WO2004081058A1 - 乳化重合用界面活性剤、当該界面活性剤を用いたポリマーエマルジョン組成物、当該組成物を含む繊維用フロック接着剤 - Google Patents
乳化重合用界面活性剤、当該界面活性剤を用いたポリマーエマルジョン組成物、当該組成物を含む繊維用フロック接着剤 Download PDFInfo
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- WO2004081058A1 WO2004081058A1 PCT/JP2004/003167 JP2004003167W WO2004081058A1 WO 2004081058 A1 WO2004081058 A1 WO 2004081058A1 JP 2004003167 W JP2004003167 W JP 2004003167W WO 2004081058 A1 WO2004081058 A1 WO 2004081058A1
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- surfactant
- polymerization
- emulsion
- polymer emulsion
- emulsion polymerization
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06Q—DECORATING TEXTILES
- D06Q1/00—Decorating textiles
- D06Q1/12—Decorating textiles by transferring a chemical agent or a metallic or non-metallic material in particulate or other form, from a solid temporary carrier to the textile
- D06Q1/14—Decorating textiles by transferring a chemical agent or a metallic or non-metallic material in particulate or other form, from a solid temporary carrier to the textile by transferring fibres, or adhesives for fibres, to the textile
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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
- C08F2/00—Processes of polymerisation
- C08F2/12—Polymerisation in non-solvents
- C08F2/16—Aqueous medium
- C08F2/22—Emulsion polymerisation
- C08F2/24—Emulsion polymerisation with the aid of emulsifying agents
- C08F2/30—Emulsion polymerisation with the aid of emulsifying agents non-ionic
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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
- C08L71/00—Compositions of polyethers obtained by reactions forming an ether link in the main chain; Compositions of derivatives of such polymers
- C08L71/02—Polyalkylene oxides
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J11/00—Features of adhesives not provided for in group C09J9/00, e.g. additives
- C09J11/08—Macromolecular additives
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J157/00—Adhesives based on unspecified polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
Definitions
- the present invention provides a surfactant for emulsion polymerization, which has a low amount of aggregates and good polymerization stability and mechanical stability, and a boule-based polymer emulsion composition containing the surfactant for emulsion polymerization.
- the present invention relates to a fiber flock adhesive containing the bull-based polymer emulsion composition, and a method for producing a flocked fabric characterized by flocking using the fiber flock adhesive.
- the paints, inks, sealants, adhesives, etc. used in the conventional organic solvent type reduce the environmental impact and cause health hazards caused by volatile organic compounds (VOC) commonly found in solvent type compositions.
- VOC volatile organic compounds
- the emulsion polymerization composition should meet or exceed the performance criteria expected for solvent-based compositions. As it is necessary to meet or exceed such performance criteria, the properties and properties of the aqueous polymer composition used in the emulsion polymerization composition are regarded as important, and also exhibit efficacy as a subsequent dispersion stabilizer. It is known that the performance and physical properties of the surfactant composition for emulsion polymerization greatly affect the performance criteria.
- a variety of surfactant for emulsion polymerization can be used for emulsion polymerization of a burl-based monomer such as atalyl ester or styrene, and a surfactant that gives properties suitable for the application purpose is selected.
- a surfactant that gives properties suitable for the application purpose is selected.
- anion surfactants and cationic surfactants are used to provide small particle size polymer dispersions with negative and positive charges, respectively.
- Noyuon surfactant gives a polymer emulsion of large particle size electrically almost neutral.
- cationic surfactants are rarely used, and in many cases, an anionic surfactant and a nonionic surfactant may be used alone or in combination.
- Polymer formulations using phanionic surfactants are excellent in the polymerization stability and mechanical stability of the produced polymer, but their chemical stability is bad and they have a lot of foaming, so especially foams Noon surfactants have been used in areas where they do not like it.
- a polymer formulation using a nonionic surfactant is excellent in chemical stability, freezing stability, and low foamability, it is considered that the storage stability and mechanical stability of the produced polymer are sufficient. It could not be said, and it was not satisfactory in all performances.
- the HLB of the nonionic surfactant, the particle diameter of the polymer emulsion formed, the polymerization stability, the mechanical stability, and the storage stability have a close relationship.
- the HLB of the nonionic surfactant increases, and the particle size of the produced polymer emulsion decreases, but the polymerization stability, mechanical stability, and storage stability tend to decrease.
- the present invention is intended to solve the above-mentioned problems of the prior art, and the object of the present invention is to reduce the amount of deposits and aggregates formed inside the reactor, Stability of polymer emulsion during emulsion polymerization, polymerization stability of formed polymer emulsion, excellent mechanical stability, low foaming, small average particle diameter
- the surfactant for emulsion polymerization of the present invention, the composition of such a burle-based polymer, the flock adhesive for fibers using this polymer emulsion composition, and the flock adhesive for said fibers To provide a method for producing a flocked fabric characterized by fock processing
- the present inventors have found that the use of a specific surfactant for emulsion polymerization for emulsion polymerization reduces the amount of deposits and aggregates formed inside the reactor, and the stability of the polymer emulsion during emulsion polymerization.
- the inventors have found that it is possible to provide a surfactant for emulsion polymerization which is excellent in the polymerization stability and mechanical stability of the polymer emulsion formed, has a low foaming, and has a small average particle size, and the present invention has been accomplished.
- the present invention relates to a surfactant for emulsion polymerization which contains a surfactant having an acid as an essential component.
- R 3 (R 4 ) CH— (wherein R 3 and R 4 each independently represent a branched or linear alkyl group having 1 to 22 carbon atoms) It is preferable that it is a secondary alcohol alkoxylate represented by the general formula (I) which is
- the present invention also relates to a boule based polymer emulsion composition containing the above surfactant for emulsion polymerization.
- a fiber comprising the above-mentioned boule-based polymer emulsion composition.
- the present invention relates to flock adhesives.
- the present invention relates to a method for producing a flocked fabric characterized by flocking using the above-mentioned fiber flock adhesive.
- the present invention will be described in detail.
- the first aspect of the present invention is a compound represented by the following general formula (I):
- the present invention relates to a surfactant for emulsion polymerization which contains a surfactant having a hydrophilic lipophilic balance (GL B of HL B) represented by 18. 5 to 19.5 as an essential component.
- the hydrophilic lipophilic balance (HLB of Griffin) of the surfactant is preferably 18.6 to 19.0, more preferably 18.8 to 89.0.
- HLB hydrophilic lipophilic balance
- HLB Hydrophilic Lipophilic Balance
- HLB 20 X (1-W 0 / W) (2)
- W is the molecular weight of the hydrophobic group in the surfactant, and W is the molecular weight of the whole surfactant.
- the surfactant for emulsion polymerization used in the present invention is represented by the general formula (I)
- the compound represented by the general formula (I) is contained as an essential component, and 1 ⁇ in the general formula (I) has 1 to 24 carbon atoms, preferably 8 to 18 carbon atoms, more preferably 10 to 14 branched or Straight chain alkyl group, Number of carbon atoms:! -24, preferably 8 to 18, more preferably 10 to 14 aryl groups, carbon atoms having 8 to 18 carbon atoms, preferably 10 to 14 carbon atoms, more preferably 1 to 14 alkyl atoms Represents an aryl group containing a group.
- the emulsion polymerization does not proceed well, the amount of deposits and aggregates deposited inside the reaction increases, and the polymerization stability and mechanical properties of the resulting polymer emulsion are increased. Problems such as reduced stability occur.
- the emulsion polymerization can be efficiently proceeded, and the amount of deposits and aggregates formed on the inside of the reactor can be generated. It is possible to suppress and prevent the polymerization stability and mechanical stability of the polymer emulsion obtained by preventing it.
- branched or linear alkyl group having 1 to 24 carbon atoms among the above-mentioned R methyl, ethyl, propyl, isopropyl, pentyl, isopyl, sec-peptinore, tert-peptinore, pentinole, isopentinole, tert- Pentyl, neopentyl, hexyl, isohexyl, heptyl, octyl, noel, decyl, undecyl, dodecyl, 2-ethylhexyl, tridecyl, tetradecyl, tetradecyl, pentadecyl, hexadecyl, heptadecyl, octadecyl, nonadecyl, eicosyl, Heneikosyl, docosyl etc.
- aryl monole group having 1 to 24 carbon atoms phenylene, benzyl, phenylenele, o-, m- or p-tril, 2, 3- or 2, 4-xylyl, mesityl Naphthyl, anthryl, 7 enanthryl, biphenyl, benzhydryl, trityl, pyrenyl and the like.
- aryl group containing an alkyl group having 8 to 18 carbon atoms o, m, ⁇ -torinore, o, m, p-phenylenyl, phenethyl, xylinole, o, m, p-cumenole, o, m, p- Shimenire, o, p, m-mentha-nore, mesityl, diphenyl methyl and the like.
- the surfactant according to the present invention is a secondary alcohol alkoxylate represented by the general formula (I) in which R 3 (R 4 ) CH— in the general formula (I).
- the secondary alcohol alkoxylate as an essential surfactant component for the surfactant for emulsion polymerization, the amount of monomer added can be sufficient with a small amount of addition compared to other surfactants for hatching polymerization.
- the amount added is the same, the amount of deposits attached to the inside of the reactor during emulsion polymerization and the amount of aggregates formed can be further suppressed, and a polymer emulsion of small particle size can be produced.
- R 3 and R 4 each independently represent a branched or linear, preferably linear alkyl group having 1 to 22 carbon atoms, and the number of carbon atoms of R 3 and R 4 The total number of carbon atoms is 1 to 23, preferably 7 to 17, and more preferably 9 to 13.
- the above is a secondary alkyl group represented by the formula: R 3 (R 4 ) CH—, that is, in a particularly preferred embodiment in which the surfactant according to the present invention is a secondary alcohol alkoxylate, secondary Oxyalkylene group in alcohol alkoxylate
- the position of addition of (one (AO) -one in general formula (I)) is represented by the position of addition of an oxyalkylene group counted from the carbon at the end of the alkyl group, for example, a secondary alcohol having 12 carbon atoms In the case of alkoxylates, there are 2, 3, 4, 5, 6 positions.
- the addition position distribution of the oxyalkylene group the maximum amount of a single addition position component is 2
- A represents a lower isolexylene group, preferably a lower alkylene group having 2 to 8 carbon atoms, more preferably 2 to 4 carbon atoms.
- A is an alkylene group having 9 or more carbon atoms, the production cost is high, the hydrophobicity is too strong, and the emulsion polymerization does not proceed well, and deposits and aggregates attached to the inside of the reactor. It is not preferable because it may cause the increase in the amount of formation of the polymer and the decrease in the polymerization stability and mechanical stability of the formed polymer emulsion.
- examples of the oxyalkylene group represented by AO include, for example, an oxyethylene group, an oxypropylene group, an oxypeptylene group, an oxoxypentylene group, an oxypentylene group, an oxyhexylene group, an oxyheptylene group, an oxoxyiotylene group, an oxyphenyl ethylene and the like.
- it is an oxyethylene group, an oxypropylene group or an oxypeptylene group, and more preferably an oxyethylene group or an oxypropylene group.
- one kind of oxyalkylene group defined by AO when there are a plurality of AO, that is, when n in the general formula (I) is 2 or more, one kind of oxyalkylene group defined by AO is It may be composed of only two or more.
- the oxyalkylene group is composed of two or more types, two or more types of oxyalkylene groups may be randomly disposed, and each may be disposed in blocks. For example, it may be configured that a part of the long chain of the oxyethylene group is an oxypropylene group.
- ⁇ in the above general formula (I) represents the average number of oxykilene groups present in the surfactant of the general formula (I), and is on average 10 to 100, preferably 60 to 90 It is.
- ⁇ exceeds 100, the amount of aggregates formed during emulsion polymerization increases, and there is a risk that the polymerization stability of the formed polymer emulsion or the machine stability may decrease. Preferred! /.
- the n force S 10 is less than 10
- the emulsion polymerization does not proceed well, and the amount of deposits and aggregates adhering to the inside of the reactor may be increased, or the same surfactant
- the particles of the formed polymer emma / region become large, so it is necessary to use a large amount of surfactant for emulsion polymerization in order to make the particle diameter of the same degree.
- ⁇ ⁇ 2 or more
- one or two or more types of oxyalkylene groups represented by AO may be used.
- two or more types of oxyalkylene groups are used, various types of oxyalkylene groups may be used. It is assumed that the total number of oxyalkylene groups is n in total.
- R 2 represents a hydrogen atom or an alkyl group having 1 to 3 carbon atoms (a methyl group, an ethyl group, a propyl group or an isopropyl group), preferably a methylol group or an ethyl group. It is a group.
- the method for producing the surfactant of the general formula (I) according to the present invention is not particularly limited, and known methods can be used alone or in combination.
- the method for producing a secondary alcohol alkoxylate which is a preferred embodiment of the present invention, will be described in detail.
- C 1 2 ⁇ 1 4 secondary alcohol manufactured by Nippon Shokubai Co., Ltd., trade name: softer Nord one A
- the addition method of this alkylene oxide for example, the above-mentioned secondary alcohol is reacted at a reaction temperature of 50 to 2
- the desired secondary alcohol alkoxylate can be obtained by reaction with an alkylene oxide under the conditions of 0 ° C.
- an alkaline catalyst such as an acid catalyst of BF 3 ⁇ , Na OH, KO H or the like may be used.
- the acid catalyst and alkali catalyst may be added in the form of powder, granules, or as an aqueous solution.
- the surfactant for emulsion polymerization of the present invention may be composed of one or two or more of the surfactants of the above-mentioned general formula (I), or other surfactants for emulsion polymerization. And may be configured in combination. For example, a secondary alcohol alkoxylate of HLB 18.5 or more and a nonionic surfactant of HLB 18.5 or less may be combined, and a secondary alcohol alkoxylate of HLB 18: 5 or more and an anion may be used. You may combine with surfactant.
- the surfactant for emulsion polymerization to be used is not particularly limited.
- nonionic surfactants there are polyoxyethylene laurinoleate tenore, polyoxyethylene sethi / leetheneole, polyoxyethylene stearilene tenoleate, Polyoxyethylene alkyl ether such as polyoxyethylene oleyl ether / le, polyoxyethylene nonyl phenyl ether, polyoxyethylene alkyl phenyl ether, polyoxyethylene alkyl ether such as polyoxyethylene dodecyl phenyl ether, etc.
- Ryl ether Polyoxyethylene sorbitan monolaurate, polyoxyethylene sorbitan mono noremitate, polyoxyethylene sorbitan monostearate, polyoxyethylene sorbita And fatty acid esters such as polyoxyethylene fatty acid esters such as polyoxyethylene fatty acid esters such as polyoxyethylene fatty acid esters, and other reactive surfactants having functional groups in the structure of the surfactant. good.
- Polyethylene glycol ester such as polyethylene glycol ether, polyoxyethylene cetyl ether, polyoxy ethylene stearyl ether, polyoxyethylene ether, etc.
- anionic surfactants include linear alkyl sulfates, linear alkyl benzene sulfonates, polyoxyethylene alkyl ether sulfates, and polyoxyethylene alkyl phenyl ether sulfates.
- the other surfactants (nonionic surfactants and / or negative surfactants) as described above may be used alone or in the form of a mixture of two or more, and The ratio in the case of combining two or more types is not particularly limited, and can be combined within a range that does not substantially cause any problem.
- the surfactant of the general formula (I) according to the present invention is preferably contained in the range of 70% by weight or more, more preferably 80% by weight or more in the surfactant composition for emulsion polymerization. It is preferable to
- the second of the present invention is a boule based polymer emulsion composition containing the surfactant for emulsion polymerization of the present invention.
- Amount of emulsion polymerization surfactants in the polymer E Mar Ji compositions of the present invention the polymer E Mar John total composition, preferably from 0.1 to 1 .0 wt 0/0 range, more Preferably, it is in the range of 1.0 to 5.0% by weight. If the addition amount of the surfactant for emulsion polymerization is not within the appropriate range, the amount of deposits and aggregates formed on the inside of the reactor will increase, and the particle size of the formed polymer emulsion will increase, and the polymerization stability will be increased. , Mechanical stability, monomer yield tends to decrease.
- burle type monomer which comprises the polymer emulsion composition of this invention
- a well-known burle type monomer can be used.
- styrene, ⁇ Aromatic biel monomers such as monomethyl / lystyrene, chlorostyrene, dimethynoleaminostyrene, nitrostyrene, divinylbenzene and the like; halogenated butyl and halogenated biuredene monomers such as biel bromide, chloride chloride, chloride chloride and the like; Vinyl ester monomers such as acetic acid bule and propionic acid boule; ethylene, propylene, 1-butene, 1-hexene,...
- 1-refin-type monomers such as 1st grade ctenene; conjugated dienes such as butadiene and isoprene; (meth) acrylic acid (Meth) methyl acrylate, (meth) acrylic acid ethyl, (meth) acrylic acid butyl, (meth) acrylic acid methyl ethyl, atalic acid ethyl hydroxyl, (meth) atalic acid 2-ethyl ethyl ester (meta ) (Meth) acrylic acid esters such as acrylic acid 2-hydroxyl Acrylamide, 2-acrylamide, acrylic nitrile, and the like (meth) Atari Runitoriru, Jefferies chill fumarate.
- any catalyst that accelerates polymerization can be used without particular limitation, and a common peroxide, azo initiator, an oxidant and a reducing agent may be used in combination It is preferable to use a redox base polymerization initiator, and to use a redox polymerization initiator.
- Examples of the oxidizing agent to be used as a redox type polymerization initiator include persulfate lithium, sodium persulfate, ammonia persulfate, ammonium persulfate, azobisisobutyronitrile, hydrogen peroxide and the like, and reduction
- As the agent sodium sulfite, sodium metabisulfite, sodium thiosulfite, ascorbic acid, hydrozine and the like can be mentioned.
- polymerization stabilizer polysorboleone, ⁇ - methinoresenoresulose, hydroxyethenoresorellose, oleorexoxime
- Protective colloids such as chill cellulose, polybutyl pyrrolidone and water-soluble polyurethane compounds may be used in combination.
- the emulsion polymerization method of the present invention is a method of carrying out emulsion polymerization using a surfactant (including a composition) for emulsion polymerization according to the present invention, and as a method of emulsion polymerization, monomers may be used. Common emulsion polymerization methods such as addition method, emulsion addition method, seed polymerization method can be used.
- the reaction temperature at the time of dropping the monomer is adjusted by the decomposition temperature of the polymerization initiator, but it is preferably in the range of ⁇ 10 ° C. 150 ° C., preferably
- the polymerization reaction time depends on other conditions such as the reaction temperature, and is not particularly limited, but is usually 36 hours.
- the amount of aggregates formed in the polymer emulsion composition obtained in the present invention is preferably not more than 1.0% by weight, more preferably 0.5% by weight, based on the total amount of the polymer dispersion composition mixed. % Or less. If the amount of aggregate formation exceeds 1.0% by weight, it is necessary to remove the formed aggregates, and the cost of discarding the aggregates and the like will increase, so the production side tends to be less desirable. It is because there is.
- the average particle size of the polymer emulsion obtained in the present invention is preferably 150 nm or less, more preferably 10 to: 150 nm, still more preferably 10 to: L 0, particularly preferably 2 0 to 100 nm. If the average particle size of the obtained polymer emulsion exceeds 150 nm, the particles in the polymer emulsion will be prone to aggregation and sedimentation, so the amount of deposits and aggregates deposited inside the reactor increases. Also, the polymerization stability of the resulting polymer emulsion tends to decrease.
- the polymer emulsion composition of the present invention can be used as a thermoplastic resin or thermosetting resin. It can be used in various fields such as films, moldings, paints, sheet laminates, rubber adhesives, decorative plywood, flash panels, sundries, accessories, wall materials, industrial materials, etc. It is also effective as an adhesive.
- a third of the present invention is a fiber flock adhesive containing the vinyl polymer emulsion composition of the present invention.
- Such flock products include flock products for clothing such as overcoats, blazer coats, gloves, hats, mufflers, etc., flocked carpets, mats, curtains, cushions, footwear flocks for materials such as outer skins of dolls, dolls
- examples of flock adhesives that can be used for groceries such as toys, bags, hoses, electric wires, etc. are polyvinyl acetate emulsions and ataryls.
- a known flocking adhesive such as a series emulsion or synthetic rubber latex may be used in combination.
- thermosetting resins and curing accelerators such as methyl cellulose, carboxyl methyl cellulose, hydroxy cellulose and polybutyl alcohol may be used.
- Polyvinyl acetate emulsion is also thickened using a thermosetting resin and a curing accelerator in the same manner as the above-mentioned acrylic emulsion, but in addition to improving normal temperature film forming property and initial adhesion, Add a reversible agent such as phthalate, 2-ethylhexyldiphenylphosphate, methylphthalyl methyl glycolate, polyethylene glycol adipate and the like. Also, in the case of synthetic rubber latex, adhesives such as rosin, ester gum, terpene resin, petroleum resin, styrenic resin, alkyl phenol resin, etc.
- a softener such as a lysopuprylene copolymer, a polymer polybutylobutylether, lanolin, and an anti-aging agent such as phenyl 'mononaphthylamine, mercabubuto zoimidazole, and pentyl hydroquinone.
- a softener such as a lysopuprylene copolymer, a polymer polybutylobutylether, lanolin, and an anti-aging agent such as phenyl 'mononaphthylamine, mercabubuto zoimidazole, and pentyl hydroquinone.
- ethylene oxide stands for EO
- propylene oxide stands for PO
- An atarylate mixture was prepared by mixing 100. 0 g of butyl acrylate, 40. O g of methyl acrylate and 4.0 g of acrylic acid. To 500ml Separafurasu co, deionized water 226. 9 g, Atari rate mixture 14. 4 ⁇ , the nonionic surfactants listed in Table 1 (A-1) ⁇ ( A- 9), (B- 1) ⁇ Similarly, (B-8) was added in the amount described in Table 1, and nitrogen was blown in for 30 minutes while stirring at a rotation speed of 200 rpm.
- a monomer mixture was prepared by mixing 120. 0 g of styrene, 16.0 g of 2-hydroxy hydroxyl methacrylate and 4.0 g of 2 acrylamide.
- ion exchange water 23.5 g
- monomer mixture 14.4 g
- each nonionic surfactant listed in Table 2 (A-9) to (A-15)
- B-9) to ( Similarly, B-11) was added in the amount described in Table 2, and nitrogen was blown in for 30 minutes while stirring at a rotation speed of 200 rpm. Then, while stirring under a nitrogen atmosphere, add 0.33 g of potassium persulfate, raise the internal temperature to 80 ° C, and leave the temperature as it is.
- each polymer emulsion of Comparative Examples (9) to (11) in the same manner as in Synthesis Example 1, an aggregate formation amount, polymerization Rate, polymerization stability, average particle size, mechanical stability, foamability, paint pinder test was conducted. The results are shown in Tables 5 and 6.
- A— 13 Primary alcohol ethoxylate 100 19. 2 2.0
- the obtained polymer Emma / Region was subjected to gas chromatography [Gas chromatography: Shimadzu G C- 17 A Column: GL Sciences Inc., NEUTRA BOND- 1 (length; 30 m inner diameter; 0.53 mm film thickness 2. 0 ⁇ m), temperature condition; initial temperature 50 ° C. (hold for 5 minutes), heating rate 10 ° C. Zmin, final temperature 350 ° C. (hold for 40 minutes), loading amount of sample: condition of IL]
- the content of each monomer was determined from the area ratio of the resulting chart, and the polymerization rate was calculated from the weight of the blended monomer.
- the resulting polymer emulsion is allowed to stand at room temperature for a week, then filtered on a 100 mesh wire mesh, lightly washed with water, dried at 80 ° C. for 4 hours, and its mass is measured to formulate incorporated polymer emulsion.
- the weight average particle diameter of the obtained polymer emulsion was measured using a particle diameter measuring apparatus D LS-700 by a dynamic light scattering method manufactured by Union Giken.
- the resulting polymer emulsion is neutralized to pH 9 with 25% ammonia water, and 50 g of the neutralized polymer emulsion “a emulsion” is taken and subjected to a shear test under conditions of 5000 rpm for 10 minutes with a homomixer.
- the polymer emulsion after the test was filtered on a 100 mesh wire mesh, lightly washed with water, dried at 80 ° C. for 4 hours, and measured for mass to determine the mass% relative to the total amount of blended polymer emulsion.
- thermosetting catalyst Suditex ACX
- the pH was adjusted to 6.5 with 25% aqueous ammonia.
- the mixture was applied to paper / aluminium at a rate of 2 gZm 2 using a wet lamination device, and lamination was performed at a rate of 15 OmZ minutes, and the 180 ° C. peel strength of the obtained composite film was tested. .
- a pigment 300 g of titanium dioxide (rutin type), 40 g of pearlite, 20 g of talc, 140 g of calcium carbonate, and 100 g of a 2% aqueous solution of hydroxyl cellulose as a thickening agent as pigments are obtained.
- a pigment dispersant 8 g of a 10% aqueous solution of sodium hexametaphosphate was added and mixed.
- the resulting emulsion coating was applied to a mortar and tested for weatherability and washing resistance. In the weather resistance test, the coated film was left outdoors for 6 months, and the deterioration of the coating such as wrinkles, blisters, blisters, peeling and discoloration was visually examined.
- the above mortar 0.5% salt water After being soaked in water and boiled for 3 hours, tests were conducted for peeling of the coated surface. At this time, the results of the weathering test were divided into the following three classes.
- ⁇ no deterioration
- ⁇ some deterioration
- X deterioration
- Example 1 A-1 0. 19 99. 1 ⁇ 0. 01 57 ⁇ 0. 01 70
- Example 2 0. 05 99. 5 ⁇ 0. 01 35 ⁇ 0. 01 69
- Example 3 Line 3 0, 24 98. 9 0. 02 63 ⁇ 0. 01 72
- Example 4 A-4 0. 23 99. 3 ⁇ 0. 01 57 ⁇ 0. 01 77
- Example 5 A-5 0. 45 98. 6 0. 02 76 0. 02 73
- Example 6 A-6 0. 36 98. 5 ⁇ 0. 01 90 0. 02 70
- Example 7 A-7 0. 47 98. 1 0. 03 97 0.
- Example 1 A-1 7 £ 9j ⁇ 280 280 A A ⁇ A 2 A A 2 3 ⁇ J 77>>> ⁇ ⁇ 300 ⁇
- Example 3 A ⁇ 3 ⁇ > Q ⁇ J ⁇ J ⁇ J ⁇ J>> 77 330 330
- Example 4 A — 4 oq ⁇ j ⁇ ⁇ j 70J 0J 0J n 280
- Example 1 A-1 1 0. 29 98. 7 ⁇ 0. 0 1 7 1 0. 02 74
- Example 1 2 A-1 2 0. 26 98. 7 ⁇ 0. 0 1 68 ⁇ 0. 0 1 79
- Example 1 3 A-1 3 0. 4 1 98. 0 ⁇ 0. 0 1 82 0. 05 78
- Example 14 A-14 0. 28 9 9. 0 ⁇ 0. 0 1 9 3 0. 02 74
- Example 1 5 A-1 5 0. 36 98. 7 0 0 0 1 98 0. 04 78
- 96 9 1. 6 0. 1 2 245 0. 23
- Comparative example 1 1 2. 09 9 3.3 3 0. 09 1 9 3 0. 1 9 86
- the surfactant for emulsion polymerization according to the present invention for emulsion polymerization As shown in Tables 3 to 6 above, by using the surfactant for emulsion polymerization according to the present invention for emulsion polymerization, the average particle size is small, and deposits and deposits attached to the inside of the reactor. As a result, a polymer emulsion composition which can reduce the amount of the formed product and is excellent in polymerization stability and mechanical stability can be obtained, and a fiber flock adhesive containing this polymer emulsion composition can be used as a flocked fabric. By using it, a flocked product with excellent fastness and texture can be obtained.
- the polymer emulsion of the present invention may be, besides the flocked fabric, a fuinolem, a molded product, a paint, a sheet laminate, a rubber adhesive, a decorative plywood, a flash panel, miscellaneous goods, small articles, a wall material, an industrial material, Even when used in various fields such as non-woven fabrics, the effect is exhibited.
- Industrial use available Yayoi Yayoi
- the surfactant for emulsion polymerization of the present invention is used for emulsion polymerization of a boule-based monomer, the amount of deposits and aggregates adhering to the inside of the reactor can be suppressed, and the stability of polymer emulsion during emulsion polymerization By maintaining the polymerization stability of the formed polymer emulsion sufficiently, it is possible to obtain a polymer emulsion having excellent mechanical stability, low foaming and small average particle size.
- the polymer emulsion composition of the present invention can be used as a fiber flock adhesive.
- This product can be used in textiles and can be processed into flocks with excellent fastness and appearance.
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- Polymers & Plastics (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Adhesives Or Adhesive Processes (AREA)
- Polymerisation Methods In General (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
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JP2005503559A JP4118913B2 (ja) | 2003-03-13 | 2004-03-11 | 乳化重合用界面活性剤、当該界面活性剤を用いたポリマーエマルジョン組成物、当該組成物を含む繊維用フロック接着剤 |
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JP2003-068438 | 2003-03-13 | ||
JP2003068438 | 2003-03-13 |
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WO2004081058A1 true WO2004081058A1 (ja) | 2004-09-23 |
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PCT/JP2004/003167 WO2004081058A1 (ja) | 2003-03-13 | 2004-03-11 | 乳化重合用界面活性剤、当該界面活性剤を用いたポリマーエマルジョン組成物、当該組成物を含む繊維用フロック接着剤 |
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JP (1) | JP4118913B2 (ja) |
KR (1) | KR100706276B1 (ja) |
CN (1) | CN100523006C (ja) |
WO (1) | WO2004081058A1 (ja) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013213197A (ja) * | 2012-03-06 | 2013-10-17 | Nippon Synthetic Chem Ind Co Ltd:The | 合成樹脂エマルジョン、及びそれを用いてなるコーティング剤、ならびにコーティング層 |
Citations (10)
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JPS5531820A (en) * | 1978-08-24 | 1980-03-06 | Sumitomo Chem Co Ltd | Preparation of vinyl chloride type polymer emulsion |
JPS58129012A (ja) * | 1982-01-28 | 1983-08-01 | Nitto Kasei Kk | 防汚用トリ有機錫含有共重合体エマルジヨンの製造方法 |
JPH01318027A (ja) * | 1988-06-17 | 1989-12-22 | Toagosei Chem Ind Co Ltd | 水性樹脂組成物の製造方法 |
JPH0665337A (ja) * | 1992-08-14 | 1994-03-08 | Asahi Glass Co Ltd | 含フッ素ポリマー水性分散液 |
JPH0665336A (ja) * | 1992-08-14 | 1994-03-08 | Asahi Glass Co Ltd | 含フッ素重合体水性分散液 |
JPH0741748A (ja) * | 1993-07-29 | 1995-02-10 | Mitsui Petrochem Ind Ltd | 水分散型接着剤 |
JPH0912656A (ja) * | 1995-06-29 | 1997-01-14 | Sekisui Chem Co Ltd | 塩化ビニル系樹脂エマルジョン及びその製造方法 |
JPH10273570A (ja) * | 1997-03-31 | 1998-10-13 | Grand Polymer:Kk | 水分散体及び水分散型接着剤 |
JPH10296007A (ja) * | 1997-04-25 | 1998-11-10 | Asahi Denka Kogyo Kk | リン酸製造工程用消泡剤 |
JP2001072702A (ja) * | 1999-06-29 | 2001-03-21 | Asahi Denka Kogyo Kk | 乳化重合用乳化剤又は懸濁重合用分散剤 |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
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TW519535B (en) * | 1996-12-06 | 2003-02-01 | Nippon Catalytic Chem Ind | Higher secondary alcohol alkoxylate compound composition, method for production thereof, and detergent and emulsifier using the composition |
-
2004
- 2004-03-11 WO PCT/JP2004/003167 patent/WO2004081058A1/ja active Application Filing
- 2004-03-11 JP JP2005503559A patent/JP4118913B2/ja not_active Expired - Lifetime
- 2004-03-11 KR KR1020057016582A patent/KR100706276B1/ko not_active IP Right Cessation
- 2004-03-11 CN CNB2004800067398A patent/CN100523006C/zh not_active Expired - Fee Related
Patent Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5531820A (en) * | 1978-08-24 | 1980-03-06 | Sumitomo Chem Co Ltd | Preparation of vinyl chloride type polymer emulsion |
JPS58129012A (ja) * | 1982-01-28 | 1983-08-01 | Nitto Kasei Kk | 防汚用トリ有機錫含有共重合体エマルジヨンの製造方法 |
JPH01318027A (ja) * | 1988-06-17 | 1989-12-22 | Toagosei Chem Ind Co Ltd | 水性樹脂組成物の製造方法 |
JPH0665337A (ja) * | 1992-08-14 | 1994-03-08 | Asahi Glass Co Ltd | 含フッ素ポリマー水性分散液 |
JPH0665336A (ja) * | 1992-08-14 | 1994-03-08 | Asahi Glass Co Ltd | 含フッ素重合体水性分散液 |
JPH0741748A (ja) * | 1993-07-29 | 1995-02-10 | Mitsui Petrochem Ind Ltd | 水分散型接着剤 |
JPH0912656A (ja) * | 1995-06-29 | 1997-01-14 | Sekisui Chem Co Ltd | 塩化ビニル系樹脂エマルジョン及びその製造方法 |
JPH10273570A (ja) * | 1997-03-31 | 1998-10-13 | Grand Polymer:Kk | 水分散体及び水分散型接着剤 |
JPH10296007A (ja) * | 1997-04-25 | 1998-11-10 | Asahi Denka Kogyo Kk | リン酸製造工程用消泡剤 |
JP2001072702A (ja) * | 1999-06-29 | 2001-03-21 | Asahi Denka Kogyo Kk | 乳化重合用乳化剤又は懸濁重合用分散剤 |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013213197A (ja) * | 2012-03-06 | 2013-10-17 | Nippon Synthetic Chem Ind Co Ltd:The | 合成樹脂エマルジョン、及びそれを用いてなるコーティング剤、ならびにコーティング層 |
Also Published As
Publication number | Publication date |
---|---|
CN100523006C (zh) | 2009-08-05 |
JP4118913B2 (ja) | 2008-07-16 |
JPWO2004081058A1 (ja) | 2006-06-08 |
KR100706276B1 (ko) | 2007-04-12 |
KR20050117537A (ko) | 2005-12-14 |
CN1759124A (zh) | 2006-04-12 |
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