WO1997019993A1 - Acrylic emulsions useful in printing inks - Google Patents

Acrylic emulsions useful in printing inks Download PDF

Info

Publication number
WO1997019993A1
WO1997019993A1 PCT/US1996/018284 US9618284W WO9719993A1 WO 1997019993 A1 WO1997019993 A1 WO 1997019993A1 US 9618284 W US9618284 W US 9618284W WO 9719993 A1 WO9719993 A1 WO 9719993A1
Authority
WO
WIPO (PCT)
Prior art keywords
composition
isocyanate
group
monomer
polymer
Prior art date
Application number
PCT/US1996/018284
Other languages
French (fr)
Other versions
WO1997019993A9 (en
Inventor
George A. Smith
Shruti Singhal
Michael D. Mcdermott
Kartar S. Arora
Reuben H. Grinstein
Original Assignee
Henkel Corporation
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Henkel Corporation filed Critical Henkel Corporation
Publication of WO1997019993A1 publication Critical patent/WO1997019993A1/en
Publication of WO1997019993A9 publication Critical patent/WO1997019993A9/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING 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
    • C09D11/00Inks
    • C09D11/02Printing inks
    • C09D11/10Printing inks based on artificial resins
    • C09D11/106Printing inks based on artificial resins containing macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • C09D11/107Printing inks based on artificial resins containing macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds from unsaturated acids or derivatives thereof
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/02Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/10Esters
    • C08F220/34Esters containing nitrogen, e.g. N,N-dimethylaminoethyl (meth)acrylate
    • C08F220/36Esters containing nitrogen, e.g. N,N-dimethylaminoethyl (meth)acrylate containing oxygen in addition to the carboxy oxygen, e.g. 2-N-morpholinoethyl (meth)acrylate or 2-isocyanatoethyl (meth)acrylate

Definitions

  • the present invention relates to acrylic emulsions useful in printing inks, said acrylic emulsions being prepared by emulsion polymerization of acrylic monomers.
  • Flexible packaging printing inks are typically printed by rotary letterpress printing using flexible rubber plates or by gravure printing using engraved chrome-plated cylinders on a wide variety of substrates, e.g. plastic films such as cellulose acetate, polyethylene, polyethylene terephthalate, polyesters, polystyrene, cellophane, glassine, tissue, aluminum foils, liners, bags, paper labels, box coverings, gift wrappings, etc.
  • plastic films such as cellulose acetate, polyethylene, polyethylene terephthalate, polyesters, polystyrene, cellophane, glassine, tissue, aluminum foils, liners, bags, paper labels, box coverings, gift wrappings, etc.
  • Flexible packaging printing inks are widely used in the graphic arts industry. They offer economy, versatility, quality and simplicity and permit a roll of material to be multi-color printed in a continuous web at speeds of over 300 meters per minute and feed it directly to converting machines for slitting, forming or laminating
  • these inks must be carefully formulated so as to avoid the problems indigenous to these types of inks, e g chemical pinholing (failure of the ink to properly wet a plastic film surface), mechanical pinholing (the appearance of the pattern of the etched ink form roller), feathering (the appearance of stringy or ragged edges), mottle (ridged or speckled patterns), precipitation of part of the vehicle, blocking (a sticking or transfer of the image to the underside of the web), adhesion of the ink to the substrate, etc
  • U S Patent No 5,338,785 discloses a flexible packaging printing ink is formulated from a copolymer of polyethylene glycol methacrylate and a polyamide
  • U S Patent No 5,075,364 discloses a blend of a water- dissipatable polyester material, an acrylic polymer and a water-dissipatable vinyl polymer It is stated that the acrylic polymer and the vinyl polymer must be compatible with the polyester which has a particular composition It is stated that the polymer blends are useful for preparing ink compositions having improved block resistance, water resistance, and alcohol resistance
  • U S Patent No 4,921 899 discloses an ink composition containing a blend of a polyester, an acrylic polymer and a vinyl polymer The water-based inks containing the blend of these polymers as a binder can significantly improve ink film properties such as alcohol resistance, block resistance and water resistance as compared to use of water-dispersible polyester alone
  • the polymer blends were also employed to prepare ink primers and overprint varnishes It is stated that these polymer blends were prepared by mixing an aqueous polyester dispersion with an acrylic emulsion which contains surfactants and other additives and that the
  • U S Patent No 4,814,515 discloses compounds prepared by the reaction of a glycidyl (meth)acrylate with a hydroxyalkylated polyalkyleneoxy fatty alcohol followed by reaction with an alkylene oxide and the use of these compounds as an emulsifier in the emulsion or dispersion polymerization of ethylenically unsaturated monomers
  • U.S Patent No 4,390,401 discloses the use of acrylate or methacrylate esters of polyalkylene oxide derivatives of alkyl/aryl phenols as wetting agents and adhesion promoters in ultraviolet curable coating systems
  • the product when used as a primary or secondary emulsifier, provides low foaming emulsions with improved water resistance Summary of the Invention
  • This invention relates to an aqueous polymer emulsion composition
  • R 1 is hydrogen or methyl
  • R 2 is an alkylene group or substituted alkylene group (typically having less than six carbon atoms, more typically two or three carbon atoms)
  • R 3 is an alkylene group or substituted alkylene group (typically having less than ten carbon atoms, more typically from four to six carbon atoms),
  • R 4 is an aliphatic, aromatic, cycloaliphatic or heterocydic radical (i.e. the residue of an organic isocyanate, including trimerized isocyanates, but excluding isocyanate-functional prepolymers of active hydrogen compounds) having a functionality of n, n is an integer from two to four (typically two or three), x is an integer from one to three, and y is an integer from one to five.
  • the present invention also relates to printing inks comprising a colorant and a binder for said colorant comprising an aqueous emulsion polymer of this invention.
  • This invention also relates to a method of coating a substrate comprising (i) contacting a surface of a substrate with a composition comprising an ink as defined above, and (ii) drying said surface to form a film of the solids of said ink in contact with said surface.
  • this coating process is a printing process.
  • R 1 is hydrogen
  • R 2 is an ethylene group
  • R 3 is a pentamethylene group
  • R 4 is the residue of isophorone di-isocyanate (and n is two), tetramethylxylene di-isocyanate (and n is two), toluene di-isocyanate (and n is two), or trimerized hexamethylene di-isocyanate (and n is three)
  • x is one and y is two.
  • this oligomer is a polyester oligomer prepared by forming a mixture of an acrylate- or methacrylate-functional and mono-hydroxyl- functional polyester oligomer and an isocyanate. These two components of the mixture then react in the presence of a urethane catalyst. The resulting product should contain essentially no unreacted isocyanate functionality.
  • the monomer having the above formula can be characterized as an oligomer which is olefinically unsaturated.
  • These monomers are derived from hydroxy-functional lactone-modified acrylate or methacrylate acid esters (hereinafter "lactone-acrylate adducts") prepared by reacting an appropriate lactone with an acrylate or methacrylate acid ester which are in turn reacted with a polyisocyanate.
  • Lactones employed in the preparation of the lactone-acrylate adducts typically have the formula:
  • R is hydrogen or an alkyl group having from 1 to 12 carbon atoms
  • z is from 4 to 7 and at least (z - 2) of the R's is hydrogen.
  • Preferred lactones are the epsilon-caprolactones wherein z is 4 and at least 6 of the R's are hydrogen with the remainder, if any, being alkyl groups.
  • none of the substituents contain more than 12 carbon atoms and the total number of carbon atoms in these substituents on the lactone ring does not exceed 12.
  • Unsubstituted epsilon-caprolactone, i.e., where each R is hydrogen, is a derivative of 6-hydroxyhexanoic acid. Both the unsubstituted and substituted epsilon-caprolactones are available by reacting the corresponding cyclohexanone with an oxidizing agent such as peracetic acid.
  • Substituted epsilon-caprolactones found to be most suitable for preparing the present lactone-acrylate adducts are the various epsilon-monoalkylcaprolactones wherein the alkyl groups contain from 1 to 12 carbon atoms, e.g., epsilon-methyl-caprolactone, epsilon-ethyl-caprolactone, epsilon-propyl-caprolactone and epsilon-dodecyl-caprolactone.
  • epsilon-dialkylcaprolactones in which the two alkyl groups are substituted on the same or different carbon atoms, but not both on the omega carbon atoms.
  • epsilon-trialkylcaprolactones wherein 2 or 3 carbon atoms in the lactone ring are substituted provided, though, that the omega carbon atom is not di-substituted.
  • the most preferred lactone starting reactant is the epsilon-caprolactone wherein z in the lactone formula is 4 and each R is hydrogen.
  • the acrylate or methacrylate acid esters utilized to prepare the lactone-acrylate adducts contain from 1 to 3 acrylyl or alpha-substituted acrylyl groups and one or two hydroxyl groups. Such esters are commercially available and/or can be readily synthesized. Commercially available esters include the hydroxyalkyi acrylates or hydroxyalkyi methacrylates wherein the alkyl group contains from 2 to 10 carbon atoms, preferably from 2 to 6 carbon atoms.
  • the hydroxyalkyi acrylates and methacrylates have the following formula:
  • R 1 is hydrogen or methyl
  • x is an integer from 1 to 3
  • R 2 is a linear or a branched alkylene group having from 2 to 10 carbon atoms, preferably from 2 to 6 carbon atoms.
  • Suitable hydroxyalkyi acrylates and methacrylates include 2-hydroxyethyl acrylate, 2-hydroxypropyl acrylate, 2-hydroxyethyl methacrylate, 2-hydroxypropyl methacrylate, diethylene glycol monoacrylate, diethylene glycol monomethacrylate, glycerine dimethacrylate, trimethylol propane dimethacrylate, 3-hydroxypropyl acrylate, 2-hydroxybutyl acrylate, 4-hydroxybutyl acrylate, 3-hydroxypentyi acrylate, 6-hydroxynonyl acrylate, 2-hydroxyethyl methacrylate, 2-hydroxypropyl methacrylate, 3-hydroxypropyl methacrylate, 2-hydroxybutyl methacrylate, 2-hydroxypentyl methacrylate, 5-hydroxypentyl methacrylate, 7-hydroxyheptyl methacrylate and 5-hydroxydecyl methacrylate.
  • Preferred lactone-acrylate adducts have the formula:
  • CH 2 CR 1 -C(O)O-R 2 -(O-C(O)R 3 ) 2 -OH wherein R 1 , R 2 , and R 3 are as described above.
  • the lactone-acrylate adduct is prepared by reacting the lactone with the hydroxyalkyi acrylate in the presence of less than about 200 parts per million of a catalyst.
  • the catalysts which may be used include one or more organometallic compounds and other metallic compounds such as stannic chloride or ferric chloride and other Lewis or protonic acids.
  • Preferred catalysts include stannous octoate, dibutyltin dilaurate, and other tin compounds; titanates such as tetraisopropyl titanate and butyl titanate; and the like.
  • the reaction is carried out at a temperature of from about 10OX to about
  • the reaction may be carried out at atmospheric pressure, although higher or lower pressures may be used.
  • the reaction is generally carried out in the presence of oxygen to inhibit polymerization of the hydroxyalkyi acrylate.
  • the reaction is generally carried out for a period of from about 2 to about 20 hours.
  • the reaction is carried out in the presence of a suitable inhibitor to prevent polymerization of the hydroxyalkyi acrylate double bond.
  • a suitable inhibitor include the monomethyl ether of hydroquinone, benzoquinone, phenothiazine, methyl hydroquinone, 2,5-di-t-butylquinone, hydroquinone, benzoquinone and other common free radical inhibitors known in the art.
  • the level of inhibitor used is less than 1000 parts per million, preferably less than 800 parts per million, and most preferably, less than 600 parts per million.
  • a molar ratio of the lactone to hydroxyl groups in the ester of from about 1 :0.1 to about 1 :5, preferably from about 1 :0.3 to about 1 :3 is typically utilized.
  • R 4 is thus an aliphatic, aromatic, cycloaliphatic or heterocydic radical.
  • R 4 will contain from about 6 to about 36 carbon atoms, more typically from about 7 to about 24 carbon atoms.
  • R 4 will typically be a hydrocarbon group or a heterocydic group and is typically essentially free of urethane groups.
  • Suitable polyfunctional isocyanates preferably contain on average 2 to at most 4 NCO groups.
  • suitable isocyanates are 1 ,5-naphthalene di- isocyanate, 4,4'-diphenyl methane di-isocyanate (MDI), hydrogenated MDI
  • H12MDI xylylene di-isocyanate
  • TMXDI tetramethyl xylyiene di-isocyanate
  • the isomers of tolylene di-isocyanate (TDI) optionally in admixture, 1-methyl-2,4-di-isocyanatocyclohexane, 1 ,6-di- isocyanato-2,2,4-trimethyl hexane, 1 ,6-di-isocyanato-2,4,4-trimethyl hexane, 1- isocyanatomethyl-3-isocyanato-1 ,5,5-trimethyl
  • dicyclohexyl methane di-isocyanate dicyclohexyl methane di-isocyanate
  • cyclohexane- 1 ,4-di-isocyanate ethylene di-isocyanate
  • phthaiic acid bis-isocyanatoethyl ester polyisocyanates containing reactive halogen atoms, such as 1- chloromethylphenyl-2,4-di-isocyanate, 1-bromomethylphenyl-2,6-di-isocyanate, 3,3-bis-chloromethylether-4,4'-diphenyl di-isocyanate.
  • Sulfur-containing polyisocyanates are obtained, for example, by reaction of 2 mol hexamethylene di-isocyanate with 1 mol thiodiglycol or dihydroxydihexyl sulfide.
  • Other di ⁇ isocyanates are trimethyl hexamethylene di-isocyanate, 1 ,4-di-isocyanatobutane, 1 ,2-di-isocyanatododecane and dimer fatty acid di-isocyanate.
  • Tri-isocyanate isocyanurates can be prepared by trimerizing di-isocyanates at elevated temperatures, e.g.
  • the lactone-acrylate adduct is typically heated to a temperature of from about 40 to 100 °C and typically about 60 °C.
  • a catalytic amount of a urethane catalyst e.g. dibutyl tin dilaurate, is added followed by addition of an isocyanate compound the formula: R 4 - (NCO) n in which R' is as defined and n is typically 2 to 4, at a rate which maintains the desired reaction temperature.
  • the amount of the isocyanate will be essentially equal (e.g.
  • the reaction is typically heated, e.g. to a temperature of about 80 °C to about 100 °C, and held for about from 2 to about
  • the reaction with the isocyanate is entirely conventional being usually carried out at moderate temperature in the presence of a catalyst which promotes the urethane-forming reaction, such as dibutyl tin dilaurate. It is customary to limit the temperature, at least during the initial stages of the reaction, to about 60 °C, and this can be done by slowing the rate of addition of one of the components. The temperature may be raised in the later stages of the reaction to promote completion of the reaction as measured by the consumption of the isocyanate functionality.
  • the order of reaction is largely immaterial, it being possible to bring in the monohydric ethylenic compound either at the beginning, during the middle of the procedure, or as the last reactant. All of these variations are known in the art.
  • the amount of the oligomeric monomer will, in relation to the total monomers, typically be a minor amount, i.e. less than 50% by weight of the total monomers. Typically, the amount of the oligomeric monomer will range from about 0.1 % to about 30% by weight, more typically from about 1 % to about 20% by weight, and even more typically from about 5% to about 15% by weight of the total monomers.
  • the aqueous polymer emulsion of this invention also contains repeating units derived from alkyl esters of acrylic acid or methacrylic acid. Such esters are described in "Acrylic and Methacrylic Ester Polymers", Encyclopedia of Polymer Science and Engineering, vol. 1 , pp.
  • the polymer may also have repeating units derived from other monomers including, without limitation, ethylenically unsaturated carboxylic acids and vinyl aromatic monomers. Vinyl aromatic compounds are discussed in “Styrene Polymers” Encyclopedia of Polymer Science and Engineering, vol. 16, pp. 1-21 (John Wiley & Sons, Inc., N.Y., N.Y., 1989) and examples of such acids are described in "Acrylic and Methacrylic Acid Polymers", Encyclopedia of Polymer
  • acrylates and methacrylates examples include methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, sec-butyl, n-amyl, isoamyl, t-amyl, n-hexyl, 2-ethylbutyl, cyclohexyl, 2-heptyl, n-octyl, 2-ethylhexyl, n-decyl, and n-undecyl.
  • a potential utility of such monomers is the ability of one of ordinary skill, in possession of this disclosure, to use such monomers to optimize the softness of the polymer.
  • one measure of their utility will depend upon the desired degree of softness of the polymer which, in turn, depends at least in part, on the identity and amounts of the other monomeric units.
  • a measure of the softening or plasticizing effect of a monomer can be found by examining the glass transition temperature of a homopolymer of the monomer.
  • a plasticizing monomer will be such that a homopolymer of the monomer will exhibit a glass transition temperature (Tg) of less than about -30 °C.
  • Tg glass transition temperature
  • acrylates of a straight chain alkyl having from 3 to 1 1 carbon atoms or a branched chain alkyl having from 5 to 11 carbon atoms may generally be useful for plasticizing the polymer.
  • Vinyl aromatic compounds comprise monovinyl aromatic hydrocarbons containing from 8 to 12 carbon atoms and halogenated derivatives thereof having halo-substituted aromatic moieties
  • Examples include styrene alpha-methylstyrene, vinyl toluene (e g a 60/40 mixture by weight of meta- methylstyrene and para-methylstyrene), meta-methylstyrene, para- methylstyrene, para-ethylstyrene, para-n-propylstyrene, para-isopropylstyrene, para-tert-butylstyrene, ortho-chlorostyrene, para-chlorostyrene, alpha-methyl- meta-methylstyrene, alpha-methyl-para-methylstyrene
  • alkyl acrylates and methacrylates described above are preferably employed without additional comonomers for preparing ink vehicles of this invention
  • other monoethylenically unsaturated polymerizable monomers useful in minor proportion (e g less than 10% by weight of the total monomer composition) as comonomers with acrylic monomers may be useful in preparing the polymers of this invention, particularly for uses other than in ink vehicles
  • These monomers include the vinylidene halides, vinyl halides, acrylonitrile, methacrylonit ⁇ le, vinyl esters such as vinyl formate, vinyl acetate and vinyl propionate, and mixtures of ethylene and such vinyl esters, acrylic and methacrylic acid esters of alcohol ethers such as diethylene glycol monoethyl or monobutyl ether methacrylate, C1-C10alkyl esters of beta- acryloxypropionic acid and higher oligomers of acrylic acid, styrene and alkyl substituted styre
  • Additional monoethylenically unsaturated polymenzable comonomers that may be useful in preparing the polymer of the invention include hydroxy functional vinyl monomers such as 2-hydroxyethyl methacrylate, 2-hydroxyethyl acrylate, 3-hydroxypropyl methacrylate, butanediol acrylate,
  • useful monomers include the partial esters of unsaturated aliphatic dicarboxylic acids and particularly the alkyl half esters of such acids.
  • examples of such partial esters are the alkyl half esters of itaconic acid, fumaric acid and maleic acid wherein the alkyl group contains 1 to 6 carbon atoms.
  • Representative members of this group of compounds include methyl acid itaconic, butyl acid itaconic, ethyl acid fumarate, butyl acid fumarate, and methyl acid maleate.
  • alpha, beta-ethylenically unsaturated carboxylic acids which may also be useful as comonomers to prepare the polymer of the invention include acrylic acid, beta-acryloxypropionic acid and higher oligomers of acrylic acid and mixtures thereof, methacrylic acid, itaconic acid, aconitic acid, crotonic acid, citraconic acid, maleic acid, fumaric acid, alpha-chloroacrylic acid, cinnamic acid, mesaconic acid and mixtures thereof.
  • monomers may be emulsified with an anionic, cationic or nonionic dispersing agent, using for example from about 0.05% to 10% by weight of dispersing agent on the weight of total monomers.
  • an anionic, cationic or nonionic dispersing agent such as hydroxy ethyl cellulose, methyl cellulose and polyvinyl alcohol may be used as emulsion stabilizers and protective colloids, as may polyelectrolytes such as polyacrylic acid.
  • Cationic dispersion agents include lauryl-pyridinium chlorides, cetyldimethyl amine acetate, and alkyldimethylbenzylammonium chlorides in which the alkyl group has from 8 to 18 carbon atoms.
  • Anionic dispersing agents include, for example, the higher fatty alcohol sulfates, such as sodium lauryl sulfate, and the like; alkylaryl sulfonates such as sodium or potassium isopropylbenzene sulfonates or isopropylnaphthalene sulfonates, and the like; alkali metal higher alkyl sulfosuccinates, such as sodium octyl sulfosuccinate, sodium N-methyl-N-palmitoyltaurate, sodium oleyl isothionate, and the like; and alkali metal salts of alkylarylpolyethoxyethanol sulfates or sulfonates, such
  • Suitable non-ionic dispersing agents incl ude alkylphenoxypolyethoxyethanols having alkyl groups of from about 7 to 18 carbon atoms and from about 6 to about 60 oxyethylene units such as heptylphenoxypolyethoxyethanols, methyloctylphenoxypolyethoxyethanols, and the like; polyethoxyethanol derivatives of methylene-linked alkyl phenols; sulfur-containing agents such as those made by condensing from about 6 to about 60 moles of ethylene oxide with nonyl mercaptan, dodecyl mercaptan, and the like, or with alkylthiophenols wherein the alkyl groups contain from 6 to 16 carbon atoms; ethylene oxide derivatives of long-chained carboxylic acids, such as lauric acid, myristic acid, palmitic acid, oleic acid, and the like, or mixtures of acids such as those found in tall oil containing from 6 to 60 oxethylene units
  • the emulsion may contain one or more suspending aids.
  • Preferred compositions contain an acrylic resin having a substantial acid number as a suspending aid. Such resins become and contribute to the polymer film prepared from the emulsion, but do not have acceptable properties by themselves.
  • Preferred carboxylate polymers are vinyl aromatic acrylic copolymers (e.g. styrene/acrylic copolymers) having a substantial acid number (typically 150-250, and preferably 180-220) and a moderate molecular weight (e.g. 6,000 to 10,000). Vinyl aromatic compounds are discussed in "Styrene Polymers” Encyclopedia of Polymer Science and Engineering, vol. 16, pp. 1-21 (John Wiley & Sons, Inc., N.Y., N.Y., 1989), the disclosure of which is incorporated herein by reference.
  • the vinyl aromatic compounds comprise monovinyl aromatic hydrocarbons containing from 8 to 12 carbon atoms and halogenated derivatives thereof having halo-substituted aromatic moieties.
  • Examples include styrene, alpha-methylstyrene, vinyl toluene (e.g. a 60/40 mixture by weight of meta- methylstyrene and para-methylstyrene), meta-methylstyrene, para- methylstyrene, para-ethylstyrene, para- ⁇ -propylstyrene, para-isopropylstyrene, para-tert-butylstyrene, ortho-chlorostyrene, para-chlorostyrene, alpha-methyl- meta-methylstyrene, alpha-methyl-para-methylstyrene, tert-butyl styrene, alpha- methyl-ortho-chlorostyrene, and alpha-methyl-para-chlorostyrene.
  • styrene alpha-methylstyrene
  • vinyl toluene e.g. a 60
  • At least a portion of the acrylic units of the polymer will bear free carboxyl or carboxylate groups (the carboxyl or carboxylate form depending upon the pH of the aqueous emulsion).
  • This carboxylate functionality is solvated by the aqueous polymerization medium and, thus, contributes to the stability of the polymer suspension.
  • the aqueous composition should be essentially free of species which can react with or form a complex with such carboxylate functionality. Such freedom will ensure that the carboxylate functionality remains solvated by the aqueous polymerization medium and/or that the carboxylate polymer will not engage in measurable crosslinking, either in the aqueous polymerization medium or the films prepared therewith.
  • emulsion stabilizers i.e. water soluble polymers such as water-soluble polyalkylene oxides, may be useful.
  • a preferred emulsion stabilizer is a polypropylene glycol having a molecular weight in the range of 1 ,000 to 1 ,500.
  • a polymerization initiator of the free radical type such as ammonium or potassium persulfate
  • a redox system which also includes a reducing component such as potassium metabisulfite, sodium thiosulfate or sodium formaldehyde sulfoxylate.
  • the reducing component is frequently referred to as an accelerator.
  • the initiator and accelerator commonly referred to as catalyst, catalyst system or redox system, may be used in proportion from about 0.01% or less to 3% each, based on the weight of monomers to be copolymerized.
  • redox catalyst systems examples include t-butyl hydroperoxide/sodium formaldehyde sulfoxylate/Fe(ll), and ammonium persulfate/sodium bisulfite/sodium hydrosulfite/Fe(ll).
  • the polymerization temperature may be from room temperature to 90°C, or more, and may be optimized for the catalyst system employed, as is conventional.
  • Emulsion polymerization may be seeded or unseeded. Seeded polymerization is preferred and tends to yield aqueous dispersions of latex polymer having more uniform physical properties than unseeded polymerization.
  • Chain transfer agents including mercaptans, polymercaptans and polyhalogen compounds are sometimes desirable in the polymerization mixture to moderate polymer molecular weight.
  • chain transfer agents which may be used include long chain alkyl mercaptans such as t-dodecyl mercaptans, alcohols such as isopropanol, isobutanol, lauryl alcohol ort-octyl alcohol, carbon tetrachloride, tetrachloroethylene and trichlorobromoethane. Generally from about 0 to 3% by weight, based on the weight of the monomer mixture, may be used.
  • the polymerization process may be a thermal or redox type; that is, free radicals may be generated solely by the thermal dissociation of an initiator species or a redox system may be used.
  • a monomer emulsion containing all or some portion of the monomers to be polymerized may be prepared using the monomers, water and emulsifiers.
  • a catalyst solution containing catalyst in water may be separately prepared.
  • the monomer emulsion and catalyst solution may be co-fed into the polymerization vessel over the course of the emulsion polymerization.
  • the reaction vessel itself may initially contain water.
  • the reaction vessel may also additionally contain seed emulsion and further may additionally contain an initial charge of polymerization catalyst.
  • the temperature of the reaction vessel during the emulsion polymerization may be controlled by cooling to remove heat generated by the polymerization reaction or by heating the reaction vessel.
  • Several monomer emulsions may be simultaneously co-fed into the reaction vessel. When multiple monomer emulsions are co-fed, they may be of different monomer composition. The sequence and rates at which the diverse monomer emulsions are co-fed may be altered during the emulsion polymerization process.
  • the polymerization reaction mixture may be chased (e.g. with t-butyl hydroperoxide and sodium ascorbate) to minimize the concentrations of unreacted monomer and unreacted polymerization catalyst species.
  • the pH of the contents of the reaction vessel may also be altered during the course of the emulsion polymerization process. Both thermal and redox polymerization processes may be employed.
  • the inks, overprints, and primers of this invention can be prepared, for example, as disclosed in U.S. Pat. No. 4,148,779, which is incorporated herein by reference in its entirety.
  • the printing ink, overprint, or primer may be prepared as follows.
  • the colorant is added to the binder resin or a solution or dispersion thereof and, at a properly adjusted viscosity, dispersed thereinto with ball mill, sand mill, high-shear fluid flow mill, Cowles Dissolver, Katy Mill or the like.
  • the colorants also may be dispersed directly in the polymer by milling on a heated two-roll mill at about 220°F to 360°F.
  • the viscosity and printing characteristics of the ink composition may be modified further by addition of water, solvents, plasticizers, sequestered wax, surfactants and the like to suit the particular printing needs.
  • the ink compositions of the present invention are not limited to any type of dye, pigment, filler, or the like, all of which are hereinafter included in the term "colorant,” and can accommodate any colorant which can be dispersed, milled, mixed, blended or dissolved in any manner in either the polymer blend, water or aqueous polymer system.
  • the printing processes most advantageously used with the inks or varnishes are the flexographic and/or gravure printing processes.
  • this invention relates to a method of printing comprising applying a first portion of an aqueous dispersion comprised of the polymer of this invention to a first essentially impervious printing surface, said surface having recesses therein which define a resolvable image, contacting said surface with a printable substrate, and repeating said applying and said contacting with a second portion of said aqueous dispersion and a second printable surface.
  • This method may be a letterpress printing method (wherein said recesses define raised portions of the surface which carry the aqueous dispersion to the substrate, e.g. flexography) or a gravure printing method (wherein said recesses carry the aqueous dispersion to the substrate).
  • an aqueous dispersion comprised of the polymer of this invention is applied to a flexible plate mounted on a plate cylinder.
  • the flexible plate is then contacted with a printable substrate by rotation of the plate cylinder.
  • the aqueous dispersion is applied to the flexible plate with a cylindrical transfer roll which is rotated to successively take up and then apply successive portions of the aqueous dispersion.
  • a printing ink comprising a polymer of this invention as a binder and a colorant distributed through the composition in an effective amount sufficient to impart a predetermined color to the resulting composition.
  • another ingredient of the printing ink of this invention is the colorant.
  • colorant is specifically used in this specification in that it is intended to refer to both pigments and dyes which impart a distinct color to the composition.
  • the purpose of any colorant is to provide contrast between the color of the substrate and the color of ink in order to provide a visually identifiable indicia on the substrate.
  • the colorant may be any of those which are typically used in flexographic inks such as monoazo yellows (e.g. Cl Pigment Yellows 3, 5, 98); diarylide yellows (e.g. Cl Pigment Yellows 12, 13, 14); Pyrazolone Orange, Permanent Red 2G, Lithol Rubine 4B, Rubine 2B, Red Lake C, Lithol Red, Permanent Red R, Phthalocyanine Green, Phthalo-cyanine Blue, Permanent Violet, titanium dioxide, carbon black, etc.
  • the colorant is typically employed in amounts of about 10-45 wt. %, preferably 15-40 wt. %, based on the weight of the ink.
  • Typical substrates to which the coating or printing compositions of this invention may be applied include a wide variety of flexible materials.
  • typical substrates include films of polyethylene and polypropylene generally treated for adhesion promotion; also polyester such as polyethylene terephthalate, cellophane and polyamide which may or may not be coated with PVDC for improved barrier properties.
  • substrates of woven and non-woven fabrics where the fibers are of cotton, polyester, polyolefin, polyamide, polyimide and the like; metallic foils such as aluminum foil; metallized films; paper and paperboard; and cellular flexible sheet material such as polyethylene foam, polyurethane foam and sponge and foam rubber.
  • compositions In coating the substrates, conventional techniques known per se are employed to apply the composition to the substrate. Thus, these compositions may be applied by use of any mechanical coating process such as air knife, trailing blade, knife coater, reverse roll or gravure coating technique. Most commonly, the composition is coated on the substrate and allowed to dry.
  • a polymer can be prepared as set forth below from starting materials premixed as six separate charges in the amounts set forth below.
  • the oligomer monomer is a compound of the above formula wherein R 1 is methyl, R 2 is an ethylene group, R 3 is a pentamethylene group, R 4 is the residue of bis(1 ,1'-isocyanato-4,4'-cyclohexyl) methane, n is two, x is one, and y is two.
  • the polymer can be prepared by the following steps. Blanket the reactor with nitrogen and add Charge 1. Heat Charge 1 in the reactor to 77°C. Pump 17.3 parts of Charge 2 from monomer tank into the reactor and add Charge 3 to the reactor and continue mixing. Meter the remaining Charge 2 from the monomer tank into the reactor over a 70 minute period at 81 °C and mix for 1.5 hour at about 80°C.
  • the resulting dispersion gave a particle size ⁇ 20 micrometers on a fineness of grind gauge. Equal parts of latex and pigment dispersion were mixed and the viscosity of the sample adjusted with deionized water to 20 seconds on a #2 shell cup. The ink was applied to the corona treated side of 1 mil polypropylene film using a hand proofer and dried using forced air gun. As a second example, this procedure was repeated using Unitane R-900 titanium dioxide pigment.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Wood Science & Technology (AREA)
  • Paints Or Removers (AREA)

Abstract

An aqueous polymer emulsion composition comprising a polymer having repeating units derived from at least one monomer selected from the group consisting of alkyl acrylates and alkyl methacrylates, and at least one monomer having the formula: (x(CH2=CR1-C(O)O-)R2-(O-C(O)R3)y-O-C(O)-NH)n-R4, wherein R1 is hydrogen or methyl, R2 is an alkylene group or substituted alkylene group (typically having less than six carbon atoms, more typically two or three carbon atoms), R3 is an alkylene group or substituted alkylene group (typically having less than ten carbon atoms, more typically from four to six carbon atoms), R4 is the residue of an organic isocyanate (including trimerized isocyanates, but excluding isocyanate-functional prepolymers of active hydrogen compounds) having a functionality of n, n is an integer from two to four (typically two or three), x is an integer from one to three, and y is an integer from one to five, is provided. Also provided are printing inks comprising a colorant and a binder for said colorant comprising an aqueous emulsion polymer of this invention.

Description

ACRYLIC EMULSIONS USEFUL IN PRINTING INKS
Field of the Invention
The present invention relates to acrylic emulsions useful in printing inks, said acrylic emulsions being prepared by emulsion polymerization of acrylic monomers.
Background of the Invention
Flexible packaging printing inks are typically printed by rotary letterpress printing using flexible rubber plates or by gravure printing using engraved chrome-plated cylinders on a wide variety of substrates, e.g. plastic films such as cellulose acetate, polyethylene, polyethylene terephthalate, polyesters, polystyrene, cellophane, glassine, tissue, aluminum foils, liners, bags, paper labels, box coverings, gift wrappings, etc.
Flexible packaging printing inks are widely used in the graphic arts industry. They offer economy, versatility, quality and simplicity and permit a roll of material to be multi-color printed in a continuous web at speeds of over 300 meters per minute and feed it directly to converting machines for slitting, forming or laminating However, these inks must be carefully formulated so as to avoid the problems indigenous to these types of inks, e g chemical pinholing (failure of the ink to properly wet a plastic film surface), mechanical pinholing (the appearance of the pattern of the etched ink form roller), feathering (the appearance of stringy or ragged edges), mottle (ridged or speckled patterns), precipitation of part of the vehicle, blocking (a sticking or transfer of the image to the underside of the web), adhesion of the ink to the substrate, etc U S Patent No 5,338,785 (Catena et al ) discloses a flexible packaging printing ink is formulated from a copolymer of polyethylene glycol methacrylate and a polyamide resin, pigment, solvent and cellulose acetate butyrate The polyamide resin is prepared by condensing a dibasic acid mixture with a diamine mixture The dibasic acid mixture comprises about 0 5 to 0 8 equivalents of a C20-C44 dibasic acid mixture comprised of about 60 to 100% dimers, 0 to 40% trimers and 0 to 5% monomers, and about 0 2-0 7 equivalents of at least one C6-C12 dibasic acid such as azelaic acid and adipic acid, while the diamine mixture comprises about 0 5-0 8 equivalents of piperazine or a substituted piperazine and the balance comprises at least one C2-C12 alkyl diamine such as ethylene diamine
The use of acrylate ester polymers as printing ink vehicles is generally discussed in "Printing Ink Vehicles", Encyclopedia of Polymer Science and Engineering, vol 13, pp 368-398 (John Wiley & Sons, Inc N Y , N Y , 1988) For example, at page 393, it is stated that while acrylic and methacrylic ester resins are used in water-based systems, several problems still exist, for example balancing water solubility in the ink and water resistance in the end product
U S Patent No 5,075,364 (Phaπ et al ) discloses a blend of a water- dissipatable polyester material, an acrylic polymer and a water-dissipatable vinyl polymer It is stated that the acrylic polymer and the vinyl polymer must be compatible with the polyester which has a particular composition It is stated that the polymer blends are useful for preparing ink compositions having improved block resistance, water resistance, and alcohol resistance U S Patent No 4,921 899 discloses an ink composition containing a blend of a polyester, an acrylic polymer and a vinyl polymer The water-based inks containing the blend of these polymers as a binder can significantly improve ink film properties such as alcohol resistance, block resistance and water resistance as compared to use of water-dispersible polyester alone The polymer blends were also employed to prepare ink primers and overprint varnishes It is stated that these polymer blends were prepared by mixing an aqueous polyester dispersion with an acrylic emulsion which contains surfactants and other additives and that the presence of surfactants in the ink formulations creates several problems related to ink stability, printing process and print quality of the ink film
A number of patent documents disclose surfactants which are polymenzable, degradable or otherwise reactive duπng or after use Examples of Japanese patent documents describing reactive anionic surfactants are listed as follows Patent Application Nos 46-12472, 46-34894, 49-46291 , 56-29657, and Laid Open Application 51 -30285, 54-14431 , and 56-127697 Examples of Japanese patent documents describing reactive nonionic surfactants include Laid Open Applications Nos 50-98484 and 56-28208
U S Patent No 4,814,515 (Yokota et al ) discloses compounds prepared by the reaction of a glycidyl (meth)acrylate with a hydroxyalkylated polyalkyleneoxy fatty alcohol followed by reaction with an alkylene oxide and the use of these compounds as an emulsifier in the emulsion or dispersion polymerization of ethylenically unsaturated monomers
U.S Patent No 4,390,401 (Costanza) discloses the use of acrylate or methacrylate esters of polyalkylene oxide derivatives of alkyl/aryl phenols as wetting agents and adhesion promoters in ultraviolet curable coating systems A technical bulletin entitled "TREM LF-40 Reactive Anionic Surfactant for Emulsion Polymerization", Henkel Corporation, Ambler, Pennsylvania, states that TREM LF-40 is a sodium alkyl allyl sulfosuccinate with a reactive group in its molecule that will copolymenze with monomers via free radical polymerization
It is stated that the product, when used as a primary or secondary emulsifier, provides low foaming emulsions with improved water resistance Summary of the Invention
This invention relates to an aqueous polymer emulsion composition comprising a polymer having repeating units derived from at least one monomer selected from the group consisting of alkyl acrylates and alkyl methacrylates and at least one monomer having the formula:
(x(CH2=CR1-C(O)O-)R2-(O-C(O)R3)y-O-C(O)-NH)n-R4
wherein:
R1 is hydrogen or methyl, R2 is an alkylene group or substituted alkylene group (typically having less than six carbon atoms, more typically two or three carbon atoms),
R3 is an alkylene group or substituted alkylene group (typically having less than ten carbon atoms, more typically from four to six carbon atoms),
R4 is an aliphatic, aromatic, cycloaliphatic or heterocydic radical (i.e. the residue of an organic isocyanate, including trimerized isocyanates, but excluding isocyanate-functional prepolymers of active hydrogen compounds) having a functionality of n, n is an integer from two to four (typically two or three), x is an integer from one to three, and y is an integer from one to five.
The present invention also relates to printing inks comprising a colorant and a binder for said colorant comprising an aqueous emulsion polymer of this invention.
This invention also relates to a method of coating a substrate comprising (i) contacting a surface of a substrate with a composition comprising an ink as defined above, and (ii) drying said surface to form a film of the solids of said ink in contact with said surface. In certain embodiments, this coating process is a printing process.
Among the compounds which fall within the above formula are those in which R1 is hydrogen, R2 is an ethylene group, R3 is a pentamethylene group, and R4 is the residue of isophorone di-isocyanate (and n is two), tetramethylxylene di-isocyanate (and n is two), toluene di-isocyanate (and n is two), or trimerized hexamethylene di-isocyanate (and n is three), x is one and y is two.
Broadly speaking, this oligomer is a polyester oligomer prepared by forming a mixture of an acrylate- or methacrylate-functional and mono-hydroxyl- functional polyester oligomer and an isocyanate. These two components of the mixture then react in the presence of a urethane catalyst. The resulting product should contain essentially no unreacted isocyanate functionality.
Detailed Description of the Invention
The monomer having the above formula can be characterized as an oligomer which is olefinically unsaturated. These monomers are derived from hydroxy-functional lactone-modified acrylate or methacrylate acid esters (hereinafter "lactone-acrylate adducts") prepared by reacting an appropriate lactone with an acrylate or methacrylate acid ester which are in turn reacted with a polyisocyanate.
Lactones employed in the preparation of the lactone-acrylate adducts typically have the formula:
0-CH(R)-(CR2)z-C=0
wherein R is hydrogen or an alkyl group having from 1 to 12 carbon atoms, z is from 4 to 7 and at least (z - 2) of the R's is hydrogen. Preferred lactones are the epsilon-caprolactones wherein z is 4 and at least 6 of the R's are hydrogen with the remainder, if any, being alkyl groups. Preferably, none of the substituents contain more than 12 carbon atoms and the total number of carbon atoms in these substituents on the lactone ring does not exceed 12. Unsubstituted epsilon-caprolactone, i.e., where each R is hydrogen, is a derivative of 6-hydroxyhexanoic acid. Both the unsubstituted and substituted epsilon-caprolactones are available by reacting the corresponding cyclohexanone with an oxidizing agent such as peracetic acid.
Substituted epsilon-caprolactones found to be most suitable for preparing the present lactone-acrylate adducts are the various epsilon-monoalkylcaprolactones wherein the alkyl groups contain from 1 to 12 carbon atoms, e.g., epsilon-methyl-caprolactone, epsilon-ethyl-caprolactone, epsilon-propyl-caprolactone and epsilon-dodecyl-caprolactone. Useful also are the epsilon-dialkylcaprolactones in which the two alkyl groups are substituted on the same or different carbon atoms, but not both on the omega carbon atoms. Also useful are the epsilon-trialkylcaprolactones wherein 2 or 3 carbon atoms in the lactone ring are substituted provided, though, that the omega carbon atom is not di-substituted. The most preferred lactone starting reactant is the epsilon-caprolactone wherein z in the lactone formula is 4 and each R is hydrogen. The acrylate or methacrylate acid esters utilized to prepare the lactone-acrylate adducts contain from 1 to 3 acrylyl or alpha-substituted acrylyl groups and one or two hydroxyl groups. Such esters are commercially available and/or can be readily synthesized. Commercially available esters include the hydroxyalkyi acrylates or hydroxyalkyi methacrylates wherein the alkyl group contains from 2 to 10 carbon atoms, preferably from 2 to 6 carbon atoms. The hydroxyalkyi acrylates and methacrylates have the following formula:
(CH2=CR1-C(O)O)x-R2-OH
wherein R1 is hydrogen or methyl, x is an integer from 1 to 3, and R2 is a linear or a branched alkylene group having from 2 to 10 carbon atoms, preferably from 2 to 6 carbon atoms.
Examples of suitable hydroxyalkyi acrylates and methacrylates include 2-hydroxyethyl acrylate, 2-hydroxypropyl acrylate, 2-hydroxyethyl methacrylate, 2-hydroxypropyl methacrylate, diethylene glycol monoacrylate, diethylene glycol monomethacrylate, glycerine dimethacrylate, trimethylol propane dimethacrylate, 3-hydroxypropyl acrylate, 2-hydroxybutyl acrylate, 4-hydroxybutyl acrylate, 3-hydroxypentyi acrylate, 6-hydroxynonyl acrylate, 2-hydroxyethyl methacrylate, 2-hydroxypropyl methacrylate, 3-hydroxypropyl methacrylate, 2-hydroxybutyl methacrylate, 2-hydroxypentyl methacrylate, 5-hydroxypentyl methacrylate, 7-hydroxyheptyl methacrylate and 5-hydroxydecyl methacrylate. Preferred lactone-acrylate adducts have the formula:
CH2=CR1-C(O)O-R2-(O-C(O)R3)2-OH wherein R1, R2, and R3 are as described above.
The lactone-acrylate adduct is prepared by reacting the lactone with the hydroxyalkyi acrylate in the presence of less than about 200 parts per million of a catalyst. The catalysts which may be used include one or more organometallic compounds and other metallic compounds such as stannic chloride or ferric chloride and other Lewis or protonic acids. Preferred catalysts include stannous octoate, dibutyltin dilaurate, and other tin compounds; titanates such as tetraisopropyl titanate and butyl titanate; and the like. The reaction is carried out at a temperature of from about 10OX to about
400°C, preferably from about 120°C to about 130°C. The reaction may be carried out at atmospheric pressure, although higher or lower pressures may be used. The reaction is generally carried out in the presence of oxygen to inhibit polymerization of the hydroxyalkyi acrylate. The reaction is generally carried out for a period of from about 2 to about 20 hours. The reaction is carried out in the presence of a suitable inhibitor to prevent polymerization of the hydroxyalkyi acrylate double bond. These inhibitors include the monomethyl ether of hydroquinone, benzoquinone, phenothiazine, methyl hydroquinone, 2,5-di-t-butylquinone, hydroquinone, benzoquinone and other common free radical inhibitors known in the art. The level of inhibitor used is less than 1000 parts per million, preferably less than 800 parts per million, and most preferably, less than 600 parts per million. A molar ratio of the lactone to hydroxyl groups in the ester of from about 1 :0.1 to about 1 :5, preferably from about 1 :0.3 to about 1 :3 is typically utilized. An example of a lactone-acrylate adduct preferred for use in the present invention is a caprolactone-2-hydroxyethyl acrylate adduct supplied by Union Carbide Corporation under the tradename TONE M-100, which has the formula CH2=CH-C(O)O-CH2-CH2-(O-C(O)(CH2)5)2-OH.
A polyfunctional aromatic and aliphatic isocyanate is reacted with the lactone-acrylate adduct to introduce the isocyanate residue into the compound. The R4 is thus an aliphatic, aromatic, cycloaliphatic or heterocydic radical. Typically, R4 will contain from about 6 to about 36 carbon atoms, more typically from about 7 to about 24 carbon atoms. R4 will typically be a hydrocarbon group or a heterocydic group and is typically essentially free of urethane groups.
Suitable polyfunctional isocyanates preferably contain on average 2 to at most 4 NCO groups. Examples of suitable isocyanates are 1 ,5-naphthalene di- isocyanate, 4,4'-diphenyl methane di-isocyanate (MDI), hydrogenated MDI
(H12MDI), xylylene di-isocyanate (XDI), tetramethyl xylyiene di-isocyanate (TMXDI), 4,4'-diphenyl dimethyl methane di-isocyanate, di- and tetraalkyl diphenyl methane di-isocyanate, 4,4'-dibenzyl di-isocyanate, 1 ,3-phenylene di¬ isocyanate, 1 ,4-phenylene di-isocyanate, the isomers of tolylene di-isocyanate (TDI), optionally in admixture, 1-methyl-2,4-di-isocyanatocyclohexane, 1 ,6-di- isocyanato-2,2,4-trimethyl hexane, 1 ,6-di-isocyanato-2,4,4-trimethyl hexane, 1- isocyanatomethyl-3-isocyanato-1 ,5,5-trimethyl cydohexane (IPDI), chlorinated and brominated di-isocyanates, phosphorus-containing di-isocyanates, 4,4'-di- isocyanatophenyl perfluoroethane, tetramethoxybutane-1 ,4-di-isocyanate, 1 ,4- butane di-isocyanate, 1 ,6-hexane di-isocyanate (HDI), bis(1 ,1'-isocyanato-4,4'- cyclohexyl) methane (a.k.a. dicyclohexyl methane di-isocyanate), cyclohexane- 1 ,4-di-isocyanate, ethylene di-isocyanate, phthaiic acid bis-isocyanatoethyl ester; polyisocyanates containing reactive halogen atoms, such as 1- chloromethylphenyl-2,4-di-isocyanate, 1-bromomethylphenyl-2,6-di-isocyanate, 3,3-bis-chloromethylether-4,4'-diphenyl di-isocyanate. Sulfur-containing polyisocyanates are obtained, for example, by reaction of 2 mol hexamethylene di-isocyanate with 1 mol thiodiglycol or dihydroxydihexyl sulfide. Other di¬ isocyanates are trimethyl hexamethylene di-isocyanate, 1 ,4-di-isocyanatobutane, 1 ,2-di-isocyanatododecane and dimer fatty acid di-isocyanate. Tri-isocyanate isocyanurates can be prepared by trimerizing di-isocyanates at elevated temperatures, e.g. at about 200 °C and/or in the presence of a catalyst such as an amine, metal alkyl, or carboxylate zwitterion. For reaction with the isocyanate, the lactone-acrylate adduct is typically heated to a temperature of from about 40 to 100 °C and typically about 60 °C. At this time, a catalytic amount of a urethane catalyst, e.g. dibutyl tin dilaurate, is added followed by addition of an isocyanate compound the formula: R4- (NCO)n in which R' is as defined and n is typically 2 to 4, at a rate which maintains the desired reaction temperature. The amount of the isocyanate will be essentially equal (e.g. 1.01:1 to 1:1.01), on an equivalents basis, to the hydroxyl equivalents of the lactone-acrylate adduct. When the addition is complete, the reaction is typically heated, e.g. to a temperature of about 80 °C to about 100 °C, and held for about from 2 to about
4 hours or until the NCO content is <0.5% by weight as measured for example by titration with dibutyl amine. Thereafter, the product is cooled prior to storage.
The reaction with the isocyanate is entirely conventional being usually carried out at moderate temperature in the presence of a catalyst which promotes the urethane-forming reaction, such as dibutyl tin dilaurate. It is customary to limit the temperature, at least during the initial stages of the reaction, to about 60 °C, and this can be done by slowing the rate of addition of one of the components. The temperature may be raised in the later stages of the reaction to promote completion of the reaction as measured by the consumption of the isocyanate functionality. The order of reaction is largely immaterial, it being possible to bring in the monohydric ethylenic compound either at the beginning, during the middle of the procedure, or as the last reactant. All of these variations are known in the art. It is usual herein to employ the di-isocyanate and the materials reactive therewith in stoichiometric amounts and to continue the reaction until the isocyanate functionality is substantially undetectable. As will be understood, these reactions are conveniently carried out neat with reactants that are liquid at the reaction temperature or in solvent solution, this being illustrated using the preferred tetrahydrofuran to maintain the liquid condition as the reaction proceeds.
The amount of the oligomeric monomer will, in relation to the total monomers, typically be a minor amount, i.e. less than 50% by weight of the total monomers. Typically, the amount of the oligomeric monomer will range from about 0.1 % to about 30% by weight, more typically from about 1 % to about 20% by weight, and even more typically from about 5% to about 15% by weight of the total monomers. The aqueous polymer emulsion of this invention also contains repeating units derived from alkyl esters of acrylic acid or methacrylic acid. Such esters are described in "Acrylic and Methacrylic Ester Polymers", Encyclopedia of Polymer Science and Engineering, vol. 1 , pp. 234-299 (John Wiley & Sons, Inc., N.Y., N.Y., 1985), the disclosure of which is incorporated herein by reference. The polymer may also have repeating units derived from other monomers including, without limitation, ethylenically unsaturated carboxylic acids and vinyl aromatic monomers. Vinyl aromatic compounds are discussed in "Styrene Polymers" Encyclopedia of Polymer Science and Engineering, vol. 16, pp. 1-21 (John Wiley & Sons, Inc., N.Y., N.Y., 1989) and examples of such acids are described in "Acrylic and Methacrylic Acid Polymers", Encyclopedia of Polymer
Science and Engineering, vol. 1 , pp. 211-234 (John Wiley & Sons, Inc., N.Y.,
N.Y., 1985), the disclosures of which are incorporated herein by reference.
Examples of acrylates and methacrylates that should be useful include methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, sec-butyl, n-amyl, isoamyl, t-amyl, n-hexyl, 2-ethylbutyl, cyclohexyl, 2-heptyl, n-octyl, 2-ethylhexyl, n-decyl, and n-undecyl. A potential utility of such monomers is the ability of one of ordinary skill, in possession of this disclosure, to use such monomers to optimize the softness of the polymer. Thus, one measure of their utility will depend upon the desired degree of softness of the polymer which, in turn, depends at least in part, on the identity and amounts of the other monomeric units. A measure of the softening or plasticizing effect of a monomer can be found by examining the glass transition temperature of a homopolymer of the monomer. Generally, a plasticizing monomer will be such that a homopolymer of the monomer will exhibit a glass transition temperature (Tg) of less than about -30 °C. Thus, acrylates of a straight chain alkyl having from 3 to 1 1 carbon atoms or a branched chain alkyl having from 5 to 11 carbon atoms may generally be useful for plasticizing the polymer. Because of the relatively high Tg of poly(t-butyl acrylate), the use of a monomer t-butyl acrylate is unlikely to be advantageous Vinyl aromatic compounds comprise monovinyl aromatic hydrocarbons containing from 8 to 12 carbon atoms and halogenated derivatives thereof having halo-substituted aromatic moieties Examples include styrene alpha-methylstyrene, vinyl toluene (e g a 60/40 mixture by weight of meta- methylstyrene and para-methylstyrene), meta-methylstyrene, para- methylstyrene, para-ethylstyrene, para-n-propylstyrene, para-isopropylstyrene, para-tert-butylstyrene, ortho-chlorostyrene, para-chlorostyrene, alpha-methyl- meta-methylstyrene, alpha-methyl-para-methylstyrene, tert-butyl styrene, alpha- methyl-ortho-chlorostyrene, and alpha-methyl-para-chlorostyrene
Further, while the preferred alkyl acrylates and methacrylates described above are preferably employed without additional comonomers for preparing ink vehicles of this invention, other monoethylenically unsaturated polymerizable monomers useful in minor proportion (e g less than 10% by weight of the total monomer composition) as comonomers with acrylic monomers may be useful in preparing the polymers of this invention, particularly for uses other than in ink vehicles These monomers include the vinylidene halides, vinyl halides, acrylonitrile, methacrylonitπle, vinyl esters such as vinyl formate, vinyl acetate and vinyl propionate, and mixtures of ethylene and such vinyl esters, acrylic and methacrylic acid esters of alcohol ethers such as diethylene glycol monoethyl or monobutyl ether methacrylate, C1-C10alkyl esters of beta- acryloxypropionic acid and higher oligomers of acrylic acid, styrene and alkyl substituted styrenes and vinyl aromatics including alpha-methyl styrene, mixtures of ethylene and other alkylolefins such as propylene, butylene, pentene and the like, vinyl ethers such as methyl vinyl ether, ethyl vinyl ether, vinyl 2-methoxyethyl ether, vinyl 2-chloroethyl ether and the like
Additional monoethylenically unsaturated polymenzable comonomers that may be useful in preparing the polymer of the invention include hydroxy functional vinyl monomers such as 2-hydroxyethyl methacrylate, 2-hydroxyethyl acrylate, 3-hydroxypropyl methacrylate, butanediol acrylate,
3-chloro-2-hydroxypropyl acrylate, 2-hydroxypropyl acrylate, and 2-hydroxypropyl methacrylate Further examples of useful monomers include the partial esters of unsaturated aliphatic dicarboxylic acids and particularly the alkyl half esters of such acids. Examples of such partial esters are the alkyl half esters of itaconic acid, fumaric acid and maleic acid wherein the alkyl group contains 1 to 6 carbon atoms. Representative members of this group of compounds include methyl acid itaconic, butyl acid itaconic, ethyl acid fumarate, butyl acid fumarate, and methyl acid maleate. Minor amounts of other comonomers, such as adhesion promoting comonomers, may also be used. These monomers may be copolymerized with acrylic monomers to yield the polymer. Examples of alpha, beta-ethylenically unsaturated carboxylic acids which may also be useful as comonomers to prepare the polymer of the invention include acrylic acid, beta-acryloxypropionic acid and higher oligomers of acrylic acid and mixtures thereof, methacrylic acid, itaconic acid, aconitic acid, crotonic acid, citraconic acid, maleic acid, fumaric acid, alpha-chloroacrylic acid, cinnamic acid, mesaconic acid and mixtures thereof.
The preparation of aqueous dispersions of polymers by emulsion polymerization for use in coatings applications is well known in the art. The practice of emulsion polymerization is discussed in detail in G. Poehlein, "Emulsion Polymerization", Encyclopedia of Polymer Science and Technology. vol. 6, pp. 1-51 (John Wiley & Sons, Inc. N.Y., N.Y., 1986), the disclosure of which is incoφorated herein by reference. Conventional emulsion polymerization techniques may be used to prepare the aqueous dispersion of polymers of this invention.
Thus, monomers may be emulsified with an anionic, cationic or nonionic dispersing agent, using for example from about 0.05% to 10% by weight of dispersing agent on the weight of total monomers. Combinations of anionic and nonionic emulsifiers may also be used. High molecular weight polymers such as hydroxy ethyl cellulose, methyl cellulose and polyvinyl alcohol may be used as emulsion stabilizers and protective colloids, as may polyelectrolytes such as polyacrylic acid. Cationic dispersion agents include lauryl-pyridinium chlorides, cetyldimethyl amine acetate, and alkyldimethylbenzylammonium chlorides in which the alkyl group has from 8 to 18 carbon atoms. Anionic dispersing agents include, for example, the higher fatty alcohol sulfates, such as sodium lauryl sulfate, and the like; alkylaryl sulfonates such as sodium or potassium isopropylbenzene sulfonates or isopropylnaphthalene sulfonates, and the like; alkali metal higher alkyl sulfosuccinates, such as sodium octyl sulfosuccinate, sodium N-methyl-N-palmitoyltaurate, sodium oleyl isothionate, and the like; and alkali metal salts of alkylarylpolyethoxyethanol sulfates or sulfonates, such as sodium tert-octylphenoxypolyethoxyethyl sulfate having 1 to 5 oxyethylene units, and the like.
Suitable non-ionic dispersing agents incl ude alkylphenoxypolyethoxyethanols having alkyl groups of from about 7 to 18 carbon atoms and from about 6 to about 60 oxyethylene units, such as heptylphenoxypolyethoxyethanols, methyloctylphenoxypolyethoxyethanols, and the like; polyethoxyethanol derivatives of methylene-linked alkyl phenols; sulfur-containing agents such as those made by condensing from about 6 to about 60 moles of ethylene oxide with nonyl mercaptan, dodecyl mercaptan, and the like, or with alkylthiophenols wherein the alkyl groups contain from 6 to 16 carbon atoms; ethylene oxide derivatives of long-chained carboxylic acids, such as lauric acid, myristic acid, palmitic acid, oleic acid, and the like, or mixtures of acids such as those found in tall oil containing from 6 to 60 oxethylene units per molecule; analogous ethylene oxide condensates of long-chained alcohols such as octyl, decyl, lauryl, or cetyl alcohols, ethylene oxide derivative of etherified or esterified polyhydroxy compounds having a hydrophobic hydrocarbon chain, such as sorbitan monostearate containing from 6 to 60 oxethylene units; also, ethylene oxide condensates of long-chain or branched chain amines, such as dodecyl amine, hexadecyl amine, and octadecyl amine, containing from 6 to 60 oxyethylene units; block copolymers of ethylene oxide sections combined with one or more hydrophobic propylene oxide sections; and alkyl polyglycosides. Mixtures of alkyl benzenesulfonates and ethoxylated alkylphenols may be employed. In addition to the emulsifiers set forth above, the emulsion may contain one or more suspending aids. Preferred compositions contain an acrylic resin having a substantial acid number as a suspending aid. Such resins become and contribute to the polymer film prepared from the emulsion, but do not have acceptable properties by themselves.
Preferred carboxylate polymers are vinyl aromatic acrylic copolymers (e.g. styrene/acrylic copolymers) having a substantial acid number (typically 150-250, and preferably 180-220) and a moderate molecular weight (e.g. 6,000 to 10,000). Vinyl aromatic compounds are discussed in "Styrene Polymers" Encyclopedia of Polymer Science and Engineering, vol. 16, pp. 1-21 (John Wiley & Sons, Inc., N.Y., N.Y., 1989), the disclosure of which is incorporated herein by reference. The vinyl aromatic compounds comprise monovinyl aromatic hydrocarbons containing from 8 to 12 carbon atoms and halogenated derivatives thereof having halo-substituted aromatic moieties. Examples include styrene, alpha-methylstyrene, vinyl toluene (e.g. a 60/40 mixture by weight of meta- methylstyrene and para-methylstyrene), meta-methylstyrene, para- methylstyrene, para-ethylstyrene, para-π-propylstyrene, para-isopropylstyrene, para-tert-butylstyrene, ortho-chlorostyrene, para-chlorostyrene, alpha-methyl- meta-methylstyrene, alpha-methyl-para-methylstyrene, tert-butyl styrene, alpha- methyl-ortho-chlorostyrene, and alpha-methyl-para-chlorostyrene. At least a portion of the acrylic units of the polymer will bear free carboxyl or carboxylate groups (the carboxyl or carboxylate form depending upon the pH of the aqueous emulsion). This carboxylate functionality is solvated by the aqueous polymerization medium and, thus, contributes to the stability of the polymer suspension. The aqueous composition should be essentially free of species which can react with or form a complex with such carboxylate functionality. Such freedom will ensure that the carboxylate functionality remains solvated by the aqueous polymerization medium and/or that the carboxylate polymer will not engage in measurable crosslinking, either in the aqueous polymerization medium or the films prepared therewith. Also, emulsion stabilizers, i.e. water soluble polymers such as water-soluble polyalkylene oxides, may be useful. A preferred emulsion stabilizer is a polypropylene glycol having a molecular weight in the range of 1 ,000 to 1 ,500.
A polymerization initiator of the free radical type, such as ammonium or potassium persulfate, may be used alone or as the oxidizing component of a redox system, which also includes a reducing component such as potassium metabisulfite, sodium thiosulfate or sodium formaldehyde sulfoxylate. The reducing component is frequently referred to as an accelerator. The initiator and accelerator, commonly referred to as catalyst, catalyst system or redox system, may be used in proportion from about 0.01% or less to 3% each, based on the weight of monomers to be copolymerized. Examples of redox catalyst systems include t-butyl hydroperoxide/sodium formaldehyde sulfoxylate/Fe(ll), and ammonium persulfate/sodium bisulfite/sodium hydrosulfite/Fe(ll). The polymerization temperature may be from room temperature to 90°C, or more, and may be optimized for the catalyst system employed, as is conventional.
Emulsion polymerization may be seeded or unseeded. Seeded polymerization is preferred and tends to yield aqueous dispersions of latex polymer having more uniform physical properties than unseeded polymerization.
Chain transfer agents including mercaptans, polymercaptans and polyhalogen compounds are sometimes desirable in the polymerization mixture to moderate polymer molecular weight. Examples of chain transfer agents which may be used include long chain alkyl mercaptans such as t-dodecyl mercaptans, alcohols such as isopropanol, isobutanol, lauryl alcohol ort-octyl alcohol, carbon tetrachloride, tetrachloroethylene and trichlorobromoethane. Generally from about 0 to 3% by weight, based on the weight of the monomer mixture, may be used.
The polymerization process may be a thermal or redox type; that is, free radicals may be generated solely by the thermal dissociation of an initiator species or a redox system may be used. A monomer emulsion containing all or some portion of the monomers to be polymerized may be prepared using the monomers, water and emulsifiers. A catalyst solution containing catalyst in water may be separately prepared. The monomer emulsion and catalyst solution may be co-fed into the polymerization vessel over the course of the emulsion polymerization. The reaction vessel itself may initially contain water. The reaction vessel may also additionally contain seed emulsion and further may additionally contain an initial charge of polymerization catalyst. The temperature of the reaction vessel during the emulsion polymerization may be controlled by cooling to remove heat generated by the polymerization reaction or by heating the reaction vessel. Several monomer emulsions may be simultaneously co-fed into the reaction vessel. When multiple monomer emulsions are co-fed, they may be of different monomer composition. The sequence and rates at which the diverse monomer emulsions are co-fed may be altered during the emulsion polymerization process. After addition of the monomer emulsion or emulsions has been completed, the polymerization reaction mixture may be chased (e.g. with t-butyl hydroperoxide and sodium ascorbate) to minimize the concentrations of unreacted monomer and unreacted polymerization catalyst species. The pH of the contents of the reaction vessel may also be altered during the course of the emulsion polymerization process. Both thermal and redox polymerization processes may be employed.
The inks, overprints, and primers of this invention can be prepared, for example, as disclosed in U.S. Pat. No. 4,148,779, which is incorporated herein by reference in its entirety. For example, the printing ink, overprint, or primer may be prepared as follows. The colorant is added to the binder resin or a solution or dispersion thereof and, at a properly adjusted viscosity, dispersed thereinto with ball mill, sand mill, high-shear fluid flow mill, Cowles Dissolver, Katy Mill or the like. The colorants also may be dispersed directly in the polymer by milling on a heated two-roll mill at about 220°F to 360°F. (104.44°C to 182.22CC.) and using processing aids as desired, such as solvents or plasticizers. The viscosity and printing characteristics of the ink composition may be modified further by addition of water, solvents, plasticizers, sequestered wax, surfactants and the like to suit the particular printing needs. The ink compositions of the present invention are not limited to any type of dye, pigment, filler, or the like, all of which are hereinafter included in the term "colorant," and can accommodate any colorant which can be dispersed, milled, mixed, blended or dissolved in any manner in either the polymer blend, water or aqueous polymer system. The printing processes most advantageously used with the inks or varnishes are the flexographic and/or gravure printing processes. One characteristic of such printing processes, is that the aqueous dispersion of ink or varnish is supplied to said surface by a hydrophilic cylindrical transfer roll. Printing processes are described by T. Sulzberg et al., "Printing Ink Vehicles", Encyclopedia of Polymer Science and Engineering, vol. 13, pp. 368-398 (John Wiley & Sons, Inc., N.Y., N.Y., 1988), the disclosure of which is incorporated herein by reference. Thus, this invention relates to a method of printing comprising applying a first portion of an aqueous dispersion comprised of the polymer of this invention to a first essentially impervious printing surface, said surface having recesses therein which define a resolvable image, contacting said surface with a printable substrate, and repeating said applying and said contacting with a second portion of said aqueous dispersion and a second printable surface. This method may be a letterpress printing method (wherein said recesses define raised portions of the surface which carry the aqueous dispersion to the substrate, e.g. flexography) or a gravure printing method (wherein said recesses carry the aqueous dispersion to the substrate). In flexographic printing in particular, an aqueous dispersion comprised of the polymer of this invention is applied to a flexible plate mounted on a plate cylinder. The flexible plate is then contacted with a printable substrate by rotation of the plate cylinder. In preferred embodiments, the aqueous dispersion is applied to the flexible plate with a cylindrical transfer roll which is rotated to successively take up and then apply successive portions of the aqueous dispersion.
Also provided by this invention is a printing ink comprising a polymer of this invention as a binder and a colorant distributed through the composition in an effective amount sufficient to impart a predetermined color to the resulting composition. Thus, another ingredient of the printing ink of this invention is the colorant.
The generic term colorant is specifically used in this specification in that it is intended to refer to both pigments and dyes which impart a distinct color to the composition. The purpose of any colorant is to provide contrast between the color of the substrate and the color of ink in order to provide a visually identifiable indicia on the substrate.
The colorant may be any of those which are typically used in flexographic inks such as monoazo yellows (e.g. Cl Pigment Yellows 3, 5, 98); diarylide yellows (e.g. Cl Pigment Yellows 12, 13, 14); Pyrazolone Orange, Permanent Red 2G, Lithol Rubine 4B, Rubine 2B, Red Lake C, Lithol Red, Permanent Red R, Phthalocyanine Green, Phthalo-cyanine Blue, Permanent Violet, titanium dioxide, carbon black, etc. The colorant is typically employed in amounts of about 10-45 wt. %, preferably 15-40 wt. %, based on the weight of the ink.
Typical substrates to which the coating or printing compositions of this invention may be applied include a wide variety of flexible materials. Thus, typical substrates include films of polyethylene and polypropylene generally treated for adhesion promotion; also polyester such as polyethylene terephthalate, cellophane and polyamide which may or may not be coated with PVDC for improved barrier properties. Also contemplated within the present invention are substrates of woven and non-woven fabrics where the fibers are of cotton, polyester, polyolefin, polyamide, polyimide and the like; metallic foils such as aluminum foil; metallized films; paper and paperboard; and cellular flexible sheet material such as polyethylene foam, polyurethane foam and sponge and foam rubber.
In coating the substrates, conventional techniques known per se are employed to apply the composition to the substrate. Thus, these compositions may be applied by use of any mechanical coating process such as air knife, trailing blade, knife coater, reverse roll or gravure coating technique. Most commonly, the composition is coated on the substrate and allowed to dry.
The following examples will serve to further illustrate the invention, but should not be construed to limit the invention, unless expressly set forth in the appended claims. All parts, percentages, and ratios are by weight unless otherwise indicated in context.
Examples A polymer can be prepared as set forth below from starting materials premixed as six separate charges in the amounts set forth below.
Figure imgf000021_0001
The oligomer monomer is a compound of the above formula wherein R1 is methyl, R2 is an ethylene group, R3 is a pentamethylene group, R4 is the residue of bis(1 ,1'-isocyanato-4,4'-cyclohexyl) methane, n is two, x is one, and y is two. The polymer can be prepared by the following steps. Blanket the reactor with nitrogen and add Charge 1. Heat Charge 1 in the reactor to 77°C. Pump 17.3 parts of Charge 2 from monomer tank into the reactor and add Charge 3 to the reactor and continue mixing. Meter the remaining Charge 2 from the monomer tank into the reactor over a 70 minute period at 81 °C and mix for 1.5 hour at about 80°C. Add Charge 4 to the reactor and one-third of Charge 5 and mix for 5 minutes 80°C. Add another one-third of Charge 5 and mix for 10 minutes at 80°C . Add remaining one-third of Charge 5 and mix for about 1 hour. Allow to cool to ambient temperature. The latex from above was used to prepare white inks by blending with an aqueous titanium dioxide dispersion. The titanium dioxide dispersion was prepared by charging the following to a high speed Waring blender for 30 minutes:
- 150 parts titanium dioxide (Unitane R-960);
- 50 parts styrenated acrylic resin at 30 wt.% solids in water, acid value: 255, M.W.: 8000; and
- 30 parts deionized water.
The resulting dispersion gave a particle size < 20 micrometers on a fineness of grind gauge. Equal parts of latex and pigment dispersion were mixed and the viscosity of the sample adjusted with deionized water to 20 seconds on a #2 shell cup. The ink was applied to the corona treated side of 1 mil polypropylene film using a hand proofer and dried using forced air gun. As a second example, this procedure was repeated using Unitane R-900 titanium dioxide pigment.
The printed inks were tested for adhesion to polypropylene film using both dry and wet tape tests. Gloss measurements were determined from 60° reflectance measurements. Ten separate measurements were made on each print and the results averaged. Tape adhesion was determined using Scotch 610 tape. The tape was placed on the print in the cross direction and removed. The amount of ink removed from the print was determined for each sample and ranked (1-10, 10 = best) Both dry tape and wet tape tests (overnight in ice¬ water) were determined for each print Compared to a standard latex polymer (G-CRYL 1200), the latex prepared as above showed improved adhesion to plastic
SAMPLE PIGMENT GLOSS DRY TAPE WET TAPE
G-CRYL 1200 R-900 41 1 4 4
G-CRYL 1200 R-960 13 4 5 2
Example 1 R-900 40.1 4 6
Example 2 R-960 21 5 4 4

Claims

WHAT IS CLAIMED IS:
1. An aqueous polymer emulsion composition comprising a polymer having repeating units derived from at least one monomer selected from the group consisting of alkyl acrylates and alkyl methacrylates and at least one monomer having the formula:
(x(CH2=CR1-C(O)O-)R2-(O-C(O)R3)y-O-C(O)-NH)n-R4
wherein:
R1 is hydrogen or methyl,
R2 is an alkylene group or substituted alkylene group,
R3 is an alkylene group or substituted alkylene group,
R4 is an aliphatic, aromatic, cycloaliphatic or heterocydic radical having a functionality of n, n is an integer from two to four, x is an integer from one to three, and y is an integer from one to five.
2. The composition of claim 1 wherein R1 is hydrogen.
3. The composition of claim 1 wherein R2 is an ethylene group.
4. The composition of claim 1 wherein R3 is a pentamethylene group.
5. The composition of claim 1 wherein R4is the residue of a compound selected from the group consisting of isophorone di-isocyanate, tetramethylxylene di¬ isocyanate, toluene di-isocyanate, dicyclohexyl methane di-isocyanate, and trimerized hexamethylene di-isocyanate.
6. The composition of claim 1 wherein R4 is the residue of isophorone di- isocyanate.
7. The composition of claim 1 wherein R4 is the residue of tetramethylxylene di¬ isocyanate.
8. The composition of claim 1 wherein R4is the residue of toluene di-isocyanate.
9. The composition of claim 1 wherein R4 is the residue of trimerized hexamethylene di-isocyanate.
10. The composition of claim 1 wherein R4 is the residue of dicyclohexyl methane di-isocyanate.
11. The composition of claim 1 wherein x is one.
12. The composition of claim 1 wherein y is two.
13. The composition of claim 1 wherein R1 is hydrogen, R2 is an ethylene group, R3 is a pentamethylene group, R4 is the residue of a compound selected from the group consisting of isophorone di-isocyanate, tetramethylxylene di-isocyanate, toluene di-isocyanate, dicyclohexyl methane di-isocyanate, and trimerized hexamethylene di-isocyanate, x is one and y is two.
14. The composition of claim 1 wherein the amount of said monomer of said formula is less than about 50% by weight of the total monomers.
15. The composition of claim 1 wherein the amount of said monomer of said formula is from about 0.1% to about 30% by weight.
16. The composition of claim 1 wherein the amount of said monomer of said formula is from about 1 % to about 20% by weight.
17. The composition of claim 1 wherein the amount of said monomer of said formula is from about 5% to about 15% by weight of the total monomers.
18. The composition of claim 1 wherein said monomer selected from the group consisting of alkyl acrylates and alkyl methacrylates is selected from the group consisting of acrylates and methacrylates of alcohols selected from the group consisting of methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, sec-butyl, n-amyl, isoamyl, t-amyl, n-hexyl, 2-ethylbutyl, cyclohexyl, 2-heptyl, n-octyl, 2-ethylhexyl, n- decyl, and n-undecyl.
19. The composition of claim 1 wherein said monomer selected from the group consisting of alkyl acrylates and alkyl methacrylates is a plasticizing monomer such that a homopolymer of the monomer will exhibit a glass transition temperature of less than about -30°C.
20. The composition of claim 1 wherein said monomer selected from the group consisting of alkyl acrylates and alkyl methacrylates is selected from the group consisting of acrylates of straight chain alkyls having from 3 to 11 carbon atoms and branched chain alkyls having from 5 to 11 carbon atoms.
21. The composition of claim 1 wherein said monomer is selected from the group consisting of alkyl acrylates and alkyl methacrylates is selected from the group consisting of 2-ethylhexyl acrylate, methylmethacrylate and mixtures thereof.
22. A printing ink comprising a colorant and a binder for said colorant comprising an aqueous emulsion polymer as claimed in claim 1.
23. A method of coating a substrate comprising (i) contacting a surface of a substrate with a composition comprising a printing ink as claimed in claim 2 and (ii) drying said surface to form a film of the solids of said ink in contact with said surface.
PCT/US1996/018284 1995-11-30 1996-11-25 Acrylic emulsions useful in printing inks WO1997019993A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US777995P 1995-11-30 1995-11-30
US60/007,779 1995-11-30

Publications (2)

Publication Number Publication Date
WO1997019993A1 true WO1997019993A1 (en) 1997-06-05
WO1997019993A9 WO1997019993A9 (en) 1997-08-14

Family

ID=21728106

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US1996/018284 WO1997019993A1 (en) 1995-11-30 1996-11-25 Acrylic emulsions useful in printing inks

Country Status (1)

Country Link
WO (1) WO1997019993A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006052381A1 (en) * 2004-11-03 2006-05-18 Johnson Polymer, Llc Color enhancing emulsions
CN116925596A (en) * 2023-07-04 2023-10-24 青岛点石文具用品有限公司 Quick-drying ink free of feathering and preparation method thereof

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4847329A (en) * 1987-06-30 1989-07-11 Union Carbide Corporation (N-substituted carbamoyloxy)alkanoyloxyalkyl acrylate polymers and compositions made therefrom
US5342891A (en) * 1987-06-30 1994-08-30 Union Carbide Chemicals & Plastics Technology Corporation (N-substituted carbamoyloxy) alkanoyloxyalkyl acrylate polymers and compositions made therefrom

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4847329A (en) * 1987-06-30 1989-07-11 Union Carbide Corporation (N-substituted carbamoyloxy)alkanoyloxyalkyl acrylate polymers and compositions made therefrom
US5342891A (en) * 1987-06-30 1994-08-30 Union Carbide Chemicals & Plastics Technology Corporation (N-substituted carbamoyloxy) alkanoyloxyalkyl acrylate polymers and compositions made therefrom

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006052381A1 (en) * 2004-11-03 2006-05-18 Johnson Polymer, Llc Color enhancing emulsions
US7717992B2 (en) 2004-11-03 2010-05-18 Basf Corporation Color enhancing emulsions
US8168266B2 (en) 2004-11-03 2012-05-01 Basf Corporation Method for changing the color of a substrate coating by application of a stimulus
US8663377B2 (en) 2004-11-03 2014-03-04 Basf Corporation Method for changing color of substrate coating by application of stimulus
CN116925596A (en) * 2023-07-04 2023-10-24 青岛点石文具用品有限公司 Quick-drying ink free of feathering and preparation method thereof

Similar Documents

Publication Publication Date Title
US8691888B2 (en) Vinyl chloride resin emulsion, aqueous ink, and recording sheet
EP1732962B1 (en) Aqueous vinyl oligomer and vinyl polymer compositions
CA2453185A1 (en) Energy curable polymeric ink compositions
US5523335A (en) Printing inks and related laminates and processes
US5545678A (en) Polymer systems, process for their preparation, and their use for printing inks
US5714526A (en) Method of preparing resin/pigment compositions for printing inks
CN109689811A (en) Dispersion
US6338875B1 (en) Heat resistant emulsion resins
US4940744A (en) Insolubilizing system for water based inks
US20100240772A1 (en) Pigment-free, aqueous polymer dispersions marked with fluorescent dyes, process for their preparation and their use
EP0732344B1 (en) Polymers useful as printing vehicles
EP0758673B1 (en) Method for improving drying speed in printing process and fast dry printing ink used therein
US5616364A (en) Aqueous compositions useful as printing vehicles
EP1448649A1 (en) Water-borne aqueous epoxy-ester/acrylate and poly(urethane-urea) based crosslinked resins
JP3289314B2 (en) Aqueous coating composition
US5623041A (en) Polymers useful as printing vehicles
WO1997019993A1 (en) Acrylic emulsions useful in printing inks
WO1997019993A9 (en) Acrylic emulsions useful in printing inks
EP3198079A1 (en) Paper coatings
JP3593224B2 (en) Aqueous printing ink composition and method for producing printed matter using the same
JP3792815B2 (en) Coating composition and production method and use
JP7177963B1 (en) Aqueous ink composition for shrink label
CA2166412A1 (en) Copolymers useful as printing vehicles
JPH10158564A (en) Aqueous printing ink composition and production of printed matter by using the same
WO1997019992A1 (en) Acrylic emulsions useful in printing inks

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): CA MX

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): AT BE CH DE DK ES FI FR GB GR IE IT LU MC NL PT SE

DFPE Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101)
COP Corrected version of pamphlet

Free format text: PAGES 22-24,CLAIMS,REPLACED BY NEW PAGES BEARING THE SAME NUMBER;DUE TO LATE TRANSMITTAL BY THE RECEIVING OFFICE

121 Ep: the epo has been informed by wipo that ep was designated in this application
122 Ep: pct application non-entry in european phase
NENP Non-entry into the national phase

Ref country code: CA