketone insoluble content (%).
- the test piece was pulled by a Tensilon universal testing machine (RTC-1225A: manufactured by Orientec Co., Ltd.) at a tensile speed of 50 Omm / min, and the tensile stress at an elongation of 300% was measured. The smaller this value is, the better the texture is, and if it is approximately 3 MPa, it is good.
- RTC-1225A manufactured by Orientec Co., Ltd.
- test piece was pulled with a Tensilon universal testing machine at a pulling speed of 50 Omm / min, and the tensile strength immediately before breaking was measured.
- test specimen was pulled at a tensile speed of 50 Omm / min using a Tensilon universal testing machine, and the elongation immediately before breaking was measured.
- the obtained dip-formed product was cut into a disk having a diameter of 2 cm (R1). After immersing the test piece in 10 Oml of an organic solvent for 48 hours, the diameter (R 2) of the swollen film was measured. The value calculated by squaring the value obtained by dividing R2 by R1 was defined as the organic solvent swelling degree. The smaller the value, the better the resistance to organic solvents. (Example 1)
- TD MJ. t-decyl mercaptan
- Vulcanization prepared by mixing 1 part of sulfur, 0.5 part of zinc oxide, 0.5 part of zinc getylcarbamate, 1.5 parts of titanium oxide, 0.02 parts of potassium hydroxide and 3.52 parts of water After mixing 7.04 parts of the dispersant with 222.22 parts of copolymer latex A (100 parts of solid content), add an appropriate amount of deionized water and 5% aqueous ammonia to obtain a solid content of 30%.
- a composition for dip molding having a pH of 8.5 was obtained.
- the glove mold was immersed for 1 minute in an aqueous solution of coagulant prepared by mixing 25 parts of calcium nitrate, 0.05 parts of nonionic emulsifier polyoxyethylene octyl phenyl ether and 75 parts of water. After pulling up, it was dried for 3 minutes at 50 ° C., and the coagulant was adhered to the glove mold.
- coagulant prepared by mixing 25 parts of calcium nitrate, 0.05 parts of nonionic emulsifier polyoxyethylene octyl phenyl ether and 75 parts of water. After pulling up, it was dried for 3 minutes at 50 ° C., and the coagulant was adhered to the glove mold.
- the glove mold to which the coagulant was attached was immersed in the dip-forming composition for 1 minute, pulled up, and then dried at 25 ° C. for 3 minutes at the glove mold on which the dip-formed layer was formed. It was immersed in warm water at ° C for 3 minutes to elute water-soluble impurities. Then, The glove mold was dried at 80 ° C. for 20 minutes and subsequently heat-treated at 120 ° C. for 20 minutes to cure the dip molding layer. Finally, the vulcanized dip molding layer was peeled off from the glove mold to obtain a glove-shaped dip molding having a thickness of about 0.1 mm. Table 1 shows the evaluation results of this dip-formed product.
- Example 1 was repeated except that the initial charge amounts of the monomer mixture and TDM at the start of the polymerization reaction, and the amounts of acrylonitrile and methacrylic acid added after the start of the polymerization reaction were changed as shown in Table 1.
- copolymer latexes B and C were obtained.
- the MEK insolubles of the copolymer latexes B and C were measured and are shown in Table 1, respectively.
- a dip-formed product was obtained in the same manner as in Example 1, except that copolymer latex B and C were used instead of copolymer latex A, respectively.
- Table 1 shows the evaluation results of the dip molded products.
- Example 2 Polymerization was performed in the same manner as in Example 1 except that the initial charge amount of TDM was changed to 0.7 part, to obtain a copolymer latex D.
- the MEK insoluble content of the copolymer latex D was measured and is shown in Table 1.
- a dip molded product was obtained in the same manner as in Example 1 except that copolymer latex D was used instead of copolymer latex A.
- Table 1 shows the evaluation results of the dip molded products.
- Copolymer latex E was obtained by polymerization in the same manner as in Example 1 except that the charge composition shown in Table 1 was used, and the addition of atari-tolyl and methacrylic acid was not performed.
- the MEK insoluble content of the copolymer latex E was measured and is shown in Table 1.
- a dip molded product was obtained in the same manner as in Example 1 except that copolymer latex E was used instead of copolymer latex A.
- Table 1 shows the evaluation results of the dip molded products. Table 1 shows the following.
- the dip-molded product obtained using copolymer latex D, in which the MEK insoluble content is lower than the range specified in the present invention, is excellent in texture, but has tensile strength, stress retention and Table 1 shows the following.
- the dip-molded product obtained by using the copolymer latex D having an MEK insoluble content lower than the range specified in the present invention is excellent in texture, but is inferior in tensile strength, stress retention and organic solvent resistance ( Comparative Example 1).
- the dip molded products obtained using the copolymer latexes A to C of the present invention are excellent in organic solvent resistance and feeling, have sufficient tensile strength, and have good adhesion. Excellent state persistence (Examples 1-3).
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- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP04748243A EP1650237A4 (en) | 2003-07-31 | 2004-07-29 | TAUCHCOPOLYMERLATEX |
JP2005512568A JP4404053B2 (ja) | 2003-07-31 | 2004-07-29 | ディップ成形用の共重合体ラテックス |
US10/562,638 US20060235158A1 (en) | 2003-07-31 | 2004-07-29 | Dipping copolymer latex |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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JP2003-283857 | 2003-07-31 | ||
JP2003283857 | 2003-07-31 |
Publications (1)
Publication Number | Publication Date |
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WO2005012375A1 true WO2005012375A1 (ja) | 2005-02-10 |
Family
ID=34113822
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2004/011194 WO2005012375A1 (ja) | 2003-07-31 | 2004-07-29 | ディップ成形用の共重合体ラテックス |
Country Status (5)
Country | Link |
---|---|
US (1) | US20060235158A1 (ja) |
EP (1) | EP1650237A4 (ja) |
JP (1) | JP4404053B2 (ja) |
CN (1) | CN100400560C (ja) |
WO (1) | WO2005012375A1 (ja) |
Cited By (7)
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JP2006321954A (ja) * | 2005-05-20 | 2006-11-30 | Nippon Zeon Co Ltd | ディップ成形品 |
JP2008545814A (ja) * | 2005-05-13 | 2008-12-18 | キンバリー クラーク ワールドワイド インコーポレイテッド | 天然ゴムの特性を有するニトリルゴム物品 |
JP2009529585A (ja) * | 2006-03-10 | 2009-08-20 | キンバリー クラーク ワールドワイド インコーポレイテッド | 天然ゴムの特性を有する、外側がコーティングされたニトリルゴム物品 |
JP2009197149A (ja) * | 2008-02-22 | 2009-09-03 | Nippon A&L Inc | ディップ成形用共重合体ラテックス、ディップ成形用組成物およびディップ成形品 |
US8207276B2 (en) | 2005-05-20 | 2012-06-26 | Zeon Corporation | DIP forming latex composition and DIP formed article |
WO2021200984A1 (ja) * | 2020-03-31 | 2021-10-07 | ミドリ安全株式会社 | ディップ成形用組成物、及びその成形体 |
KR102732602B1 (ko) | 2020-04-28 | 2024-11-19 | 주식회사 엘지화학 | 니트릴계 공중합체의 제조방법 |
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WO2008099421A2 (en) * | 2007-02-13 | 2008-08-21 | Paradise Rubber Industries | A carboxylated acrylonitrile butadiene latex seamless bladder and a process for manufacturing thereof |
WO2008107914A2 (en) * | 2007-03-06 | 2008-09-12 | Paradise Rubber Industries | A laminated carboxylated acrylonitrile butadiene latex seamless bladder and a process for manufacturing thereof |
US8001809B2 (en) * | 2007-09-04 | 2011-08-23 | Ansell Healthcare Products Llc | Lightweight robust thin flexible polymer coated glove |
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CN101624433B (zh) * | 2009-08-07 | 2012-06-06 | 华东理工大学 | 一种热敏性共聚物胶乳及其制备方法和应用 |
US10336918B2 (en) * | 2012-08-31 | 2019-07-02 | Zeon Corporation | Adhesive composition |
US10344158B2 (en) | 2013-07-16 | 2019-07-09 | Skinprotect Corporation Sdn Bhd | Elastomeric film-forming compositions and articles made from the elastomeric film |
MY190720A (en) * | 2014-03-28 | 2022-05-12 | Zeon Corp | Composition for dip molding and dip-molded article |
KR20180132055A (ko) * | 2016-03-30 | 2018-12-11 | 니폰 제온 가부시키가이샤 | 공중합체 라텍스 |
WO2018017564A1 (en) * | 2016-07-19 | 2018-01-25 | Young Walter Michael | Animal toy and method of manufacture |
KR102081764B1 (ko) | 2016-09-01 | 2020-02-26 | 주식회사 엘지화학 | 딥 성형용 라텍스 조성물 및 이로부터 제조된 성형품 |
EP3587487A4 (en) * | 2017-02-22 | 2020-10-14 | Zeon Corporation | COMPOSITION OF LATEX |
US20220386719A1 (en) * | 2021-06-02 | 2022-12-08 | Twolink Sdn Bhd | Disposable vinyl acetate ethylene glove |
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MY125326A (en) * | 1999-06-21 | 2006-07-31 | Nippon A&L Inc | A latex compound for dip molding and a dip-molded product |
JP4554767B2 (ja) * | 1999-06-21 | 2010-09-29 | 日本エイアンドエル株式会社 | ディップ成形用ラテックス組成物及びディップ成形物 |
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US6870019B2 (en) * | 2000-12-12 | 2005-03-22 | Nippon A & L Inc. | Latex for dip molding and a dip molded product |
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2004
- 2004-07-29 US US10/562,638 patent/US20060235158A1/en not_active Abandoned
- 2004-07-29 CN CNB2004800220171A patent/CN100400560C/zh not_active Expired - Fee Related
- 2004-07-29 JP JP2005512568A patent/JP4404053B2/ja not_active Expired - Fee Related
- 2004-07-29 WO PCT/JP2004/011194 patent/WO2005012375A1/ja active Application Filing
- 2004-07-29 EP EP04748243A patent/EP1650237A4/en not_active Withdrawn
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Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008545814A (ja) * | 2005-05-13 | 2008-12-18 | キンバリー クラーク ワールドワイド インコーポレイテッド | 天然ゴムの特性を有するニトリルゴム物品 |
JP2012057164A (ja) * | 2005-05-13 | 2012-03-22 | Kimberly Clark Worldwide Inc | 天然ゴムの特性を有するニトリルゴム物品及びその作成方法 |
JP2006321954A (ja) * | 2005-05-20 | 2006-11-30 | Nippon Zeon Co Ltd | ディップ成形品 |
US8207276B2 (en) | 2005-05-20 | 2012-06-26 | Zeon Corporation | DIP forming latex composition and DIP formed article |
JP2009529585A (ja) * | 2006-03-10 | 2009-08-20 | キンバリー クラーク ワールドワイド インコーポレイテッド | 天然ゴムの特性を有する、外側がコーティングされたニトリルゴム物品 |
JP2009197149A (ja) * | 2008-02-22 | 2009-09-03 | Nippon A&L Inc | ディップ成形用共重合体ラテックス、ディップ成形用組成物およびディップ成形品 |
WO2021200984A1 (ja) * | 2020-03-31 | 2021-10-07 | ミドリ安全株式会社 | ディップ成形用組成物、及びその成形体 |
CN115397909A (zh) * | 2020-03-31 | 2022-11-25 | 绿安全股份有限公司 | 浸渍成型用组合物及其成型体 |
KR102732602B1 (ko) | 2020-04-28 | 2024-11-19 | 주식회사 엘지화학 | 니트릴계 공중합체의 제조방법 |
Also Published As
Publication number | Publication date |
---|---|
US20060235158A1 (en) | 2006-10-19 |
CN100400560C (zh) | 2008-07-09 |
EP1650237A1 (en) | 2006-04-26 |
EP1650237A4 (en) | 2010-05-05 |
JPWO2005012375A1 (ja) | 2006-10-05 |
JP4404053B2 (ja) | 2010-01-27 |
CN1829751A (zh) | 2006-09-06 |
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