WO2015159587A1 - Latex de caoutchouc, composition de latex de caoutchouc et article moulé - Google Patents

Latex de caoutchouc, composition de latex de caoutchouc et article moulé Download PDF

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Publication number
WO2015159587A1
WO2015159587A1 PCT/JP2015/055269 JP2015055269W WO2015159587A1 WO 2015159587 A1 WO2015159587 A1 WO 2015159587A1 JP 2015055269 W JP2015055269 W JP 2015055269W WO 2015159587 A1 WO2015159587 A1 WO 2015159587A1
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rubber latex
mass
vinyl monomer
carboxyl group
copolymer
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PCT/JP2015/055269
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English (en)
Japanese (ja)
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佳祐 東
潔 砂田
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電気化学工業株式会社
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Priority to CN201580020397.3A priority Critical patent/CN106232645A/zh
Priority to JP2016513660A priority patent/JP6490670B2/ja
Publication of WO2015159587A1 publication Critical patent/WO2015159587A1/fr

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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
    • C08F236/18—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 containing chlorine
    • 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
    • C08K5/09—Carboxylic acids; Metal salts thereof; Anhydrides thereof
    • 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

Definitions

  • This technology relates to rubber latex containing polychloroprene.
  • the present invention also relates to a rubber latex composition using the rubber latex and a molded product using the rubber latex composition.
  • Rubber latex containing polychloroprene is used as a material for molded articles such as gloves and sheets because a flexible and well-stretched film is obtained.
  • a technique for controlling the structure by adjusting the polymerization temperature and polymerization rate when producing polychloroprene a technique for controlling the structure by adjusting the polymerization temperature and polymerization rate when producing polychloroprene, Technology for copolymerization of 2,3-dichloro-1,3-butadiene to lower the crystallization rate of the copolymer, and technology for adjusting the crosslinking component of the copolymer (insoluble matter in organic solvents such as tetrahydrofuran and toluene) are known (see Patent Documents 1 to 3).
  • the above-mentioned conventional technology can form a uniform film as long as a molded product having a film thickness of 0.1 mm or more is produced, and can produce a molded product having sufficient mechanical strength and flexibility. .
  • the film may be perforated due to insufficient mechanical strength.
  • a molded article is produced using a rubber latex known as a water-based adhesive material, an effect of improving mechanical strength can be obtained by ion crosslinking between zinc oxide added as a compounding agent and a carboxyl group. Therefore, it can be expected that the molded product will be thin.
  • the rubber latex as the material of the water-based adhesive cannot be used as a material of a molded product because the viscosity increases in an alkaline environment and the film cannot be formed.
  • the present technology intends to provide a rubber latex having good viscosity stability in an alkaline environment.
  • the present technology intends to provide a rubber latex composition using the rubber latex and a molded product using the rubber latex composition that can maintain the mechanical strength even when the film is thinned.
  • the rubber latex according to the present technology is a rubber latex containing a copolymer of chloroprene and a carboxyl group-containing vinyl monomer, and is derived from the carboxyl group-containing vinyl monomer in 100% by mass of the copolymer. 0.1 to 2.0% by mass of a free carboxyl group-containing vinyl monomer having a binding unit of 0.5 to 3.5% by mass and not bound to the copolymer in 100% by mass of the rubber latex. It is a rubber latex having a pH of 8-14.
  • the emulsifier used in the production of the copolymer may contain an anionic emulsifier, and the polymerization rate of the copolymer may be in the range of 70 to 99.9%.
  • the rubber latex composition according to the present technology includes 100 parts by mass of the solid content of the rubber latex, 1 to 10 parts by mass of a metal oxide, and 0.1 to 3 parts by mass of sulfur.
  • the molded product according to the present technology is obtained by molding the rubber latex composition.
  • This technology provides rubber latex with good viscosity stability in an alkaline environment.
  • a rubber latex composition using the rubber latex and a molded article using the rubber latex composition that can maintain the mechanical strength even when the film is thinned are obtained.
  • the rubber latex according to the embodiment of the present technology includes (1) a copolymer of chloroprene and (2) a carboxyl group-containing vinyl monomer, and (3) a free carboxyl group-containing vinyl monomer.
  • Chloroprene is 2-chloro-1,3-butadiene, which is copolymerized with a carboxyl group-containing vinyl monomer described later to form a copolymer contained in rubber latex.
  • carboxyl group-containing vinyl monomer improves the mechanical strength of the film of the molded article and prevents the increase in viscosity when the pH of the rubber latex is adjusted to 8-14. Copolymerized with chloroprene.
  • the carboxyl group-containing vinyl monomer is copolymerizable with chloroprene and includes acrylic acid, methacrylic acid, fumaric acid, maleic acid, crotonic acid, and citraconic acid. These can be used alone or in combination of two or more. Among these, methacrylic acid, maleic acid, and crotonic acid are preferably used alone or in combination of two or more. Since the storage stability of the rubber latex is further improved, it is more preferable to use methacrylic acid alone.
  • the copolymer has a binding unit of 0.5 to 3.5% by mass derived from a carboxyl group-containing vinyl monomer in 100% by mass.
  • the binding amount of the carboxyl group-containing vinyl monomer is less than 0.5% by mass, the solid content of the rubber latex may be aggregated and separated during pH adjustment.
  • the binding amount of the carboxyl group-containing vinyl monomer exceeds 3.5% by mass, the elongation at break becomes insufficient in the mechanical strength of the molded product.
  • the amount of bond units derived from the carboxyl group-containing vinyl monomer is more preferably 0.8 to 2.5% by mass.
  • the ratio of these monomers may be adjusted when chloroprene and the carboxyl group-containing vinyl monomer are copolymerized.
  • the proportion of the carboxyl group-containing vinyl monomer charged to the reactor is preferably 0.5 to 10 parts by mass, and 1.0 to 6.0 parts by mass in 100 parts by mass of the total monomers. More preferably, it is a part.
  • the method for charging chloroprene and carboxyl group-containing monomer into the reactor is not particularly limited. All monomers may be charged all at once in the initial stage, or some monomers may be added in portions during polymerization.
  • the rubber latex is lyophilized to form a dry product, which is dissolved in benzene, and methanol is added to remove the rubber component. Precipitation is performed, and the deposited rubber content may be measured by 1 H-NMR.
  • the rubber latex is freeze-dried to obtain a dry product, which is dissolved in an ethanol-toluene mixed solution to recover a rubber component (insoluble matter).
  • the recovered rubber component is measured with a pyrolysis gas chromatograph mass spectrometer. Also good.
  • the rubber latex is 0.1 to 2.0% by mass of a free carboxyl group-containing vinyl monomer that is not bonded to the copolymer in 100% by mass of the rubber latex. It is what has. When the content of the free carboxyl group-containing vinyl monomer is less than 0.1% by mass, the viscosity increases when the pH of the rubber latex is adjusted to 8 to 14, and handling such as filtration with a filter or filling into a container is possible. It becomes difficult. If the content of the free carboxyl group-containing vinyl monomer exceeds 2.0% by mass, the solid content of the rubber latex may be aggregated and separated during pH adjustment.
  • the content of the free carboxyl group-containing vinyl monomer is more preferably 0.2 to 1.0% by mass.
  • the solid content of the rubber latex is all components obtained by removing volatile components such as water from the rubber latex, and a copolymer of chloroprene and a carboxyl group-containing vinyl monomer, and various kinds of components added during emulsion polymerization. It contains the nonvolatile content of the additive.
  • the charge amount and polymerization rate of the carboxyl group-containing vinyl monomer when copolymerized with chloroprene may be adjusted.
  • the rubber latex In order to measure the content of the free carboxyl group-containing vinyl monomer, the rubber latex is diluted with pure water and then centrifuged, and the free carboxyl group-containing vinyl monomer in the resulting supernatant is subjected to liquid chromatography. And the amount of free carboxyl group-containing vinyl monomer in the rubber latex may be converted based on the measured value.
  • the pH of the rubber latex is adjusted to 8-14. If the pH of the rubber latex is less than 8, the stability of the rubber latex itself during long-term storage becomes low, and solid content may settle during storage.
  • the pH of the rubber latex is adjusted by adding a pH adjuster to the rubber latex after completion of emulsion polymerization.
  • pH adjusters include potassium pyrosulfite, potassium sulfite, potassium hydrogen sulfite, potassium phosphate, potassium hydrogen phosphate, sodium pyrosulfite, sodium sulfite, sodium hydrogen sulfite, sodium phosphate, sodium hydrogen phosphate, potassium hydroxide, sodium hydroxide, There is ammonia.
  • the pH adjuster may be used alone or in combination of two or more. In particular, potassium hydroxide or sodium hydroxide is preferable because the pH can be adjusted efficiently with a small addition amount.
  • chloroprene and carboxyl group-containing vinyl monomer are emulsion copolymerized in the presence of water, emulsifier, initiator and chain transfer agent, and after reaching the predetermined polymerization rate, the polymerization is stopped.
  • An agent may be added to terminate the polymerization reaction, remove unreacted monomers, and adjust the pH and solid content concentration.
  • the solid content concentration is a mass ratio of non-volatile components contained in the rubber latex, and can be calculated from the mass before and after drying when the rubber latex is dried.
  • the ratio of the monomer and water during the emulsion polymerization is preferably 75 to 200 parts by mass, more preferably 80 to 150 parts by mass with respect to 100 parts by mass of the total monomers.
  • a polymerization temperature stably by making the ratio of the water with respect to 100 mass parts of total monomers into 75 mass parts or more, and it becomes industrial of rubber latex by making it into 200 mass parts or less.
  • Productivity can be improved.
  • the polymerization temperature is not particularly limited, but it is preferably 5 to 50 ° C. in order to perform the polymerization reaction smoothly.
  • the copolymer contained in the rubber latex according to the present technology is preferably obtained by copolymerizing chloroprene and a carboxyl group-containing vinyl monomer in the presence of an emulsifier. It is more preferable to use an anionic emulsifier as the emulsifier. In order to improve storage stability and low-temperature stability, an anionic emulsifier and a nonionic emulsifier may be used in combination. These emulsifiers may be used alone or in combination of two or more.
  • anionic emulsifier examples include carboxylic acid type and sulfuric acid ester type.
  • alkali metal salts of rosin acid alkali metal salts of alkyl sulfuric acid, alkali metal salts of alkyl polyoxyethylene sulfuric acid, alkali metal salts of alkyl aryl sulfuric acid And the like, sulfuric acid group-containing alkali metal salts such as alkylbenzene sulfonic acid, and sulfonic acid group-containing alkali metal salts such as a condensate of sodium naphthalene sulfonate and formaldehyde.
  • anionic emulsifiers Although it does not specifically limit as an alkali metal salt in these anionic emulsifiers, A sodium salt and potassium salt are preferable. These anionic emulsifiers can be used alone or in combination of two or more. As the anionic emulsifier, one or more sulfonic acid alkali metal salts are preferably used, and one or more benzenesulfonic acid alkali metal salts are more preferably used. By using a benzenesulfonic acid type emulsifier, the stability during emulsion polymerization can be further improved.
  • anionic emulsifiers include dialkylsulfosuccinic acid alkali metal salts, alkane sulfonic acid alkali metal salts, alpha olefin sulfonic acid alkali metal salts, linear alkyl benzene sulfonic acid alkali metal salts, and alkyl (branched) benzene sulfonic acid alkali metals. Salt, alkali metal naphthalenesulfonate formaldehyde condensate, and alkali metal alkylnaphthalenesulfonate.
  • nonionic emulsifier examples include polyvinyl alcohol or a copolymer thereof (for example, a copolymer with acrylamide), polyvinyl ether or a copolymer thereof (for example, a copolymer with maleic acid), polyoxyethylene alkyl ether. , Polyoxyethylene alkylphenols, sorbitan fatty acid esters and polyoxyethylene acyl esters. These can be used alone or in combination of two or more. Among these, it is preferable to use polyvinyl alcohol and polyoxyethylene alkyl ether alone or in combination of two or more, and it is more preferable to use polyvinyl alcohol or polyoxyethylene lauryl ether alone.
  • the amount of the emulsifier used for the emulsion polymerization is preferably 0.5 to 5 parts by mass, more preferably 1 to 3 parts by mass with respect to 100 parts by mass of all monomers.
  • the stability of a polymerization liquid can be improved more by making the preparation amount of an emulsifier 0.5 mass parts or more with respect to 100 mass parts of all the monomers.
  • molding a rubber latex composition becomes more favorable because the preparation amount of an emulsifier shall be 5 mass parts or less with respect to 100 mass parts of all the monomers.
  • the initiator those usually used for emulsion polymerization of chloroprene can be used. Specifically, there are persulfates such as potassium persulfate and organic peroxides such as tertiary butyl hydroperoxide.
  • chain transfer agent those usually used for emulsion polymerization of chloroprene can be used.
  • alkyl mercaptans such as n-dodecyl mercaptan and tertiary-dodecyl mercaptan
  • dialkylxanthogen disulfides such as diisopropylxanthogen disulfide and diethylxanthogen disulfide
  • iodoform alkyl mercaptans such as n-dodecyl mercaptan and tertiary-dodecyl mercaptan
  • dialkylxanthogen disulfides such as diisopropylxanthogen disulfide and diethylxanthogen disulfide
  • iodoform iodoform
  • polymerization terminator those usually used for emulsion polymerization of chloroprene can be used. Specific examples include 2,6-tertiarybutyl-4-methylphenol, phenothiazine, and hydroxyamine.
  • the polymerization rate of the copolymer is preferably 65 to 99.9%, and more preferably 70 to 99.9%.
  • the polymerization rate of the copolymer is preferably 65% or more, more preferably 70% or more from the viewpoint of the stability of the rubber latex at the time of pH adjustment, and preferably 99.9% from the viewpoint of industrial feasibility. Below, more preferably 99% or less.
  • the removal of the unreacted monomer (demonomer) may be performed by a known method such as heating under reduced pressure.
  • rubber latex may be copolymerized with other monomers that can be copolymerized with chloroprene and carboxyl group-containing monomers as long as the effects of the present technology are not impaired. it can.
  • Such copolymerizable monomers include 2,3-dichloro-1,3-butadiene, 1-chloro-1,3-butadiene, sulfur, methacrylic esters, acrylic esters, 1-chloro There are butadiene, butadiene, isoprene, ethylene, styrene, and acrylonitrile. These may be used alone or in combination of two or more.
  • a freezing stabilizer In the rubber latex, a freezing stabilizer, an emulsion stabilizer, a viscosity modifier, an antioxidant, a preservative, and the like can be optionally added to the rubber latex as long as the effects of the present technology are not impaired.
  • a rubber latex composition according to an embodiment of the present technology includes 100 parts by mass of the solid content of the rubber latex, 1 to 10 parts by mass of a metal oxide, and 0.1 to 3 parts by mass of sulfur. By adding (4) metal oxide and (5) sulfur to the rubber latex, a rubber latex composition can be obtained.
  • the rubber latex composition can be used as a material for a molded article having a low film modulus and excellent mechanical properties such as strength and elongation.
  • the metal oxide improves the mechanical strength of the film of the molded article using the rubber latex composition.
  • the metal oxide include zinc oxide and magnesium oxide. These may be used alone or in combination of two or more as required.
  • the addition amount of the metal oxide is preferably 1 to 10 parts by weight, more preferably 1.5 to 5 parts by weight, per 100 parts by weight of the solid content of the rubber latex. By making the addition amount of the metal oxide 1 part by mass or more per 100 parts by mass of the solid content of the rubber latex, the tensile strength is further improved out of the mechanical strength of the film of the molded article, and it is 10 parts by mass or less. Thus, the elongation becomes better in the mechanical strength of the film of the molded article.
  • Sulfur Sulfur improves the productivity of the molded product by adjusting the vulcanization speed of the rubber latex composition.
  • the amount of sulfur added is preferably 0.1 to 3 parts by mass, more preferably 0.3 to 1.5 parts by mass, per 100 parts by mass of the solid content of the rubber latex. By making it in this range, the productivity of the molded product is further improved, and the dispersibility of the rubber latex composition is further improved.
  • the rubber latex composition of the present embodiment as additives other than metal oxides and sulfur, vulcanization accelerators, antioxidants, fillers, plasticizers, pigments, and colorants as long as the effects of the present technology are not impaired. , Wetting agents, antifoaming agents and the like can be added.
  • vulcanization accelerators antioxidants, fillers, plasticizers, pigments, and colorants as long as the effects of the present technology are not impaired.
  • Wetting agents, antifoaming agents and the like can be added.
  • those that are insoluble in water or destabilize the colloidal state of the rubber latex composition may be added after preparing their aqueous dispersions in advance.
  • the molded article according to the embodiment of the present technology is obtained by molding the rubber latex composition according to the embodiment.
  • the rubber latex composition can be formed into a molded product by dip molding as it is, or by freeze-drying the rubber latex composition to obtain a solid chloroprene rubber, followed by extrusion molding, blow molding, injection molding or the like.
  • Examples of molded products obtained by immersion molding include medical gloves and inspection gloves.
  • a rubber latex composition using the rubber latex of the present technology is a molded product excellent in mechanical properties and wearing feeling such as high strength but low modulus and easy elongation. This molded product can also be reduced in cost by thinning.
  • Example 1 The rubber latex of Example 1 has 1.5% by mass of bond units derived from methacrylic acid as a carboxyl group-containing vinyl monomer in 100% by mass of the copolymer contained in the rubber latex. Have a free carboxyl group-containing vinyl monomer of 0.3% by mass and a pH of 10.5. The rubber latex of Example 1 had good viscosity stability in an alkaline environment. A rubber latex composition using this rubber latex yielded a molded product that could retain its mechanical strength even when it was thinned.
  • the rubber latex production method and evaluation method, rubber latex composition and molded product production method, and molded product evaluation method of Example 1 were performed as shown below.
  • ⁇ PH> The pH of the rubber latex was measured using a pH meter F-22 manufactured by Horiba, Ltd. after adjusting the temperature of the rubber latex to 20 ° C.
  • the polymerization rate of the copolymer in the rubber latex was calculated by the following formula.
  • the total charge refers to the charge of all materials charged into the reactor, such as water, chloroprene and carboxyl group-containing vinyl monomer, emulsifier and initiator.
  • the evaporation residue is a non-volatile component excluding the copolymer contained in the rubber latex, and is derived from the emulsifier and the initiator.
  • the total monomer means all monomers charged into the reactor in addition to chloroprene and a carboxyl group-containing vinyl monomer.
  • ⁇ Viscosity stability under alkaline environment The rubber latex was adjusted to 25 ° C., and the viscosity at 30 rpm was measured with a Brookfield viscometer. A sample having a viscosity of less than 500 mPa ⁇ s was evaluated as ⁇ , and a sample having a viscosity of 500 or more was evaluated as ⁇ .
  • ⁇ Storage stability> The rubber latex was allowed to stand in a sealed state at 23 ° C. for 8 weeks, and the pH change of the rubber latex was measured. The magnitude of the decrease in pH is a measure for judging storage stability. A sample in which the decrease in pH was suppressed to less than 0.5 was evaluated as “good” (good storage stability) because there was no possibility of formation of aggregates or precipitation of components. A drop in pH of 0.5 or more, or a product in which coagulation or a coagulated product was apparently generated was evaluated as x because of insufficient storage stability.
  • a ceramic cylinder with an outer diameter of 50 mm heated to 50 ° C. in a dryer is immersed in a coagulation liquid in which 70 parts by mass of water and 30 parts by mass of calcium nitrate tetrahydrate are mixed for 30 seconds, and again in the dryer at 50 ° C. And dried for 2 minutes.
  • the treated ceramic cylinder was dipped in the rubber latex composition produced by the above method for 4 minutes and then washed with running water for 1 minute.
  • the washed ceramic pottery cylinder was dried in an atmosphere of 23 ° C. for 1 day, and the film formed on the surface was peeled off from the pottery cylinder to obtain an unvulcanized film.
  • the obtained unvulcanized film was heat-treated in a dryer at 120 ° C. for 30 minutes to obtain a molded product.
  • the thin film was evaluated by measuring the thickness of the vulcanized film using a test piece thickness meter (SDA-12, manufactured by Kobunshi Keiki Co., Ltd.) and visually observing the presence or absence of pinholes or tears.
  • a film having a film thickness of less than 0.1 mm and having no pinholes or tearing was rated as “ ⁇ ”, a film having a film thickness of less than 0.1 mm and having a pinhole or tearing, or a film having a thickness of 0.1 mm or more as “x”.
  • X Normal physical properties were not measured for the samples for evaluation.
  • Table 1 shows the information regarding the production of the rubber latex of Example 1 and the evaluation results of the rubber latex and the molded product.
  • Example 2 to 14 Comparative Examples 1 to 5
  • the initial charge amount and addition amount of chloroprene used in preparing the rubber latex, the type and amount of the carboxyl group-containing vinyl monomer, the type and amount of the emulsifier, A rubber latex, a rubber latex composition, and a molded product were prepared in the same manner as in Example 1 except that the pH and the polymerization rate were changed as described in Table 1 or Table 2, and evaluated in the same manner as in Example 1. The evaluation results are shown in Table 1 or Table 2.
  • sodium alkyldiphenyl ether disulfonate is Perex SS-H (purity 50%) manufactured by Kao Corporation.
  • Sodium polyoxyethylene lauryl ether sulfate is LATEMUL E-150 (purity 33%) manufactured by Kao Corporation.
  • Polyvinyl alcohol is Nichigo G polymer (degree of saponification 89 mol%) manufactured by Nippon Synthetic Chemical Industry Co., Ltd. “Perex”, “Latemul” and “Nichigo G-Polymer” are registered trademarks.
  • the rubber latex of Examples 1 to 14 had good viscosity stability in an alkaline environment, and the molded product was excellent in mechanical strength even when it was thinned.
  • a rubber latex having good viscosity stability in an alkaline environment can be obtained, and a molded product obtained by molding a rubber latex composition containing the rubber latex can be a thin film. It was suggested that the mechanical strength can be maintained.
  • molded products according to the present technology were produced and evaluated according to the following procedure.
  • the rubber latex compositions of Examples 1 to 14 were made into a solid chloroprene rubber by a known freeze-drying method, and the resulting chloroprene rubber was blow-molded to obtain a film having a thickness of 0.05 mm. The obtained film was able to maintain the mechanical strength even when it was thinned like the molded product.

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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)
  • Compositions Of Macromolecular Compounds (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)

Abstract

L'invention concerne : un latex de caoutchouc qui présente une stabilité de viscosité satisfaisante dans un environnement alcalin ; une composition de latex de caoutchouc comprenant le latex de caoutchouc ; et un article moulé obtenu à partir de la composition de latex de caoutchouc, l'article moulé étant apte à conserver la résistance mécanique même lorsqu'il est mince. Le latex de caoutchouc contient un copolymère de chloroprène avec un monomère vinylique carboxylé. La teneur en motifs combinés, dérivés du monomère vinylique carboxylé est de 0,5 à 3,5 % en masse pour 100 % en masse du copolymère et la teneur en monomère vinylique carboxylé libre et ne s'étant pas combiné au copolymère est de 0,1 à 2,0 % en masse pour 100 % en masse du latex de caoutchouc, le latex de caoutchouc ayant un pH de 8 à 14.
PCT/JP2015/055269 2014-04-18 2015-02-24 Latex de caoutchouc, composition de latex de caoutchouc et article moulé WO2015159587A1 (fr)

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CN201580020397.3A CN106232645A (zh) 2014-04-18 2015-02-24 橡胶胶乳、橡胶胶乳组合物及成形品
JP2016513660A JP6490670B2 (ja) 2014-04-18 2015-02-24 ゴムラテックス、ゴムラテックス組成物及び成形品

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JP2018111772A (ja) * 2017-01-11 2018-07-19 東ソー株式会社 クロロプレンラテックス組成物
EP3904403A4 (fr) * 2018-12-27 2022-10-12 Showa Denko K.K. Procédé pour la production de latex de polymère de chloroprène

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