Classifications

• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
  • C09D11/00—Inks
  • C09D11/02—Printing inks
  • C09D11/03—Printing inks characterised by features other than the chemical nature of the binder
  • C09D11/033—Printing inks characterised by features other than the chemical nature of the binder characterised by the solvent
• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
  • C09D11/00—Inks
  • C09D11/02—Printing inks
  • C09D11/03—Printing inks characterised by features other than the chemical nature of the binder
  • C09D11/037—Printing inks characterised by features other than the chemical nature of the binder characterised by the pigment
• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
  • C09D11/00—Inks
  • C09D11/02—Printing inks
  • C09D11/10—Printing inks based on artificial resins
  • C09D11/106—Printing inks based on artificial resins containing macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
  • C09D11/107—Printing inks based on artificial resins containing macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds from unsaturated acids or derivatives thereof
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B41—PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
  • B41M—PRINTING, DUPLICATING, MARKING, OR COPYING PROCESSES; COLOUR PRINTING
  • B41M1/00—Inking and printing with a printer's forme
  • B41M1/10—Intaglio printing ; Gravure printing

Definitions

• the present invention relates to a resin particle dispersion.
• Gravure printing is intaglio printing in which the ink in the concave portion of the plate is transferred under pressure, and is excellent in gradation reproducibility, and therefore, it is widely used in the commercial printing field of magazines, catalogs, brochures, and the like.
• conventional substrates such as cardboard, paper board, resin film and the like which is not white, from printing on conventional white paper.
• improvement of coating film properties such as adhesion to a substrate is required for a resin film substrate made of polyolefin resin, polyester resin and the like.
• aqueous ink In the case of printing on a substrate that is not a white background, white ink is used to render white or to enhance visibility.
• a pigment used for a white ink titanium oxide having high hiding power is widely used.
• the aqueous ink composition generally contains a pigment, a polymer and water, and the polymer is added as a pigment dispersant or binder for the purpose of improving the film physical properties of the printed matter.
• the polymer a dispersion of core-shell resin particles obtained by emulsion polymerization in the presence of the core resin is often used.
• Patent Document 1 discloses a core-shell type resin particle dispersion that exhibits excellent coating film physical properties with respect to a resin film substrate, and an aqueous solution used for gravure printing and the like containing the same.
• An ink composition is disclosed.
• Patent Document 1 discloses a core-shell type resin for an aqueous ink having a specific average particle size and a Tg, which is obtained by polymerizing an ethylenically unsaturated monomer in an aqueous medium in the presence of a water-soluble resin.
• a particle dispersion wherein the water-soluble resin is a water-soluble resin formed by polymerizing an aromatic ethylenic unsaturated monomer and a carboxyl group-containing ethylenic unsaturated monomer, and the ethylenic unsaturated
• a core-shell type resin particle dispersion for water-based ink, and a water-based ink composition are described, the monomers comprising an aromatic ethylenically unsaturated monomer and an ethylenically unsaturated monomer as essential components. .
• the present invention is a resin particle dispersion containing core-shell type resin particles (A), glycol ether (B) and water
• the core unit resin of the core-shell type resin particles (A) comprises 40% by mass of a structural unit derived from a (meth) acrylate having a hydrocarbon group of 2 to 18 carbon atoms in the structural unit constituting the core resin
• the core-shell resin particles (A) have an acid value of 50 mg KOH / g or more and 100 mg KOH / g or less.
• the carbon number of the hydrocarbon group of the ether portion of the glycol ether (B) is 2 or more and 8 or less, and the content of the glycol ether (B) is 2.8% by mass or more in the resin particle dispersion.
• the present invention relates to a resin particle dispersion.
• an ink that can be printed on various resin films has high versatility, and is excellent in storage stability and substrate adhesion is desired.
• a glycol ether having a carbon number of 2 in the hydrocarbon portion of the ether portion is blended at a maximum of 2.5% by mass in the examples, but the core of the core-shell type resin particles And it is necessary to use 2 or more types of monomers containing a specific amount of aromatic ethylenically unsaturated monomer for resin which comprises a shell.
• the present invention relates to a resin particle dispersion that can be used as an aqueous ink having excellent substrate adhesion.
• the present inventors contain a specific amount of a structural unit derived from a specific (meth) acrylic acid ester in the core portion, and combine the core-shell type resin particles having a specific acid value with a specific glycol ether to obtain the above. I found that I could solve the problem.
• the present invention is a resin particle dispersion containing core-shell type resin particles (A), glycol ether (B) and water
• the core unit resin of the core-shell type resin particles (A) comprises 40% by mass of a structural unit derived from a (meth) acrylate having a hydrocarbon group of 2 to 18 carbon atoms in the structural unit constituting the core resin
• the core-shell resin particles (A) have an acid value of 50 mg KOH / g or more and 100 mg KOH / g or less.
• the carbon number of the hydrocarbon group of the ether portion of the glycol ether (B) is 2 or more and 8 or less, and the content of the glycol ether (B) is 2.8% by mass or more in the resin particle dispersion.
• the present invention relates to a resin particle dispersion.
• the resin particle dispersion which can be used as aqueous ink excellent in storage stability and base-material adhesiveness can be provided.
• the resin particle dispersion of the present invention is a resin particle dispersion containing core-shell type resin particles (A) (hereinafter also referred to as "resin particles (A)”), glycol ether (B) and water.
• the core unit resin of the core-shell type resin particles (A) comprises 40% by mass of a structural unit derived from a (meth) acrylate having a hydrocarbon group of 2 to 18 carbon atoms in the structural unit constituting the core resin
• the core-shell resin particles (A) have an acid value of 50 mg KOH / g or more and 100 mg KOH / g or less.
• the carbon number of the hydrocarbon group of the ether portion of the glycol ether (B) is 2 or more and 8 or less, and the content of the glycol ether (B) is 2.8% by mass or more in the resin particle dispersion.
• the resin particle dispersion of the present invention may further contain a pigment or the like to be used as an aqueous ink for printing, particularly for gravure printing. When the resin particle dispersion of the present invention does not contain a pigment, it can be used as a clear ink.
• the resin particle dispersion of the present invention has an effect that it can be used as an aqueous ink excellent in printability and excellent in storage stability and adhesion to a substrate. Although the reason is not clear, it is considered as follows.
• the acid value of the core-shell type resin particles (A) according to the present invention is 50 mg KOH / g or more and 100 mg KOH / g or less, whereby the resin particles (A) are stabilized as a dispersion.
• the structural unit derived from a (meth) acrylic acid ester having a hydrocarbon group having 2 to 18 carbon atoms constituting the core portion resin of the resin particle (A) has high affinity with the glycol ether (B).
• the resin particle (A) contains the structural unit derived from the (meth) acrylic acid ester in a relatively large amount of 40% by mass or more in the structural unit constituting the core portion resin, whereby the resin particle dispersion is obtained. It is considered that the glycol ether (B) contained at 2.8% by mass or more penetrates into the resin particles (A), and the resin particles (A) are plasticized. And since resin particles (A) have an appropriate acid value, not only stability is provided to the ink by electrostatic repulsion, but a resin particle dispersion is applied to the surface of a substrate such as a resin film.
• the ink is spread uniformly on the surface of the substrate, and the evaporation of water during the drying process promotes plasticization of the resin particles (A), which is considered to facilitate elastic deformation of the resin particles (A). .
• the film formed by the aggregation of the resin particles (A) is a compact and uniform film that does not cause gaps between the resin particles.
• the adhesion of the base material is considered to be improved because it acts like an elastic body with the fused portions of the resin particles as a base point.
• the resin particle dispersion of the present invention contains core-shell resin particles (A).
• the core-shell type resin particle (A) is a resin particle having a structure in which the core portion resin is covered with the resin of the shell portion, and the core portion resin of the core-shell type resin particle (A) is a hydrocarbon group having 2 to 18 carbon atoms.
• the constituent unit derived from (meth) acrylic acid ester having 40% by mass or more in the constituent unit constituting the core part resin, and the acid value of the core-shell type resin particle (A) is 50 mgKOH / g or more and 100 mgKOH / g or less It is.
• core-shell type resin particle (A) consists of multiple phases
• resin which exists in the innermost core be core part resin.
• the core-shell resin particles (A) have, for example, 2 to 18 carbon atoms in the presence of an emulsion of a vinyl-based polymer (shell part resin) formed by polymerizing a monomer mixture containing an ionic monomer or the like as described later.
• the acid value of the core-shell resin particles (A) is the acid value of the entire resin constituting the core portion and the shell portion, and from the viewpoint of improving storage stability and adhesion to a substrate, 50 mg KOH / g or more and 100 mg KOH / g It is below.
• the acid value of the core-shell resin particles (A) can be calculated from the mass ratio of the constituting monomers. Further, the core-shell type resin particles can be dissolved or swollen in a suitable organic solvent (for example, methyl ethyl ketone), and measured in accordance with the neutralization titration method of JIS K 0070.
• the resin of the shell portion of the core-shell resin particles (A) is not particularly limited, and examples thereof include condensation resins such as polyester and polyurethane, and vinyl polymers.
• vinyl polymers obtained by addition polymerization of vinyl monomers are preferable from the viewpoint of improving storage stability and adhesion to substrates, and acrylic polymers are more preferable.
• the vinyl polymer may be appropriately synthesized, or a commercially available product may be used.
• the shell resin may be either a water-soluble polymer or a water-insoluble polymer, but a water-soluble polymer is preferable from the viewpoint of improving storage stability and adhesion to a substrate.
• water-soluble means that it becomes transparent when the polymer is dispersed in water. Specifically, when the polymer is dried at 105 ° C. for 2 hours and dissolved to 100 g of ion-exchanged water at 25 ° C., the dissolved amount is 10 g or more. .
• the acid value of the shell resin is preferably 100 mg KOH / g or more, more preferably 120 mg KOH / g or more, and preferably 280 mg KOH / g or less, more preferably 250 mg KOH / g from the viewpoint of improving the adhesion to the substrate. It is below.
• the shell resin when it is a vinyl polymer, in particular an acrylic polymer, it preferably contains (a) a constituent unit derived from an ionic monomer (hereinafter also referred to as “component (a)”), and further (b) hydrophobic At least one selected from structural units derived from a hydrophobic monomer (hereinafter also referred to as “component (b)”) and structural units derived from a hydrophilic nonionic monomer (c) (hereinafter referred to as “component (c)”) Is more preferable, and a polymer containing a constituent unit derived from the component (a) and a constituent unit derived from the component (b) is more preferable.
• component (a) ionic monomer
• component (c) hydrophilic nonionic monomer
• the shell part resin contains, for example, a component (a) and, if necessary, a monomer mixture containing one or more selected from the components (b) and (c) or the component (a) and the component (b).
• the monomer mixture (hereinafter, also referred to as "monomer mixture”) can be obtained by addition polymerization by a known method.
• the ionic monomer is used as a monomer component of a polymer from the viewpoint of improving the dispersion stability of the resin particle (A).
• an ionic monomer an anionic monomer and a cationic monomer are mentioned, An anionic monomer is preferable.
• an anionic monomer a carboxylic acid monomer, a sulfonic acid monomer, a phosphoric acid monomer etc. are mentioned.
• carboxylic acid monomers having a carboxy group are preferable from the viewpoint of improving the dispersion stability of the resin particles (A), and acrylic acid, methacrylic acid, crotonic acid, itaconic acid, maleic acid, fumaric acid Citruconic acid, 2-methacryloyloxymethylsuccinic acid and the like are more preferable, and one or more selected from acrylic acid and methacrylic acid are more preferable.
• the cationic monomer include N, N-dimethylaminoethyl methacrylate, N, N-dimethylaminoethyl acrylamide and the like.
• the (a) ionic monomers include monomers that become ions under acidic or alkaline conditions, even monomers that are not neutral ions, such as acids and amines.
• hydrophobic monomer is preferably used as a monomer component of a polymer from the viewpoint of improving the dispersion stability of the resin particle (A).
• hydrophobic monomers include alkyl (meth) acrylates and aromatic group-containing monomers.
• the alkyl (meth) acrylate is preferably one having an alkyl group having 1 to 22 carbon atoms, preferably 6 to 18 carbon atoms, and examples thereof include methyl (meth) acrylate, ethyl (meth) acrylate and (iso) propyl (meth) acrylate.
• (iso or tertiary)” and “(iso)” mean both the case where these groups exist, and the case where they do not exist, and when these groups do not exist, they show a normal.
• (meth) acrylate shows an acrylate and / or a methacrylate.
• the aromatic group-containing monomer is preferably a vinyl monomer having an aromatic group having 6 to 22 carbon atoms, which may have a substituent containing a hetero atom, and a styrenic monomer, and an aromatic group-containing (meth) Acrylate is more preferred.
• the styrene monomer is preferably one or more selected from styrene, 2-methylstyrene, divinylbenzene and the like, with styrene being more preferred.
• the aromatic group-containing (meth) acrylate is preferably at least one selected from benzyl (meth) acrylate, phenoxyethyl (meth) acrylate and the like, and more preferably benzyl (meth) acrylate.
• hydrophilic nonionic monomer can be used as a monomer component of a polymer from the viewpoint of improving the dispersion stability of the resin particle (A).
• hydrophilic nonionic monomers include NK esters M-20G, 40G, 90G, 230G, etc. of Shin-Nakamura Chemical Co., Ltd., and BLEMMER PE of NOF Corporation. -90, 200, 350, PME-100, 200, 400, etc., PP-500, 800, 1000, etc. AP-150, 400, 550, etc., 50 PEP-300, 50 POEP-800 B, 43 PAPE-600B and the like.
• the above components (a) to (c) can be used alone or in combination of two or more.
• the polymer used in the present invention may contain a structural unit derived from another monomer other than the components (a) to (c) as long as the effects of the present invention are not impaired.
• composition of each component or each constituent unit in the monomer mixture or in the polymer Content in a monomer mixture containing (a) component and at least one selected from (b) component and (c) component as needed at the time of shell part resin production (content as unneutralized amount)
• content of the constituent unit derived from each component in the shell part resin is as follows from the viewpoint of improving storage stability and adhesion to a substrate.
• the content of the (a) ionic monomer is preferably 3% by mass or more, more preferably 5% by mass or more, still more preferably 8% by mass or more, and preferably 60% by mass or less, more preferably 50% by mass %, More preferably 40% by mass or less.
• the content of the (b) hydrophobic monomer is preferably 20% by mass or more, more preferably 40% by mass or more, still more preferably 50% by mass or more, and preferably 95% by mass or less, more preferably 90% by mass. % Or less, more preferably 85% by mass or less.
• the hydrophilic nonionic monomer When the hydrophilic nonionic monomer is contained, its content is preferably 5% by mass or more, more preferably 10% by mass or more, still more preferably 20% by mass or more, and preferably 60% by mass The content is more preferably 55% by mass or less, still more preferably 50% by mass or less.
• the shell resin can be produced by copolymerizing a monomer mixture by a known polymerization method.
• a solution polymerization method is preferable.
• the organic solvent used in the solution polymerization method is not particularly limited, but is preferably a polar organic solvent such as aliphatic alcohol having 1 to 3 carbon atoms, ketones having 3 to 8 carbon atoms, ethers and esters, specifically methanol Ethanol, acetone, methyl ethyl ketone are mentioned, and methyl ethyl ketone is more preferable.
• a polymerization initiator or a polymerization chain transfer agent can be used, but as the polymerization initiator, an azo compound is preferable, and 4,4′-azobis (4-cyanovaleric acid), 2,2 ′ -Azobis (2,4-dimethyl valeronitrile) and the like are more preferable.
• the polymerization chain transfer agent mercaptans are preferable, and 3-mercaptopropionic acid, 2-mercaptoethanol and the like are more preferable.
• the polymerization temperature is preferably 50 ° C. to 90 ° C.
• the polymerization time is preferably 1 hour to 20 hours.
• the polymerization atmosphere is preferably a nitrogen gas atmosphere or an inert gas atmosphere such as argon.
• the shell resin is preferably used as a polymer solution as it is without removing the solvent used for the polymerization reaction from the viewpoint of improving the productivity of the resin particle dispersion.
• the solid content concentration of the polymer solution is preferably 20% by mass or more, more preferably 25% by mass or more, still more preferably 30% by mass or more, from the viewpoint of improving the productivity of the resin particle dispersion. Is 70% by mass or less, more preferably 65% by mass or less, still more preferably 60% by mass or less.
• the solid content concentration of the polymer solution is measured by the method described in the examples.
• a neutralizing agent may be used to neutralize anionic groups in the polymer.
• a neutralizing agent it is preferable to neutralize so that pH may be 7 or more and 11 or less.
• the neutralizing agent include alkali metal hydroxides, ammonia, organic amines and the like.
• the alkali metal hydroxide include lithium hydroxide, sodium hydroxide, potassium hydroxide and cesium hydroxide.
• organic amines include trimethylamine, ethylamine, diethylamine, triethylamine, triethanolamine and the like.
• the neutralizing agent is preferably an alkali metal hydroxide such as sodium hydroxide or ammonia, more preferably sodium hydroxide, from the viewpoint of improving storage stability and adhesion to a substrate.
• the neutralizing agent is preferably used as an aqueous neutralizing agent solution from the viewpoint of promoting the neutralization sufficiently and uniformly.
• the concentration of the neutralizing agent aqueous solution is preferably 3% by mass or more, more preferably 10% by mass or more, further preferably 15% by mass or more, and preferably 30% by mass or less, 25% by mass The following are more preferable.
• the degree of neutralization of the anionic group of the polymer is preferably 30 mol% or more, more preferably 40 mol% or more, and still more preferably 50 mol% or more, from the viewpoint of improving storage stability and adhesion to a substrate.
• the degree of neutralization is the molar equivalent of the neutralizing agent divided by the molar amount of the anionic group of the polymer.
• the weight average molecular weight of the polymer of the shell resin is preferably 6,000 or more, more preferably 8,000 or more, and still more preferably 10,000 or more, from the viewpoint of improving the dispersion stability of the resin particles (A). And preferably 300,000 or less, more preferably 200,000 or less, still more preferably 100,000 or less, still more preferably 50,000 or less.
• the measurement of a weight average molecular weight can be performed by the method as described in an Example.
• vinyl polymer for example, “John Krill 61”, “Jong Krill 67”, “Jong Krill 611”, “Jong Krill 678”, “Jong Krill 680”, “Jong Krill 690”, “Jong Krill” And styrene-acrylic acid copolymers such as BASF Japan Ltd., and polyacrylic acids such as "Aron AC-10SL” (manufactured by Toagosei Co., Ltd.).
• the core resin is configured to constitute the core resin as a structural unit derived from a (meth) acrylate having a hydrocarbon group having 2 to 18 carbon atoms.
• a (meth) acrylate having a hydrocarbon group having 2 to 18 carbon atoms In the unit, it is a resin having 40% by mass or more, preferably 70% by mass or more, more preferably 90% by mass or more, and still more preferably 100% by mass.
• the hydrocarbon group having 2 to 18 carbon atoms may contain a hetero atom such as an oxygen atom or a nitrogen atom.
• the hydrocarbon group having 2 to 18 carbon atoms is preferably 3 or more carbon atoms, more preferably 4 or more carbon atoms, and preferably 12 or less carbon atoms, and 8 or less carbon atoms More preferable.
• the hydrocarbon group having 2 to 18 carbon atoms is preferably at least one selected from a benzyl group and a 2-ethylhexyl group.
• the core resin is a concentration point of the stress of the resin particles (A). Therefore, from the viewpoint of stress relaxation, its glass transition temperature is preferably 80 ° C. or less, more preferably 70 ° C. or less, still more preferably 60 ° C. or less More preferably, the temperature is 50 ° C. or less.
• the acid value of the core resin is preferably 50 mg KOH / g or less, more preferably 30 mg KOH / g or less, still more preferably 10 mg KOH / g or less, still more preferably 0 mg KOH / g from the viewpoint of improving the adhesion to the substrate. .
• an alkyl group and an aryl group are preferable.
• a hydrocarbon group having 2 to 18 carbon atoms from the viewpoint of adhesion to a substrate, a butyl group, an isobutyl group, a tert-butyl group, a hexyl group, an octyl group, a 2-ethylhexyl group, an octyl group, an octadecyl group, and a benzyl group
• One or more selected from a group are preferable, and one or more selected from a butyl group, an isobutyl group, a tert-butyl group, a hexyl group, an octyl group, a 2-ethylhexyl group and a benzyl group is more preferable.
• the (meth) acrylic acid ester is at least one selected from acrylic acid esters and methacrylic acid esters, and from the viewpoint of adhesion to a substrate, acrylic acid esters are preferable.
• (meth) acrylic acid ester having a hydrocarbon group having 2 to 18 carbon atoms ethyl (meth) acrylate, propyl (meth) acrylate, isopropyl (meth) acrylate, butyl (meth) acrylate, isobutyl (meth) acrylate , Pentyl (meth) acrylate, hexyl (meth) acrylate, heptyl (meth) acrylate, octyl (meth) acrylate, 2-ethylhexyl (meth) acrylate, octadecyl (meth) acrylate, benzyl (meth) acrylate and the like The above is mentioned.
• butyl (meth) acrylate preferably butyl (meth) acrylate, isobutyl (meth) acrylate, pentyl (meth) acrylate, hexyl (meth) acrylate, heptyl (meth) acrylate, octyl (meth) acrylate, 2-ethylhexyl (meth) acrylate,
• benzyl (meth) acrylate and the like more preferably one or more selected from 2-ethylhexyl (meth) acrylate and benzyl (meth) acrylate.
• the method for producing the core-shell type resin particles (A) used in the present invention is not particularly limited.
• a shell resin emulsion and an aqueous medium are mixed, a monomer for the core resin is added thereto, and raised while stirring.
• the method is warmed, and then a water-soluble polymerization initiator is dropped and reacted to obtain a core-shell type resin particle (A).
• a water-soluble polymerization initiator is dropped and reacted to obtain a core-shell type resin particle (A).
• formation of particle nuclei is confirmed by change of color in the reaction vessel and the like, and then monomer for core part resin is further dropped and reaction is continued to obtain target core-shell type resin particles (A). You can get it.
• the monomer for core part resin may be dropped directly into the reaction vessel, or may be dropped after being previously emulsified in an aqueous medium.
• the shell resin acts as a protective colloid in the aqueous medium and stabilizes the resulting particle core (core).
• the emulsion of the core-shell resin particles (A) obtained by this method is excellent in printability because it has a viscosity close to that of the Newtonian.
• the composition of the core portion resin monomer in stages, it is possible to manufacture a core portion having a plurality of phases and a core portion in which the composition continuously changes from the innermost core.
• the aqueous medium used in the above-mentioned production method means a medium in which water is the largest proportion.
• water-soluble polymerization initiators can be used.
• inorganic peroxides such as potassium persulfate, sodium persulfate, ammonium persulfate, hydrogen peroxide and the like
• azo initiators such as 2,2'-azobis (2-amidinopropane) dihydrochloride and further peroxide compounds
• a redox initiator in which a reducing agent such as sodium sulfite is combined.
• a surfactant can be used in the polymerization.
• the surfactant may, for example, be a nonionic surfactant, an anionic surfactant or a cationic surfactant.
• a nonionic surfactant is preferred.
• the polymerization temperature is preferably 50 ° C. to 90 ° C.
• the polymerization time is preferably 1 hour to 20 hours.
• the polymerization atmosphere is preferably a nitrogen gas atmosphere or an inert gas atmosphere such as argon.
• the core-shell type resin particles (A) are preferably used as an emulsion of resin particles (A) containing water as a main dispersion medium, without removing the solvent used for the polymerization reaction, from the viewpoint of compounding ability to aqueous ink .
• the mass ratio [(a1) / (a2)] of the core resin (a1) to the resin (a2) corresponding to the shell other than the core resin is preferably 1 or more. , More preferably 1.1 or more, still more preferably 1.2 or more, and preferably 2 or less, more preferably 1.7 or less, still more preferably 1.5 or less, still more preferably 1.35 or less It is.
• the acid value of the core-shell resin particles (A) is 50 mgKOH / g or more and 100 mgKOH / g or less from the viewpoint of improving storage stability and adhesion to a substrate.
• the acid value is preferably 55 mg KOH / g or more, more preferably 60 mg KOH / g or more, further preferably 65 mg KOH / g or more, and preferably 150 mg KOH / g or less, more preferably 130 mg KOH / g or less, still more preferably It is 110 mg KOH / g or less, more preferably 90 mg KOH / g or less.
• the acid value of the core-shell resin particles (A) is the acid value of the entire resin constituting the core portion and the shell portion.
• the average particle diameter of the core-shell type resin particles (A) in the emulsion is preferably 10 nm or more, more preferably 20 nm or more, still more preferably 40 nm or more, from the viewpoint of improving storage stability and adhesion to substrate. Preferably it is 150 nm or less, More preferably, it is 120 nm or less, More preferably, it is 100 nm or less.
• the average particle size in the emulsion is measured by the method described in the examples.
• the solid content concentration of the emulsion of the core-shell resin particles (A) is preferably 15% by mass or more, more preferably 20% by mass or more, and still more preferably 25% by mass or more, from the viewpoint of the blending property to the aqueous ink. And preferably it is 60% by mass or less, more preferably 50% by mass or less, still more preferably 40% by mass or less.
• the solid content concentration of the emulsion is measured by the method described in the examples.
• the glycol ether (B) is used to plasticize the core-shell resin particles (A) in order to improve the adhesion to a substrate.
• the carbon number of the hydrocarbon group in the ether portion of the glycol ether (B) is 2 or more and 8 or less in view of plasticizing the resin particle (A) more effectively.
• As said hydrocarbon group although a linear or branched alkyl group, an alkenyl group, an aryl group etc. are mentioned, an alkyl group and an aryl group are preferable.
• the carbon number of the alkyl group is preferably 3 or more, more preferably 4 or more, and preferably 6 or less.
• the boiling point of the glycol ether (B) is preferably 110 ° C. or more.
• the boiling point is more preferably 115 ° C. or more, still more preferably 120 ° C. or more, still more preferably 130 ° C. or more, and preferably 290 ° C. or less, more preferably 280 ° C. or less, further preferably 275 ° C. or less
• the temperature is more preferably 260 ° C. or less, still more preferably 230 ° C. or less.
• the boiling point represents a standard boiling point (boiling point at 1 atm). When two or more glycol ethers are used, the boiling point of the glycol ether is a weighted average value weighted by the content (mass%) of each glycol ether.
• the SP value (solubility parameter) of the glycol ether (B) is preferably 18 (J / cm 3 ) 0.5 or more, more preferably 19 (J / cm 3 ) from the viewpoint of improving the adhesion to the substrate.
• alkylene glycol mono such as monoalkylene glycol monoalkyl ether, dialkylene glycol monoalkyl ether, trialkylene glycol monoalkyl ether, etc. in which the carbon number of the hydrocarbon group in the ether part is 2 or more and 8 or less
• alkylene glycol dialkyl ethers such as alkyl ethers, monoalkylene glycol dialkyl ethers, and dialkylene glycol dialkyl ethers.
• the alkylene glycols include ethylene glycol and propylene glycol, with ethylene glycol being preferred.
• the glycol ether (B) has at least one hydrocarbon group having 2 to 8 carbon atoms.
• alkylene glycol monoalkyl ether ethylene glycol monoisopropyl ether (boiling point: 142 ° C., SP value: 22.3 (J / cm 3 ) 0.5 ) (hereinafter, in this paragraph, “° C.” represents a boiling point, Units of SP value omitted), ethylene glycol monobutyl ether (171 ° C., SP value: 20.8), ethylene glycol monoisobutyl ether (161 ° C., SP value: 18.6), ethylene glycol monohexyl ether (208 ° C.) , SP value: 20.3), etc .; diethylene glycol monoethyl ether (202 ° C., SP value: 22.2), diethylene glycol monoisopropyl ether (207 ° C., SP value: 20.3), diethylene glycol mono Butyl ether (231 Diethylene glycol monoalkyl ether such as diethylene glycol monoisobutyl ether (220 °
• alkylene glycol monoalkyl ether is preferable, and ethylene glycol monoisopropyl ether, ethylene glycol monobutyl ether, ethylene glycol monoisobutyl ether, ethylene glycol hexyl ether, diethylene glycol monoethyl ether,
• ethylene glycol monobenzyl ether is more preferable, ethylene glycol monobutyl ether, ethylene glycol monoisobu Ether, ethylene glycol hexyl ether, diethylene glycol monoethyl ether, diethylene glycol monoisopropyl ether, diethylene glycol monobutyl ether, diethylene glycol monoisobutyl
• the resin particle dispersion of the present invention can contain other water-soluble organic solvents other than glycol ether (B).
• other water-soluble organic solvents include polyhydric alcohols having a valence of 2 or more, such as alcohols and glycols, pyrrolidone, alkanolamines and the like, with preference given to glycols from the viewpoint of substrate adhesion.
• glycols include ethylene glycol, 1,2-propanediol, 1,2-butanediol, 1,2-hexanediol, 1,3-propanediol, 1,3-butanediol, diethylene glycol, etc.
• An alkanediol having 3 or more and 4 or less carbon atoms, such as 2, 2-propanediol and diethylene glycol is preferable.
• the resin particle dispersion of the present invention can contain a pigment.
• a pigment white pigments such as titanium oxide, black pigments such as carbon black, azo pigments, diazo pigments, phthalocyanine pigments, quinacridone pigments, isoindolinone pigments, dioxazine pigments, perylene pigments, perinone pigments, thioindigo pigments, anthraquinone And pigments and chromatic pigments such as quinophthalone pigments.
• the present invention is particularly useful in the case of using a titanium oxide pigment which is frequently used as a pigment for background color from the viewpoint of adhesion to a substrate.
• titanium oxide The crystal structure of titanium oxide includes rutile type (tetragonal crystal), anatase type (tetragonal crystal) and brookite type (orthogonal crystal), but from the viewpoint of crystal stability, concealability and availability, the present invention
• rutile type titanium oxide hereinafter, also simply referred to as "titanium oxide”
• titanium oxide can be produced by a vapor phase method or a liquid phase method, titanium oxide produced by a vapor phase method is more preferable because a high crystallinity can be easily obtained.
• an untreated thing can also be used for a titanium oxide
• the thing by which surface treatment was carried out from a viewpoint of sealing photocatalytic activity and a viewpoint of obtaining favorable dispersibility is preferable.
• the surface treatment of titanium oxide include surface treatment with an inorganic substance and surface treatment with an organic substance such as a titanium coupling agent and a silane coupling agent, but surface treatment with an inorganic substance is preferable.
• a surface treatment method of titanium oxide with an inorganic substance a method of treating with at least one selected from alumina (Al 2 O 3 ), silica (SiO 2 ), zinc oxide (ZnO), zirconia (ZrO 2 ), etc. is more preferable. preferable.
• the powder of the surface-treated titanium oxide can be sintered at 800 to 1000 ° C. to suppress sintering between particles and improve the fluidity and dispersibility of secondary particle size.
• the particle shape of titanium oxide is not particularly limited because it is granular or needle-like, but the average primary particle diameter is preferably 40 nm or more, more preferably 100 nm or more, in terms of the whiteness, the arithmetic mean of the major diameters of primary particles. It is more preferably 150 nm or more, still more preferably 200 nm or more, and preferably 350 nm or less, more preferably 500 nm or less, still more preferably 400 nm or less from the viewpoint of hiding power.
• the average primary particle diameter of a titanium oxide is an arithmetic mean of the major axis of a primary particle, and is measured by the method as described in an Example.
• Examples of commercially available products of rutile type titanium dioxide include: trade name of Ishihara Sangyo Co., Ltd .: Typek R, CR, PF series, trade name of Sakai Chemical Industry Co., Ltd .: trade name of R series, trade name of Taika Co., Ltd .: JR , MT series, trade name made by titanium industry Co., Ltd .: KURONOS KR series, trade name made by huntsmann: TR series, etc.
• the titanium oxide is preferably blended in the resin particle dispersion of the present invention as a titanium oxide dispersion.
• the polymer dispersant for dispersing titanium oxide is not particularly limited, but the same polymer as the shell resin of the core-shell resin particles (A), that is, a polymer containing a constituent unit derived from (a) an ionic monomer And more preferably a polymer containing one or more selected from (b) a structural unit derived from a hydrophobic monomer, and (c) a structural unit derived from a hydrophilic nonionic monomer, (a) a polymer derived from an ionic monomer More preferred are polymers containing a structural unit and a structural unit derived from (c) a hydrophilic nonionic monomer.
• the content of the constituent unit derived from the component (a) in all the constituent units of the polymer dispersant is preferably 5% by mass or more, more preferably 10% by mass or more, still more preferably It is 15% by mass or more, and preferably less than 35% by mass, more preferably less than 30% by mass, and still more preferably less than 25% by mass.
• the content of the constituent unit derived from the component (c) in all constituent units of the polymer dispersant is preferably 65% by mass or more, more preferably 70% by mass or more, still more preferably 75% by mass from the same viewpoint as above.
• the above is preferable, and it is preferably less than 95% by mass, more preferably less than 90% by mass, and still more preferably less than 85% by mass.
• the method for producing the polymer dispersant is the same as the method for producing the shell resin.
• the titanium oxide dispersion can be obtained by subjecting a mixture containing titanium oxide, a polymer dispersant, and an aqueous medium (hereinafter, also referred to as “titanium oxide mixture”) to a dispersion process.
• the aqueous medium refers to a medium containing water as a main component.
• organic solvents other than water aliphatic alcohols having 1 to 4 carbon atoms, ketones having 3 to 8 carbon atoms, ethers such as ethyl ether, propyl ether, butyl ether and tetrahydrofuran, esters such as methyl acetate and ethyl acetate Etc.
• the solvent used in the polymerization may be used as it is.
• the content of water in the titanium oxide dispersion is preferably 60% by mass or more, more preferably 70% by mass or more, and preferably 100% by mass or less, from the viewpoint of environmental friendliness.
• the pH is 7 or more, preferably 7.5 or more, more preferably 8.5 or more, and preferably 13 or less. Preferably, it is 11 or less.
• the neutralizing agent is the same as described above, preferably an alkali metal hydroxide, more preferably an aqueous solution of sodium hydroxide, potassium hydroxide or the like.
• the dispersion method for obtaining the titanium oxide dispersion is not particularly limited, but preferably the titanium oxide mixture is predispersed, and then shear stress is further applied to carry out the main dispersion to obtain an average particle diameter of titanium oxide particles as desired. Control to achieve the particle size is preferred.
• an anchor wing, a disper wing, etc. may be mentioned.
• the dispersing means include kneaders such as a roll mill and a kneader, high pressure homogenizers such as a microfluidizer (manufactured by Microfluidics), and media type dispersing machines such as a paint shaker and a bead mill.
• the pigment can be controlled to have a desired particle size by controlling the treatment pressure and the number of passes.
• the average particle diameter of the titanium oxide particles in the titanium oxide dispersion is 150 nm or more, preferably 180 nm or more, more preferably 200 nm or more, and 700 nm or less, preferably 600 nm or less, from the viewpoint of printing concentration. More preferably, it is 500 nm or less.
• the average particle size of the titanium oxide dispersion is measured by the method described in the examples.
• the solid content concentration (non-volatile component concentration) of the titanium oxide dispersion is preferably 20% by mass or more, more preferably 30% by mass or more, and preferably 70% by mass or less, more preferably from the viewpoint of dispersion stability. Is 60 mass% or less.
• the solid content concentration of a dispersion of a pigment such as titanium oxide is measured by the method described in the examples.
• Content of each component in the resin particle dispersion of this invention is as follows from a viewpoint of improving storage stability and base-material adhesiveness.
• the content of the core-shell resin particles (A) in the resin particle dispersion is preferably 5% by mass or more, more preferably 10% by mass or more, still more preferably 15% by mass or more, and preferably 50% by mass
• the content is more preferably 40% by mass or less, still more preferably 35% by mass or less.
• the content of glycol ether (B) in the resin particle dispersion is 2.8% by mass or more, preferably 3% by mass or more, more preferably 3.5% by mass or more, still more preferably 4.2% by mass
• the content is more preferably 5% by mass or more, and preferably 30% by mass or less, more preferably 20% by mass or less, still more preferably 10% by mass or less, still more preferably 7% by mass or less.
• a water-soluble organic solvent other than glycol ether (B) is used, the content thereof is preferably 15% by mass or less, more preferably 10% by mass or less, still more preferably 5% by mass or less in the resin particle dispersion.
• it is 0.2 mass% or more, More preferably, it is 0.5 mass% or more, More preferably, it is 0.8 mass% or more.
• the content of the pigment in the resin particle dispersion is preferably 2% by mass or more, more preferably 4% by mass or more, still more preferably 6% by mass or more, and preferably 50% by mass from the viewpoint of printing density.
• the content is preferably 40% by mass or less, more preferably 30% by mass or less.
• the mass ratio of the pigment to the core-shell resin particles (A) [pigment / core-shell resin particles (A)] is preferably 0.3 or more, more preferably 0.5 or more, still more preferably 0 from the viewpoint of printing density. And preferably not more than 4, more preferably not more than 3, and still more preferably not more than 2.
• the content of water in the resin particle dispersion is preferably 30% by mass or more, more preferably 40% by mass or more, still more preferably 45% by mass or more, still more preferably 50% by mass or more from the viewpoint of environmental load reduction. And preferably 80% by mass or less, more preferably 75% by mass or less, still more preferably 70% by mass or less.
• the mass ratio [water / (B)] of the content of water to the content of glycol ether (B) in the resin particle dispersion is preferably 0.5 or more, more preferably 1 or more, and still more preferably 1. It is 2 or more, more preferably 2.4 or more, and preferably 100 or less, more preferably 40 or less, still more preferably 15 or less, still more preferably 12.5 or less.
• the resin particle dispersion containing a pigment can be used as an ink as it is.
• the resin particle dispersion of the present invention can be used as an aqueous ink such as an inkjet ink and an ink for flexographic printing, but is preferably used as an aqueous ink for gravure printing.
• the aqueous ink for gravure printing further contains a surfactant, an organic solvent other than glycol ether (B), and a humectant, a wetting agent, a wetting / penetrating agent, a dispersing agent, a viscosity modifier, and an antifoaming agent. It can be prepared by mixing various additives such as an agent, an antiseptic agent, an antifungal agent, an antirust agent and the like.
• the contents of the core-shell resin particles (A), the glycol ether (B), the pigment, and the water in the aqueous ink for gravure printing are basically the same as the contents in the resin particle dispersion.
• the content of water in the aqueous ink for gravure printing is preferably 20% by mass or more, more preferably 30% by mass or more, still more preferably 40% by mass or more, and preferably 80% by mass or less, more preferably It is 75% by mass or less, more preferably 65% by mass or less.
• the mass ratio [water / (B)] of the content of water to the content of glycol ether (B) in the aqueous ink is preferably 0.5 or more, more preferably 1 or more, still more preferably 2 or more, More preferably, it is 2.3 or more, and preferably 100 or less, more preferably 65 or less, still more preferably 25 or less.
• surfactant which can be used, anionic surfactant, nonionic surfactant, amphoteric surfactant, etc. are mentioned. Among these, nonionic surfactants are preferable, and acetylene glycol surfactants are more preferable.
• acetylene glycol surfactants 2,4,7,9-tetramethyl-5-decyne-4,7-diol, 3,6-dimethyl-4-octin-3,6-diol, and 2,5 And one or more acetylene glycols selected from -dimethyl-3-hexyne-2,5-diol, and ethylene oxide adducts of the acetylene glycols.
• acetylene glycol surfactants include Surfynol 104 (2,4,7,9-Tetramethyl-5-decyne-4,7-diol, HLB: 3.0) available from Air Products & Chemicals, Inc.
• 104E diethylene glycol 50% dilution of 2,4,7,9-tetramethyl-5-decyne-4,7-diol
• 104PG-50 (2,4,7,9-tetramethyl-5-) Desicin-4,7-diol in 50% propylene glycol
• Surfynol 420 EO average 1.3 mol adduct of 2,4,7,9-tetramethyl-5-decin-4,7-diol, HLB: 4.7
• Acetylenol E13T (EO average added mole number: 1.3, HLB: 4.7) manufactured by Kawaken Fine Chemical Co., Ltd., and the like.
• the pH of the aqueous ink for gravure printing is preferably 5.5 or more, more preferably 6.0 or more, still more preferably 6.5 or more from the viewpoint of storage stability, and preferably from the viewpoint of skin irritation. Is 11.0 or less, more preferably 10.0 or less, still more preferably 9.5 or less.
• the printing substrate to which the aqueous ink for gravure printing is applied include high water absorbing plain paper, low water absorbing coated paper and a resin film.
• coated paper general purpose glossy paper, multi-color foam gloss paper and the like can be mentioned, and as resin film, polyester film, polyvinyl chloride film, polypropylene film, polyethylene film and the like can be mentioned.
• the aqueous ink for gravure printing of the present invention is preferably used for printing in which the printing substrate is a resin film, from the viewpoint of excellent substrate adhesion.
• the resin film may be a biaxially stretched film, a uniaxially stretched film, or a non-stretched film, more preferably a polyester film or a stretched polypropylene film, a corona discharge treated polyethylene terephthalate (PET) film, a corona discharge treated film Axially oriented polypropylene (OPP) films are more preferred.
• the average primary particle size of titanium oxide is 500 titanium oxides by image analysis using a transmission electron microscope “JEM-2100” (manufactured by JEOL Ltd.) Primary particles were extracted, their particle sizes were measured, and their averages were calculated as number average particle sizes. In addition, when there were a major axis and a minor axis in titanium oxide, it was calculated using the major axis.
• Solid content concentration 100-wet base water content of aqueous dispersion (% by weight) (4-2) Measurement of solid content concentration of polymer solution and pigment dispersion
• 10.0 g of sodium sulfate which has been made constant in a desiccator was weighed, and After 1.0 g of sample was added and mixed, it was accurately weighed and maintained at 105 ° C. for 2 hours to remove volatiles, and further left for 15 minutes in a desiccator to measure its mass.
• the mass of the sample after devolatilization was regarded as solid content, and was divided by the mass of the added sample to obtain solid concentration.
• ⁇ Evaluation method> Evaluation of storage stability About the water-based ink (resin particle dispersion), the time-dependent change on 40 degreeC and the conditions of 1 week was evaluated. 50 ml of ink was sealed in a glass bottle, phase separation and presence or absence of gelation were observed, and storage stability was evaluated based on the following criteria. (Evaluation criteria) A: No change in ink observed. B: The ink causes phase separation, but it returns when shaken by hand. C: The ink causes phase separation to gel and does not return even if it is shaken by hand. If it is evaluation B or more, it is practicable.
• Production Example 1 (Production of Polymer Dispersant for Dispersing Titanium Oxide)
• a 2 L glass reaction vessel equipped with a dropping funnel 182 g of water was charged, and the temperature was raised to 80 ° C. under a nitrogen atmosphere.
• methoxypolyethylene glycol monomethacrylate (ethylene oxide (EO) average added mole number n 23, manufactured by Shin-Nakamura Chemical Co., Ltd., trade name “NK ester M-230G”) 314 as a dropping solution 1 314.
• EO ethylene oxide
• Production Example 2 (Production of titanium oxide dispersion) A mixture of 6 g of the polymer dispersant obtained in Production Example 1 and 2 g of ion-exchanged water and dissolved therein is charged into a 1000 mL polyethylene bottle, and titanium oxide (rutile type: manufactured by Ishihara Sangyo Kaisha, CR-80, Al ⁇ ⁇ 120 g of Si treatment, average primary particle diameter 250 nm, 88 g of ion-exchanged water were added, 1476 g of 2 mm zirconia beads were added, and dispersion treatment was performed for 10 hours at 250 rpm using a table-top pot mill stand (As One Corporation). After the completion of dispersion, the zirconia beads were removed using a mesh, and the solid concentration was adjusted with water to obtain a titanium oxide dispersion (solid concentration 50%) having an average particle diameter of 325 nm.
• titanium oxide rutile type: manufactured by Ishihara Sangyo Kaisha, CR-80, Al
• Production Example 3 (Production of Shell Polymer P1 Solution for Core-Shell Type Resin Particles) 24.2 parts of acrylic acid (reagent manufactured by Fuji Film Wako Pure Chemical Industries, Ltd.) and 75.8 parts of styrene (reagent manufactured by Fuji Film Wako Pure Chemical Industries, Ltd.) were mixed to prepare a monomer mixed solution. In a reaction vessel, 5 parts of methyl ethyl ketone (MEK), 2.5 parts of 3-mercaptopropionic acid (polymerization chain transfer agent), and 10% of the monomer mixture were added and mixed, and nitrogen gas substitution was sufficiently performed.
• MEK methyl ethyl ketone
• 3-mercaptopropionic acid polymerization chain transfer agent
• the dropping funnel the remaining 90% of the monomer mixture, 2.25 parts of the polymerization chain transfer agent, 75 parts of MEK, and an azo radical polymerization initiator (manufactured by Fujifilm Wako Pure Chemical Industries, Ltd., trade name: V- A mixed solution of 2.0 parts of 501,4,4'-azobis (4-cyanovaleric acid)) was added, and the temperature of the monomer mixture in the reaction vessel was raised to 77 ° C with stirring under a nitrogen atmosphere, and then dropped. The mixture in the funnel was dropped over 5 hours. After completion of the dropwise addition, a solution of 0.5 part of the above-mentioned polymerization initiator in 5 parts of MEK is added, allowed to react at 77 ° C. for 2 hours, and finally MEK is added to a solid content concentration of 55%. A P1 solution was obtained. The acid value of the polymer P1 was 180 mg KOH / g, and the weight average molecular weight was 16,000.
• a monomer mixed solution was prepared by mixing 17.5 parts of acrylic acid (reagent manufactured by Fuji Film Wako Pure Chemical Industries, Ltd.) and 82.5 parts of styrene (reagent manufactured by Fuji Film Wako Pure Chemical Industries, Ltd.). In a reaction vessel, 5 parts of methyl ethyl ketone (MEK), 2.5 parts of 3-mercaptopropionic acid (polymerization chain transfer agent), and 10% of the monomer mixture were added and mixed, and nitrogen gas substitution was sufficiently performed.
• MEK methyl ethyl ketone
• 3-mercaptopropionic acid polymerization chain transfer agent
• the dropping funnel the remaining 90% of the monomer mixture, 2.25 parts of the polymerization chain transfer agent, 75 parts of MEK, and an azo radical polymerization initiator (manufactured by Fujifilm Wako Pure Chemical Industries, Ltd., trade name: V- A mixed solution of 2.0 parts of 501,4,4'-azobis (4-cyanovaleric acid)) was added, and the temperature of the monomer mixture in the reaction vessel was raised to 77 ° C with stirring under a nitrogen atmosphere, and then dropped. The mixture in the funnel was dropped over 5 hours. After completion of the dropwise addition, a solution of 0.5 part of the above-mentioned polymerization initiator in 5 parts of MEK is added, allowed to react at 77 ° C. for 2 hours, and finally MEK is added to a solid content concentration of 55%. P2 solution was obtained. The acid value of the polymer P2 was 130 mg KOH / g, and the weight average molecular weight was 15,500.
• Example 1 Production of Core-Shell Type Resin Particle Emulsion
• 300 g of the emulsion EM1 obtained in Production Example 4 and 108.9 g of ion-exchanged water were charged, and further 2-ethylhexyl methacrylate while stirring (100 rpm).
• (Fujifilm Wako Pure Chemical Industries, Ltd., monomer for core part resin) 87.6g was added, and it heated up to 75 degreeC, stirring.
• 22.5 g of a 4% aqueous solution of potassium persulfate manufactured by Fujifilm Wako Pure Chemical Industries, Ltd. was gradually dropped over 90 minutes.
• Adecanol UH-420 0.5%, acetylene glycol surfactant (Air Products & Chemicals, Inc., Surfynol 420, ethylene of 2,4,7,9-tetramethyl-5-decyne-4,7-diol) 1% of oxide adduct (1%) was mixed with water to obtain an aqueous ink as a resin particle dispersion.
• the content of water was 61% by mass, and the mass ratio of the content of water to the content of diethylene glycol monoisobutyl ether (B) [water / (B)] was 15.
• Example 2 Comparative Example 1
• Example 2 Comparative Example 1
• the same procedure as in Example 1 is repeated except that the compound shown in Table 1 is used instead of 2-ethylhexyl methacrylate as a monomer for the core part resin in Example 1, and core-shell type resin particles having a solid content concentration of 30% An emulsion was obtained.
• Example 9 to 16 and Comparative Examples 2 to 4 The same procedure as in Example 1 is repeated except that the amount of 2-ethylhexyl methacrylate is changed to that shown in Table 1 and the amount thereof is changed to that shown in Table 1, and the solid content concentration is 30%. An emulsion of core-shell resin particles was obtained.
• Example 14 was carried out in the same manner as Example 14, except that 3% of diethylene glycol monoisobutyl ether and 1% of 1,2-propanediol in the aqueous ink were changed to the amounts shown in Table 2. The results are shown in Table 2.
• Example 14 is the same as Example 14 except that 3% of diethylene glycol monoisobutyl ether and 1% of 1,2-propanediol in the aqueous ink are changed to 5% of glycol ether (B) shown in Table 3 in Example 14. went. The results are shown in Table 3. In the obtained aqueous ink, the content of water was 61.5% by mass, and the mass ratio of the content of water to the content of glycol ether (B) [water / (B)] was 12.3. . Further, Table 4 shows a list of boiling points of solvents such as glycol ether used and SP values.

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