WO2002000748A1 - Fine latex and seed method of making - Google Patents

Fine latex and seed method of making Download PDF

Info

Publication number
WO2002000748A1
WO2002000748A1 PCT/US2000/033651 US0033651W WO0200748A1 WO 2002000748 A1 WO2002000748 A1 WO 2002000748A1 US 0033651 W US0033651 W US 0033651W WO 0200748 A1 WO0200748 A1 WO 0200748A1
Authority
WO
WIPO (PCT)
Prior art keywords
latex
particles
fluorinated
highly fluorinated
alkyl
Prior art date
Legal status (The legal status 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 status listed.)
Ceased
Application number
PCT/US2000/033651
Other languages
French (fr)
Inventor
Prabhakara S. Rao
Jimmie R. Baran, Jr.
Naiyong Jing
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
3M Innovative Properties Co
Original Assignee
3M Innovative Properties Co
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 3M Innovative Properties Co filed Critical 3M Innovative Properties Co
Priority to JP2002505870A priority Critical patent/JP2004501996A/en
Priority to AT00991406T priority patent/ATE267221T1/en
Priority to EP00991406A priority patent/EP1299440B1/en
Priority to AU2001232637A priority patent/AU2001232637A1/en
Priority to DE60010938T priority patent/DE60010938T2/en
Publication of WO2002000748A1 publication Critical patent/WO2002000748A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F285/00—Macromolecular compounds obtained by polymerising monomers on to preformed graft polymers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F290/00—Macromolecular compounds obtained by polymerising monomers on to polymers modified by introduction of aliphatic unsaturated end or side groups
    • C08F290/02—Macromolecular compounds obtained by polymerising monomers on to polymers modified by introduction of aliphatic unsaturated end or side groups on to polymers modified by introduction of unsaturated end groups
    • C08F290/04—Polymers provided for in subclasses C08C or C08F
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F290/00—Macromolecular compounds obtained by polymerising monomers on to polymers modified by introduction of aliphatic unsaturated end or side groups
    • C08F290/02—Macromolecular compounds obtained by polymerising monomers on to polymers modified by introduction of aliphatic unsaturated end or side groups on to polymers modified by introduction of unsaturated end groups
    • C08F290/06—Polymers provided for in subclass C08G
    • C08F290/062—Polyethers
    • G—PHYSICS
    • G02—OPTICS
    • G02F—OPTICAL DEVICES OR ARRANGEMENTS FOR THE CONTROL OF LIGHT BY MODIFICATION OF THE OPTICAL PROPERTIES OF THE MEDIA OF THE ELEMENTS INVOLVED THEREIN; NON-LINEAR OPTICS; FREQUENCY-CHANGING OF LIGHT; OPTICAL LOGIC ELEMENTS; OPTICAL ANALOGUE/DIGITAL CONVERTERS
    • G02F1/00—Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics
    • G02F1/01—Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics for the control of the intensity, phase, polarisation or colour 
    • G02F1/165—Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics for the control of the intensity, phase, polarisation or colour  based on translational movement of particles in a fluid under the influence of an applied field
    • G02F1/166—Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics for the control of the intensity, phase, polarisation or colour  based on translational movement of particles in a fluid under the influence of an applied field characterised by the electro-optical or magneto-optical effect
    • G02F1/167—Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics for the control of the intensity, phase, polarisation or colour  based on translational movement of particles in a fluid under the influence of an applied field characterised by the electro-optical or magneto-optical effect by electrophoresis

Definitions

  • This invention relates to a very fine latex of dispersed particles in a highly fluorinated liquid solvent and a method of making which involves an initial seed particle formation step.
  • US Pat. No. 5,397,669 discloses liquid toners for use with perfluorinated solvents. The patent discloses that the compositions are film-forming, allowing them to function properly as toners. ('669 at p. 8 Ins. 3-5).
  • the ' 669 patent discloses pigment particles bound to a polymer that is highly fluorinated in specific parts, and that includes monomer units having groups that bind polyvalent metal ions.
  • the '669 patent also discloses pigment particles bound to a polymer that is highly fluorinated in its entirety, without requiring monomers having groups that bind polyvalent metal ions.
  • 5,530,053 (Minnesota Mining & Manufacturing) also discloses liquid toners for use with perfluorinated solvents.
  • the toners of '053 are polymeric dyes which are highly fluorinated in specified parts and have attached chromophoric groups.
  • the '053 patent discloses that the toner can form a latex in perfluorinated solvent, where the toner takes a core-shell form with the hydrocarbon portion in the core and the fluorocarbon portion in the shell.
  • the present invention provides a two-step method of making a latex in a highly fluorinated liquid solvent, including a first step of polymerizing together a mixture of: i) 1-2 parts by weight of one or more non-fluorinated free-radically- polymerizable monomers, and ii) 1-9 parts by weight of one or more highly fluorinated macromers terminated at one or more sites with free-radically-polymerizable groups to form a dispersion of seed particles; and a second step of polymerizing together said seed particles with an additional 10-1,000 percent by weight, relative to the total weight of the seed particles, of one or more non-fluorinated free-radically-polymerizable monomers.
  • the present invention provides a fine latex comprising a highly fluorinated liquid solvent and dispersed particles having an average particle size of 250 nm or less and more preferably 200 nm or less.
  • the present invention provides an electrophoretic display comprising the non-film-forming latex herein, wherein said dispersed particles may be alternately a) removed from dispersion by application of an electric field, and b) redispersed by removal or reversal of said electric field.
  • reacting dyes means dyes which are covalently bound to the polymer;
  • non-reacting dyes means dyes which are not substantially incorporated into a polymer by polymerization, including every dye that is not a reacting dye;
  • highly fluorinated means containing fluorine in an amount of 40 wt% or more, but preferably 50 wt% or more and more preferably 60 wt% or more, and refers to the fluorine content of a population of chemical moieties where applicable, such as in the term, "one or more highly fluorinated macromers";
  • non-fluorinated means containing substantially no fluorine, i.e. containing fluorine in an amount of 5 wt% or less, but preferably 1 wt% or less and most preferably 0 wt%, and refers to the fluorine content of a population of chemical moieties where applicable, such as in the term, "one or more non-fluorinated free- radically-polymerizable monomers";
  • C(number) refers to a chemical moiety containing the indicated number of carbon atoms
  • (meth)acrylate means acrylate and methacrylate
  • substituted means, for a chemical species, substituted by conventional substituents which do not interfere with the desired product or process, e.g., substituents can be alkyl, alkoxy, aryl, phenyl, halo (F, Cl, Br, I), cyano, etc.
  • the present invention provides a two-step method of making a latex in a highly fluorinated liquid solvent, including a first step of polymerizing together a mixture of: i) 1-2 parts by weight of one or more non-fluorinated free-radically-polymerizable monomers, and ii) 1-9 parts by weight of one or more highly fluorinated macromers terminated at one or more sites with free-radically-polymerizable groups to form a dispersion of seed particles; and a second step of polymerizing together said seed particles with an additional 10-1,000 percent by weight, relative to the total weight of the seed particles, of one or more non-fluorinated free-radically-polymerizable monomers.
  • the latex according to the present invention is preferably a non-film-forming latex comprising a highly fluorinated liquid solvent and dispersed particles comprising a polymer comprising units according to formula I: (fcp)- A / ⁇ 0) Q Q
  • the particles contain reacting or non-reacting dyes.
  • the particles additionally contain charging agents.
  • each R 1 is independently selected from -H, -CH 3 , -F and -Cl; wherein each -R 6 - is independently selected from divalent substituted or unsubstituted C1-C10 alkylene, cyclic alkylene, or arylene groups.
  • the (fcp) moieties may terminate at A groups at one or both ends.
  • the (hep) moieties may terminate at A groups at one or both ends, or at more than two ends if the (hep) moiety is branched due to the inclusion of a crosslinker.
  • a single molecule may contain numerous A groups linked by (hep) groups.
  • the fluorocarbon polymer (fcp) portions are preferably highly fluorinated macromers.
  • Preferred macromers include macromers of monomers selected from fluoroalkyl acrylates, fluoroalkyl methacrylates, fluoroalkyl haloacrylates and fluoroalkyl halomethacrylates.
  • these macromers are fluoropolymer chains comprising units according to formula HI:
  • each R 1 is independently selected from -H, -CH , -F and -Cl; each n is independently selected from integers from 1 to 10; and each R is selected independently from: highly fluorinated substituted or unsubstituted C 1 -C20 alkyl, cyclic alkyl, or aryl groups; -N(R 3 )SO 2 R 4 , where each -R 3 is selected independently from -H and substituted or unsubstituted C1-C8 alkyl, and where each -R 4 is selected independently from highly fluorinated substituted or unsubstituted C1-C20 alkyl, cyclic alkyl, or aryl groups.
  • -R 1 groups are -H or -CH 3 .
  • n is 1 or 2, more preferably 1.
  • -R 2 is a highly fluorinated C1-C20 alkyl group, more preferably a highly fluorinated C1-C8 alkyl group.
  • the -R 2 groups of the (fcp) are a mixture selected from highly fluorinated C1-C8 alkyl groups and -N(R 3 )SO 2 R 4 , where -R 3 is selected from C1-C8 alkyl groups -R 4 is selected from highly fluorinated C1-C8 alkyl groups.
  • (fcp) are polyfluoroalykylethers, preferably those comprising one or more units according to the formula -(CF 2 ) a CFXO-, where a is 0-3, but most preferably 1, and X is -F, -CF 3 or -CF 2 CF 3 but most preferably -F. More preferred polyfluoroalykylethers comprise units according to the formula -CF 2 CF 2 O-.
  • Preferred polyfluoroalykylethers are those according to the formula -NHCO 2 (CH 2 ) p (CF 2 ) q -O-(CF 2 CF 2 O) m (CF 2 ) r (CH 2 ) s OH when (fcp) is monovalent or -NHCO 2 (CH 2 ) p (CF 2 ) q -O-(CF 2 CF 2 O) m (CF 2 ) r (CH 2 ) s CO 2 NH- when (fcp) is divalent, where p is 1-4, q is 1-5, r is 1-5, s is 1-4, m is 1-50. Preferably p is 1-2. Preferably q is 1-2.
  • r is 1-2.
  • s is 1-2.
  • p is equal to s and q is equal to r.
  • m is 5-20 and more preferably 7-15.
  • the chain may alternately te ⁇ ninate with — F in place of -(CH 2 ) s OH in the formula above.
  • the hydrocarbon polymer (hep) groups are preferably non-fluorinated macromers (including co-macromers) of (meth)acrylate and other ethylenically unsaturated monomers such as styrenes.
  • the hydrocarbon polymer (hep) macromers are preferably polymers or copolymers of one or more of the following preferred monomers.
  • Especially preferred monomers of this group include ethyl (rneth)acrylate, methyl (meth)acrylate and isobornyl (meth)acrylate, butyl (meth)acrylate, isobutyl (meth)acrylate, t-butyl (meth)acrylate, hydroxypropyl (meth)acrylate, acetoacetoxyethyl (meth)acrylate.
  • Preferred monomers also include styrene or substituted styrene monomers such as methylstyrene.
  • the hydrocarbon polymer (hep) portions preferably include non-fluorinated crosslinkers, and are therefore branched.
  • Preferred crosslinkers include polyacrylates such as PEG Diacrylate with a molecular weight of preferably between 200 and 2000.
  • the (hep) portion of the particles contains one or more of: crosslinkers, cyclic or polycyclic monomers, aromatic monomers, and C12 or larger substituted or unsubstituted alkyl monomers. More preferably the (hep) portion of the particles contains one or more of: crosslinkers, cyclic or polycyclic monomers and aromatic monomers.
  • the hydrocarbon polymer (hep) portions may also include reacting dyes which are incorporated into the polymer chain as monomer units.
  • Such reacting dyes contain a chromogenic portion and a reactive portion, which are not exclusive of each other.
  • the reactive portion is a free-radically-polymerizable group, such as a vinyl or (meth)acrylate group.
  • a free-radically-polymerizable group is added to a dye by derivatization with isocyanatoethyl methacrylate.
  • the dye is suspended in a solvent such as FC-75 by sonication and an equivalent of isocyanatoethyl methacrylate is added dropwise, followed by two drops of dibutyltin dilaurate catalyst and continued sonication and agitation for 1 hour.
  • a preferred reacting dye and method of preparation is disclosed in the examples below.
  • the dispersed particles may also include non-reacting dyes.
  • the non-reacting dyes have greater affinity for the particles than for the solvent and are therefore contained in the particles.
  • the non-reacting dyes have greater affinity for the (hep) portions of the particle than for the (fcp) portions or the solvent.
  • Preferred non- reacting dyes are disclosed in the examples below.
  • the particles according to the present invention preferably contain no particulate pigments.
  • the particles take the form of a hydrocarbon-polymer-rich core and a fluoropolymer-rich shell. It is believed that most dyes are incorporated in the core due to compatibility with the hydrocarbon material of the core. Thus it is believed that reducing the fluoropolymer content of the particles improves the optical properties of the particle by allowing easier access to the dyed core, hi addition, it is believed that reducing the fluoropolymer content of the particles can improve the particle's resistance to film formation.
  • the particles are composed of 40-99 percent by weight non-fluorinated hydrocarbon polymer and 1-60 percent by weight highly fluorinated fluoropolymer.
  • the particles are composed of 60-99 percent by weight non-fluorinated hydrocarbon polymer. More preferably the particles are composed of 1-40 percent by weight highly fluorinated fluoropolymer. Most preferably the particles are composed of 1 - 10 percent by weight highly fluorinated fluoropolymer. However, greater fluoropolymer content is acceptable as particle size is decreased. In particles of less than 200nm average diameter, the particles are preferably composed of 10-40 percent by weight highly fluorinated fluoropolymer, more preferably 10-25 percent by weight highly fluorinated fluoropolymer.
  • the dispersed particles may also include charging agents.
  • the charging agent renders the particle mobile under the influence of an electric field.
  • the charge imparted to the particles by the charging agent creates an electrostatic repulsion between particles which improves resistance to film formation.
  • the charging agent has a greater affinity for the particles than for the solvent and is therefore contained in the particles.
  • the charging agent has a greater affinity for the (hep) portions of the particle than for the (fcp) portions or the solvent.
  • the charging agent is preferably cationic, more preferably a quaternary ammonium cation.
  • Preferred charging agents include l-ethyl-3-methyl-lH-imidazolium bis(trifluoromethylsulfonylamide), which may be prepared as disclosed in the examples below; (C 4 H 9 ) 3 N:HOC(O)-C 7 F 15 ; (CaEt ⁇ - ⁇ N* OC(O)-C 7 F 15 ; (GIH- -JN* OC(O)-C 9 F 19 ; C Fi 5 -CO 2 H; and combinations thereof.
  • Latexes according to the present invention preferably demonstrate a high conductance as measured by the method described in the examples below. Measured conductance is taken to reflect the charge/mass ratio (charge density) of the particles in suspension, whether imparted by the charging agent or inherent in the particle itself.
  • Preferred latexes according to the present invention have a conductance of 1 picomho/cm or more, more preferably 4 picomho/cm or more, and most preferably 9 picomho/cm or more.
  • lower conductance is acceptable when particle size is decreased, h particles of less than 200nm average diameter, conductance is preferably 0.1 picomho/cm or more.
  • the average diameter (particle size) for the dispersed particles of the latex is preferably measured by the method described in the examples below. Smaller particles are preferred for a number of reasons, including greater and faster mobility and lesser tendency to form a film. Preferably the particles have an average diameter of 1000 nm or less, more preferably 350 nm or less, more preferably 300 nm or less, more preferably 250 nm or less, and most preferably 200 nm or less.
  • the seed method of latex formation described below has been found to produce exceptionally fine particles. That method and the resulting fine particles are preferred.
  • the solvent may be any suitable highly fluorinated solvent.
  • the solvent is preferably a fluorocarbon, especially a branched or unbranched, cyclic or non-cyclic fluoroalkane.
  • Preferred solvents include FLUORTNERTTM fluorinated solvents available from 3M Company, St. Paul, Minnesota. Two especially preferred solvents are FLUORTNERT FC-75, a perfluorinated C 8 solvent, CAS No. [86508-42-1], and FLUORTNERT FC-84, a perfluorinated C 7 solvent, CAS No. [86508-42-1].
  • the density of particles in solvent maybe any level at which the dispersion is stable and does not significantly coagulate.
  • the solids content may be any level that allows proper functioning over repeated cycles.
  • the solids content is less than 10 wt%, more preferably less than 5 wt%, and most preferably less than 2 wt%.
  • the latexes according to the present invention may be incorporated into electrophoretic displays.
  • a typical display comprises two planar electrodes defining a thin gap between them which holds the latex. When a sufficient voltage of the correct polarity is applied, the suspended particles are drawn out of suspension and onto one electrode.
  • That electrode which is substantially transparent, forms the inner surface of a viewing glass, such that the particles form an image viewed through the glass.
  • the latex of the present invention must return to suspension when the voltage is removed or reversed.
  • the latexes of the present invention have high resistance to film formation when used in electrophoretic display devices.
  • an actual device may be used or a breadboard device as described in the examples below. Latexes of any solids content may be tested but preferably the solids content is 1 wt%. The device is preferably used in a normal manner, alternately applying and removing (or reversing) the typical use voltage.
  • the voltage should be sufficient to remove particles from suspension and create an image when applied.
  • the latexes are non-film-forming to the extent that they redisperse completely (by appearance to the naked eye) after at least twenty cycles, more preferably after at least 100 cycles, and most preferably after at least 10,000 cycles.
  • the resistance to film formation demonstrated by the latexes of the present invention is aided by incorporation of crosslinkers, by the choice of high Tg monomers such as 3,4 methyl styrene, isobornyl acrylate, by reduction of the fluoropolymer content resulting in a thinner outer shell zone, by increasing the electrostatic charge (conductance) of the particles, by exclusion of particulate pigments, which may be replaced with dyes.
  • the latexes and particles according to the present invention are preferably non-film-forming due to one or more of the preceding conditions.
  • any suitable method of synthesis which results in the latexes according to the present invention may be used.
  • One method of making latexes according to the present invention is illustrated by the syntheses of latexes LI to LI 5 in the Examples below.
  • a highly fluorinated macromer is synthesized by polymerization and the macromer is then derivatized to add a terminal polymerizable group.
  • the macromer is then polymerized together with non-fluorinated monomers, preferably using a polymerization initiator and optionally a crosslinker, to form the latex particle.
  • Reacting dyes must be added prior to polymerization.
  • Non-reacting dyes and charging agents may be added at any stage, but are preferably added prior to polymerization. All reactions preferably take place in a highly fluorinated solvent.
  • the reaction mixture is no more concentrated than 15 wt% reactants relative to the amount of solvent.
  • a more preferred method of making the latexes of the present invention is designated the seed method, and is illustrated by the syntheses of latexes LI 6 to LI 8 in the Examples below.
  • the polymerization to form the latex particles is performed in two steps. First, the highly fluorinated macromer and a fraction of the non-fluorinated monomers are polymerized with agitation to form a population of seed particles.
  • the weight ratio of highly fluorinated macromer to non-fluorinated monomer is preferably between 1 :2 and 9:1.
  • the remainder of the non- fluorinated monomers are added.
  • the amount of additional monomer is preferably at least 10% of the weight of the seed particles, and preferably not more than 20 times the weight of the seed particles.
  • the reaction mixture is no more concentrated than 15 wt% reactants relative to the amount of solvent.
  • the seed method can achieve a smaller average particle diameter, preferably 250 nm or less, and more preferably 200 nm or less.
  • TRIGONOXTM 21C-50 (50%) is a trade designation for a thermal free radical polymerization initiator available from Akzo Nobel Chemicals, Inc., Watertown, Connecticut.
  • FLUORINERTTM materials are fluorinated solvents available from 3M
  • FLUORTNERT FC-75 is a perfluorinated C 8 solvent, CAS No. [86508-42-1].
  • FLUORINERT FC-84 is a perfluorinated C 7 solvent, CAS No. [86508-42-1].
  • FLUORADTM materials are fluorinated surfactants/surface modifiers available from 3M Company, St. Paul, Minnesota.
  • FLUORAD FC-740 is 50% fluoroaliphatic polymeric esters in naphtha, CAS No. [64742-94-5].
  • FLUORAD FC-171 is a mixture of 87-93% fluorinated alkylalkoxylate, CAS no. [68958-61-2]; 4-10 % fluorinated alkylsulfonamide, CAS no. [4151-50-2]; and 2-4 % fluorinated alkylsulfonamide, CAS no. [68958-60-1].
  • FLUORAD FC-722 is a 2% solution of fluorinated copolymer in perfluorinated C 5 -i 8 solvent, CAS No. [86508-42-1].
  • FLUORAD FC-430 is a 98.5% solution of fluoroaliphatic polymeric esters in toluene.
  • FLUORAD FC-189 is 2-(N- butylperfluorooctanesulfonamido)ethyl acrylate.
  • FLUORAD FC-170C is 68 wt% perfluoroalkylsulfonamido oxyethylene adduct [29117-08-6], 12 wt% polyethylene glycol, 7 wt% water, approx.
  • Lithium bis(trifluoromethylsulfonyl)amide is available under the trade designation HQ-115 from 3M Company, St. Paul, Minnesota.
  • lH,lH-perfluoroalkyl methacrylate is available under the trade designation L-1987 from 3M Company, St. Paul, Minnesota.
  • lH,lH-perfluorooctyl acrylate is available from Exfluor Corp., Austin, TX.
  • PEG (400) diacrylate is a polyethylene glycol diacrylate available from Polysciences, hie, Los Angeles, California.
  • FLUORADTM FC-3275 is a blue dye in perfluorinated C 7 -C 8 solvents available from 3M Company of St. Paul, Minnesota.
  • GENSOLVETM 2000 is dichlorofluoromethane CAS No. 1717-00-6; also labeled as hydrochlorofluorocarbon HCFA-141b.
  • Fluorocarbon macromers designated FMD-1, FMD-2, FMD-3 and FMD-4 were synthesized using the components listed in Table I and the procedure described following.
  • a mixture of the monomers indicated in Table I was dissolved in the indicated solvent (FluorinertTM FC-75 or FC-84) to make a 50% (by weight) solution, in a three- neck flask equipped with a reflux condenser, nitrogen inlet tube and addition funnel.
  • the specified amount of 3-mercapto-l,2-propanediol was added as a chain transfer agent.
  • the mixture was flushed with nitrogen for 20 minutes.
  • the specified amount of the indicated polymerization initiator Trigonox 21C-50 or 2,2'-azobisisobutyronitrile
  • White (non-dye-bearing) acrylic latexes designated LI, L2, L3, L4 and L5, were synthesized using the components listed in Table ⁇ and the procedure described following.
  • a charging agent l-ethyl-3- methyl-lH-imidazolium bis(trifluoromethylsulfonylamide)
  • a polymerization initiator TrigonoxTM 21C-50
  • TrigonoxTM 21C-50 was added in an amount of 0.1-0.2 % by weight of the reaction mixture. This reaction mixture was flushed with nitrogen for 20 minutes and then the mixture was polymerized for 12 hrs at 75 °C. A second increment of the initiator in the same amount was added and the mixture was polymerized for another 12 hrs at 75 °C. The resulting latex was then filtered through a thickly folded cheese cloth to remove agglomerated particles.
  • the resulting latexes contained a solids content of about 5 wt%. Solids content was measured by evaporating a known weight of the latex to dryness by heating to 100° C in a vacuum oven and weighing of the remaining dry solids.
  • Particle size and size distribution were measured using a Coulter N4 PLUS dynamic light scattering photometer (Coulter Corp., Miami, FL) with a measuring range of 3 nm to 3 ⁇ m. Particle size and size distributions were obtained at the high dilution range set by the instrument.
  • Conductance reported in Table TL, was measured using a Scientifica Model 627 conductivity meter (available from Scientifica of Princeton, New Jersey) using a stainless steel concentric cylinder probe. A frequency of 18 Hz was applied to the outer cylinder. The conductivity of the liquid sample was determined by measuring the current between the outer cylinder and the inner cylinder. Higher conductance is indicative of higher charge/mass ratio, which indicates that the particles may be more easily moved by application of an electric field.
  • Film-forming characteristics were tested in a breadboard display device, which included a transparent indium tin oxide electrode coated on an essentially planar high refractive index display glass opposite an essentially planar metal counter electrode.
  • the gap between electrodes was 5-10 ⁇ m.
  • the volume between the display glass electrode and the counter electrode was filled with the latex to be tested and a voltage of 10 volts was applied for less than a second, driving the latex particles to the display glass.
  • a voltage of 10 volts was applied for less than a second, driving the latex particles to the display glass.
  • Non-film-forming latexes redispersed in the solvent, whereas film-forming latexes fully or partially remained on the display glass.
  • Non-film-forming latexes redisperse completely (by appearance to the naked eye) after at least twenty cycles. Film forming latexes typically would not rediperse in the first or second cycle. Toner compositions are unable to redisperse after a single cycle, consistent with their role
  • Latexes L1-L5 were found to be non-film forming.
  • Acrylic latexes LI, L2, L4 and L5 were diluted to 1 wt% dispersions in FC-75 solvent. Additional charging agent was added to the dispersion in the amount indicated and the conductivity was measured by the method described above.
  • Dye-bearing acrylic latexes designated L6 (Cyan), L7 (Cyan), L8 (Red), L9 (Yellow), L10 (Yellow), LI 1 (Violet), L12 (Magenta), L13 (Cyan) and L14 (Magenta), were synthesized using the components listed in Table TV and the procedure described following.
  • TAA isobornyl acrylate
  • MMA methyl methacrylate
  • EMA ethyl methacrylate
  • L6 (Cyan) 3 g of a mixture of FluoradTM surfactants (2:3 by weight FC-430 and FC-171) was added to enhance the stability of the dispersion.
  • the indicated hydrocarbon-soluble dye was dissolved in the monomer mixture along with a small quantity of GenesolveTM 2000 (essentially CH3CCI2F; Allied Signal, Morristown, NJ) to facilitate and accelerate the solvation of the dye.
  • a polymerization initiator, TrigonoxTM 21C-50 was added in an amount of 0.1-0.2 % by weight of the reaction mixture. This reaction mixture was flushed with nitrogen for 20 minutes and then the mixture was polymerized for 12 hrs at 75 °C. A second increment of the initiator in the same amount was added and the mixture was polymerized for another 12 hrs at 75 °C. The resulting latex was then filtered through a thickly folded cheese cloth to remove agglomerated particles. Dyes were modified as follows: PECHS salts of Basic Violet (C.I. 42555) and Basic Blue (C.I. 1) were made by exchanging cations for PECHS:
  • Derivatized Solvent Yellow 18 (C.I. 12740) was a reactive dye incorporating a function polymerizable with the acrylic monomers.
  • the derivatized dye was made as follows: 1 g of Solvent Yellow 18 (C.I. 12740) was suspended in -25 ml of FC-75 perfluorinated fluid by sonication. Isocyanatoethyl methacrylate (0.566g ) was added dropwise to the dye suspension under sonication, followed by two drops of dibutyltin dilaurate catalyst. After an hour under sonication and agitation, the suspension was filtered, washed with FC-84 and dried under vacuum below 40 °F, the dry solid being the derivatized dye.
  • the dyes were substantially entirely contained in the latex particles, presumably in the hydrocarbon polymer core. Unreacted dye was found in a coagulum obtained after filtering the latex through cheesecloth as described. The resulting latexes contained a solids content of about 5 wt%, measured as described above.
  • Latexes L6-L14 were each tested and proved to be non-film forming.
  • 2.5 g of FMD-1 and 2.5 g methylstyrene (a mixture of 3- and 4-methyl isomers obtained from Aldrich Chemical Company, Milwaukee, WI, Cat. No. 30,898-6) were added to 250 ml of FluorinertTM solvent FC-75, in a three-neck flask equipped with a reflux condenser, nitrogen inlet tube and addition funnel.
  • TrigonoxTM 21C-50 was added. This reaction mixture was flushed with nitrogen for 15 minutes and then the mixture was polymerized for about 100 minutes at 80 °C with vigorous stirring using a magnetic stir bar.
  • a white turbid suspension of seed polymer particles resulted.
  • the temperature of the reaction mixture was lowered to 70 °C with continued stirring and another 1 part TrigonoxTM 21C-50 was added.
  • An additional 10 g of the methylstyrene was added dropwise via an addition funnel into the stirred reaction mixture over a period of 2 hours while the reaction temperature was kept at 70 °C.
  • the resulting latex was then filtered through a thickly folded cheese cloth to remove agglomerated particles.
  • the latex had an average particle size of 220nm and a conductance of 0.1 picomho/cm, measured as described above.
  • a fluoromacromer dispersant designated FMD-5 based on a perfluoropolyether was synthesized as follows.
  • the perfluoroether diol HO-CH 2 CF2-O-(CF2CF2O) n -CF2CH2-OH was synthesized, where n is a distribution (nominally 10) and the diol has an average molecular weight of 1250.
  • Polyethylene glycol (ave. m.w. 600)(Aldrich Chemical Co., Milwaukee, Wis.) was mixed with approximately two equivalents of CH C(O)Cl at ambient temperature in the presence of two equivalents of triethylamine to form a diacetate.
  • the diacetate was then fluorinated by direct fluorination, such as disclosed in U.S. Pat No 4,523,039 (Lagow et al.).
  • the resulting fluorinated acetate was mixed with excess amount of methanol whereupon it reacted to give methyl esters such as CH 3 O(CO)CF 2 O-(CF 2 CF 2 O) n-2 -CF 2 (CO)OCH 3 .
  • methyl esters were then reduced to the corresponding dihydroalcohols, such as HOCH CF 2 O-(CF 2 CF 2 O) n- -CF 2 CH 2 OH, by reaction with approximately two equivalents of NaBH .
  • the resulting mixture was distilled under reduced pressure and a 1250 m.w. fraction collected.
  • Acrylic latexes designated LI 9 (Cyan) and L20 (Near- White) were synthesized as follows.
  • L19(Cyan) 5 g of FMD-5 was combined with 12.5 g methylstyrene (a mixture of 3- and 4-methyl isomers obtained from Aldrich Chemical Company, Milwaukee, WI, Cat. No. 30,898-6), 5 g of GensolveTM 2000, 0.2 g Solvent Blue (C.L 97) and 250 g of FluorinertTM solvent FC-75, in a three-neck flask equipped with a reflux condenser, nitrogen inlet tube and addition funnel.
  • a polymerization initiator TrigonoxTM 21C-50, was added in the amount of 1 g. This reaction mixture was flushed with nitrogen for 30 minutes and then the mixture was polymerized for 6 hrs at 75 °C. A second increment of the initiator in the same amount was added and the mixture was polymerized for another 20 hrs at 75 °C. The resulting latex was then filtered through a thickly folded cheese cloth to remove agglomerated particles. The resulting cyan colored latex, designated LI 9 (Cyan), had an average particle size of 172 nm, measured as described above.
  • L20 Near- White
  • Magenta Solvent Dye CAS 58559-02-7
  • the resulting latex was a near-white pale pink color and had an average particle size of 170 nm, measured as described above.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Nonlinear Science (AREA)
  • Molecular Biology (AREA)
  • Electrochemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Physics & Mathematics (AREA)
  • Optics & Photonics (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Polymerisation Methods In General (AREA)
  • Medicines Containing Antibodies Or Antigens For Use As Internal Diagnostic Agents (AREA)
  • Peptides Or Proteins (AREA)

Abstract

The present invention provides a two-step method of making a latex in a highly fluorinated liquid solvent, including a first step of polymerizing together a mixture of: i) 1-2 parts by weight of one or more non-fluorinated free-radically-polymerizable monomers, and ii) 1-9 parts by weight of one or more highly fluorinated macromers terminated at one or more sites with free-radically-polymerizable groups to form a dispersion of seed particles; and a second step of polymerizing together said seed particles with an additional 10-1,000 percent by weight, relative to the total weight of the seed particles, of one or more non-fluorinated free-radically-polymerizable monomers. The present invention additionally provides a fine latex comprising a highly fluorinated liquid solvent and dispersed particles having an average particle size of 250 nm or less and more preferably 200 nm or less. The latexes of the present invention may be useful in an electrophoretic display.

Description

Fine Latex and Seed Method of Making
Field of the Invention
This invention relates to a very fine latex of dispersed particles in a highly fluorinated liquid solvent and a method of making which involves an initial seed particle formation step.
Background of the Invention
US Pat. No. 5,397,669 (Minnesota Mining & Manufacturing) discloses liquid toners for use with perfluorinated solvents. The patent discloses that the compositions are film-forming, allowing them to function properly as toners. ('669 at p. 8 Ins. 3-5). The ' 669 patent discloses pigment particles bound to a polymer that is highly fluorinated in specific parts, and that includes monomer units having groups that bind polyvalent metal ions. The '669 patent also discloses pigment particles bound to a polymer that is highly fluorinated in its entirety, without requiring monomers having groups that bind polyvalent metal ions. US Pat. No. 5,530,053 (Minnesota Mining & Manufacturing) also discloses liquid toners for use with perfluorinated solvents. The toners of '053 are polymeric dyes which are highly fluorinated in specified parts and have attached chromophoric groups. The '053 patent discloses that the toner can form a latex in perfluorinated solvent, where the toner takes a core-shell form with the hydrocarbon portion in the core and the fluorocarbon portion in the shell.
US Pat. No. 5,919,293 (Hewlett-Packard) discloses ink jet inks composed of colorants in Fluorinert™ solvents (Minnesota Mining & Manufacturing Co., St. Paul, MN), which are perfluorinated or nearly-perfluorinated alkanes.
US Pat. No. 5,573,711 (Copytele) discloses the use of certain polymeric fluorosurfactants in electrophoretic image displays. The '711 patent teaches the use of Fluorad™ surfactants (Minnesota Mining & Manufacturing Co., St. Paul, MN), including FC-171, having the structure RrSO2N(C2H5)(CH3CH3O)nCH3, where n is about 8 and Rf is a fluorocarbon portion.
Summary of the Invention Briefly, the present invention provides a two-step method of making a latex in a highly fluorinated liquid solvent, including a first step of polymerizing together a mixture of: i) 1-2 parts by weight of one or more non-fluorinated free-radically- polymerizable monomers, and ii) 1-9 parts by weight of one or more highly fluorinated macromers terminated at one or more sites with free-radically-polymerizable groups to form a dispersion of seed particles; and a second step of polymerizing together said seed particles with an additional 10-1,000 percent by weight, relative to the total weight of the seed particles, of one or more non-fluorinated free-radically-polymerizable monomers.
In another aspect, the present invention provides a fine latex comprising a highly fluorinated liquid solvent and dispersed particles having an average particle size of 250 nm or less and more preferably 200 nm or less.
In another aspect, the present invention provides an electrophoretic display comprising the non-film-forming latex herein, wherein said dispersed particles may be alternately a) removed from dispersion by application of an electric field, and b) redispersed by removal or reversal of said electric field.
What has not been described in the art, and is provided by the present invention, is a non-film-forming latex of hydrocarbon/fluorocarbon particles dispersed in a fluorocarbon solvent useful in an electrophoretic display having the small particle size and high conductance disclosed herein. hi this application:
"reacting dyes" means dyes which are covalently bound to the polymer; "non-reacting dyes" means dyes which are not substantially incorporated into a polymer by polymerization, including every dye that is not a reacting dye;
"highly fluorinated", means containing fluorine in an amount of 40 wt% or more, but preferably 50 wt% or more and more preferably 60 wt% or more, and refers to the fluorine content of a population of chemical moieties where applicable, such as in the term, "one or more highly fluorinated macromers";
"non-fluorinated", means containing substantially no fluorine, i.e. containing fluorine in an amount of 5 wt% or less, but preferably 1 wt% or less and most preferably 0 wt%, and refers to the fluorine content of a population of chemical moieties where applicable, such as in the term, "one or more non-fluorinated free- radically-polymerizable monomers";
"C(number)" refers to a chemical moiety containing the indicated number of carbon atoms; "(meth)acrylate" means acrylate and methacrylate; and
"substituted" means, for a chemical species, substituted by conventional substituents which do not interfere with the desired product or process, e.g., substituents can be alkyl, alkoxy, aryl, phenyl, halo (F, Cl, Br, I), cyano, etc.
It is an advantage of the present invention to provide a latex of non-film- forming dye-bearing particles, which latex is useful in an electrophoretic display and can be used for repeated cycles of electrophoretically removing the particles of the latex from dispersion and returning them to dispersion.
Detailed Description of Preferred Embodiments The present invention provides a two-step method of making a latex in a highly fluorinated liquid solvent, including a first step of polymerizing together a mixture of: i) 1-2 parts by weight of one or more non-fluorinated free-radically-polymerizable monomers, and ii) 1-9 parts by weight of one or more highly fluorinated macromers terminated at one or more sites with free-radically-polymerizable groups to form a dispersion of seed particles; and a second step of polymerizing together said seed particles with an additional 10-1,000 percent by weight, relative to the total weight of the seed particles, of one or more non-fluorinated free-radically-polymerizable monomers.
The latex according to the present invention is preferably a non-film-forming latex comprising a highly fluorinated liquid solvent and dispersed particles comprising a polymer comprising units according to formula I: (fcp)- A / \ 0) Q Q
wherein each (fcp) is independently selected from highly fluorinated polymer chains which may terminate at the — A= group of another unit according to formula I so as to form a polymer molecule that contains two or more A groups linked by (fcp) groups; wherein each Q is independently selected from -H and straight or branched non- fluorinated polymer chains (hep), wherein no more than one Q of each unit according to formula I may be -H, and wherein each (hep) may terminate at the -A= group of another unit according to formula I so as to form a polymer molecule that contains two or more A groups linked by (hep) groups. Preferably some of the (hep) groups are branched due to the inclusion of polyfunctional crosslinkers. Preferably the particles contain reacting or non-reacting dyes. Preferably the particles additionally contain charging agents.
Preferably the -A= group is the moiety according to formula II:
O O R1
II II I (π) -OCNH-R6-OC-C-CH2
/ \
wherein each R1 is independently selected from -H, -CH3, -F and -Cl; wherein each -R6- is independently selected from divalent substituted or unsubstituted C1-C10 alkylene, cyclic alkylene, or arylene groups. The (fcp) moieties may terminate at A groups at one or both ends. The (hep) moieties may terminate at A groups at one or both ends, or at more than two ends if the (hep) moiety is branched due to the inclusion of a crosslinker. Thus it is contemplated that a single molecule may contain numerous A groups linked by (hep) groups. The fluorocarbon polymer (fcp) portions are preferably highly fluorinated macromers. Preferred macromers include macromers of monomers selected from fluoroalkyl acrylates, fluoroalkyl methacrylates, fluoroalkyl haloacrylates and fluoroalkyl halomethacrylates. Preferably these macromers are fluoropolymer chains comprising units according to formula HI:
(-CR^CHa-) I (m)
CO2(CH2)nR2
where each R1 is independently selected from -H, -CH , -F and -Cl; each n is independently selected from integers from 1 to 10; and each R is selected independently from: highly fluorinated substituted or unsubstituted C 1 -C20 alkyl, cyclic alkyl, or aryl groups; -N(R3)SO2R4, where each -R3 is selected independently from -H and substituted or unsubstituted C1-C8 alkyl, and where each -R4 is selected independently from highly fluorinated substituted or unsubstituted C1-C20 alkyl, cyclic alkyl, or aryl groups. Preferably -R1 groups are -H or -CH3. Preferably n is 1 or 2, more preferably 1. Preferably -R2 is a highly fluorinated C1-C20 alkyl group, more preferably a highly fluorinated C1-C8 alkyl group. In another preferred embodiment, the -R2 groups of the (fcp) are a mixture selected from highly fluorinated C1-C8 alkyl groups and -N(R3)SO2R4, where -R3 is selected from C1-C8 alkyl groups -R4 is selected from highly fluorinated C1-C8 alkyl groups. In another preferred embodiment, (fcp) are polyfluoroalykylethers, preferably those comprising one or more units according to the formula -(CF2)aCFXO-, where a is 0-3, but most preferably 1, and X is -F, -CF3 or -CF2CF3 but most preferably -F. More preferred polyfluoroalykylethers comprise units according to the formula -CF2CF2O-. Preferred polyfluoroalykylethers are those according to the formula -NHCO2(CH2)p(CF2)q-O-(CF2CF2O) m(CF2)r(CH2)sOH when (fcp) is monovalent or -NHCO2(CH2)p(CF2)q-O-(CF2CF2O)m(CF2)r(CH2)sCO2NH- when (fcp) is divalent, where p is 1-4, q is 1-5, r is 1-5, s is 1-4, m is 1-50. Preferably p is 1-2. Preferably q is 1-2. Preferably r is 1-2. Preferably s is 1-2. Preferably p is equal to s and q is equal to r. Preferably m is 5-20 and more preferably 7-15. The chain may alternately teπninate with — F in place of -(CH2)sOH in the formula above.
The hydrocarbon polymer (hep) groups are preferably non-fluorinated macromers (including co-macromers) of (meth)acrylate and other ethylenically unsaturated monomers such as styrenes. The hydrocarbon polymer (hep) macromers are preferably polymers or copolymers of one or more of the following preferred monomers. Preferred monomers include monomers according to the formula: CH2=CR1-C(O)OR2, where -R1 is hydrogen or methyl and -R2 is selected from C1-C20 substituted or unsubstituted, straight-chain or branched or cyclic, alkyl or aryl groups. Especially preferred monomers of this group include ethyl (rneth)acrylate, methyl (meth)acrylate and isobornyl (meth)acrylate, butyl (meth)acrylate, isobutyl (meth)acrylate, t-butyl (meth)acrylate, hydroxypropyl (meth)acrylate, acetoacetoxyethyl (meth)acrylate. Preferred monomers also include styrene or substituted styrene monomers such as methylstyrene.
The hydrocarbon polymer (hep) portions preferably include non-fluorinated crosslinkers, and are therefore branched. Preferred crosslinkers include polyacrylates such as PEG Diacrylate with a molecular weight of preferably between 200 and 2000. In order to improve resistance to film-fonning, preferably the (hep) portion of the particles contains one or more of: crosslinkers, cyclic or polycyclic monomers, aromatic monomers, and C12 or larger substituted or unsubstituted alkyl monomers. More preferably the (hep) portion of the particles contains one or more of: crosslinkers, cyclic or polycyclic monomers and aromatic monomers.
The hydrocarbon polymer (hep) portions may also include reacting dyes which are incorporated into the polymer chain as monomer units. Such reacting dyes contain a chromogenic portion and a reactive portion, which are not exclusive of each other. Preferably the reactive portion is a free-radically-polymerizable group, such as a vinyl or (meth)acrylate group. In one preferred embodiment, a free-radically-polymerizable group is added to a dye by derivatization with isocyanatoethyl methacrylate. In one procedure, the dye is suspended in a solvent such as FC-75 by sonication and an equivalent of isocyanatoethyl methacrylate is added dropwise, followed by two drops of dibutyltin dilaurate catalyst and continued sonication and agitation for 1 hour. A preferred reacting dye and method of preparation is disclosed in the examples below. The dispersed particles may also include non-reacting dyes. The non-reacting dyes have greater affinity for the particles than for the solvent and are therefore contained in the particles. Preferably the non-reacting dyes have greater affinity for the (hep) portions of the particle than for the (fcp) portions or the solvent. Preferred non- reacting dyes are disclosed in the examples below. The particles according to the present invention preferably contain no particulate pigments.
Without wishing to be bound by theory, it is believed that the particles take the form of a hydrocarbon-polymer-rich core and a fluoropolymer-rich shell. It is believed that most dyes are incorporated in the core due to compatibility with the hydrocarbon material of the core. Thus it is believed that reducing the fluoropolymer content of the particles improves the optical properties of the particle by allowing easier access to the dyed core, hi addition, it is believed that reducing the fluoropolymer content of the particles can improve the particle's resistance to film formation. Preferably the particles are composed of 40-99 percent by weight non-fluorinated hydrocarbon polymer and 1-60 percent by weight highly fluorinated fluoropolymer. More preferably the particles are composed of 60-99 percent by weight non-fluorinated hydrocarbon polymer. More preferably the particles are composed of 1-40 percent by weight highly fluorinated fluoropolymer. Most preferably the particles are composed of 1 - 10 percent by weight highly fluorinated fluoropolymer. However, greater fluoropolymer content is acceptable as particle size is decreased. In particles of less than 200nm average diameter, the particles are preferably composed of 10-40 percent by weight highly fluorinated fluoropolymer, more preferably 10-25 percent by weight highly fluorinated fluoropolymer.
The dispersed particles may also include charging agents. The charging agent renders the particle mobile under the influence of an electric field. In addition, the charge imparted to the particles by the charging agent creates an electrostatic repulsion between particles which improves resistance to film formation. Like non-reacting dyes, the charging agent has a greater affinity for the particles than for the solvent and is therefore contained in the particles. Preferably the charging agent has a greater affinity for the (hep) portions of the particle than for the (fcp) portions or the solvent. The charging agent is preferably cationic, more preferably a quaternary ammonium cation. Preferred charging agents include l-ethyl-3-methyl-lH-imidazolium bis(trifluoromethylsulfonylamide), which may be prepared as disclosed in the examples below; (C4H9)3N:HOC(O)-C7F15; (CaEtø-μN* OC(O)-C7F15; (GIH- -JN* OC(O)-C9F19; C Fi5-CO2H; and combinations thereof.
Latexes according to the present invention preferably demonstrate a high conductance as measured by the method described in the examples below. Measured conductance is taken to reflect the charge/mass ratio (charge density) of the particles in suspension, whether imparted by the charging agent or inherent in the particle itself. Preferred latexes according to the present invention have a conductance of 1 picomho/cm or more, more preferably 4 picomho/cm or more, and most preferably 9 picomho/cm or more. However, lower conductance is acceptable when particle size is decreased, h particles of less than 200nm average diameter, conductance is preferably 0.1 picomho/cm or more.
The average diameter (particle size) for the dispersed particles of the latex is preferably measured by the method described in the examples below. Smaller particles are preferred for a number of reasons, including greater and faster mobility and lesser tendency to form a film. Preferably the particles have an average diameter of 1000 nm or less, more preferably 350 nm or less, more preferably 300 nm or less, more preferably 250 nm or less, and most preferably 200 nm or less. The seed method of latex formation described below has been found to produce exceptionally fine particles. That method and the resulting fine particles are preferred. The solvent may be any suitable highly fluorinated solvent. The solvent is preferably a fluorocarbon, especially a branched or unbranched, cyclic or non-cyclic fluoroalkane. Preferred solvents include FLUORTNERT™ fluorinated solvents available from 3M Company, St. Paul, Minnesota. Two especially preferred solvents are FLUORTNERT FC-75, a perfluorinated C8 solvent, CAS No. [86508-42-1], and FLUORTNERT FC-84, a perfluorinated C7 solvent, CAS No. [86508-42-1].
The density of particles in solvent (solids content) maybe any level at which the dispersion is stable and does not significantly coagulate. For use of the latex in an electrophoretic display, the solids content may be any level that allows proper functioning over repeated cycles. Preferably, the solids content is less than 10 wt%, more preferably less than 5 wt%, and most preferably less than 2 wt%. The latexes according to the present invention may be incorporated into electrophoretic displays. A typical display comprises two planar electrodes defining a thin gap between them which holds the latex. When a sufficient voltage of the correct polarity is applied, the suspended particles are drawn out of suspension and onto one electrode. That electrode, which is substantially transparent, forms the inner surface of a viewing glass, such that the particles form an image viewed through the glass. In contradiction to the characteristics of an electrostatic toner, which must form a permanent image under analogous conditions, the latex of the present invention must return to suspension when the voltage is removed or reversed. The latexes of the present invention have high resistance to film formation when used in electrophoretic display devices. To determine resistance to film formation, an actual device may be used or a breadboard device as described in the examples below. Latexes of any solids content may be tested but preferably the solids content is 1 wt%. The device is preferably used in a normal manner, alternately applying and removing (or reversing) the typical use voltage. The voltage should be sufficient to remove particles from suspension and create an image when applied. Preferably the latexes are non-film-forming to the extent that they redisperse completely (by appearance to the naked eye) after at least twenty cycles, more preferably after at least 100 cycles, and most preferably after at least 10,000 cycles. Without wishing to be bound by theory, it is believed that the resistance to film formation demonstrated by the latexes of the present invention is aided by incorporation of crosslinkers, by the choice of high Tg monomers such as 3,4 methyl styrene, isobornyl acrylate, by reduction of the fluoropolymer content resulting in a thinner outer shell zone, by increasing the electrostatic charge (conductance) of the particles, by exclusion of particulate pigments, which may be replaced with dyes. The latexes and particles according to the present invention are preferably non-film-forming due to one or more of the preceding conditions.
Any suitable method of synthesis which results in the latexes according to the present invention may be used. One method of making latexes according to the present invention is illustrated by the syntheses of latexes LI to LI 5 in the Examples below. In this method, a highly fluorinated macromer is synthesized by polymerization and the macromer is then derivatized to add a terminal polymerizable group. The macromer is then polymerized together with non-fluorinated monomers, preferably using a polymerization initiator and optionally a crosslinker, to form the latex particle. Reacting dyes must be added prior to polymerization. Non-reacting dyes and charging agents may be added at any stage, but are preferably added prior to polymerization. All reactions preferably take place in a highly fluorinated solvent. Preferably the reaction mixture is no more concentrated than 15 wt% reactants relative to the amount of solvent.
A more preferred method of making the latexes of the present invention is designated the seed method, and is illustrated by the syntheses of latexes LI 6 to LI 8 in the Examples below. In this method the polymerization to form the latex particles is performed in two steps. First, the highly fluorinated macromer and a fraction of the non-fluorinated monomers are polymerized with agitation to form a population of seed particles. The weight ratio of highly fluorinated macromer to non-fluorinated monomer is preferably between 1 :2 and 9:1. In the second step, the remainder of the non- fluorinated monomers are added. The amount of additional monomer is preferably at least 10% of the weight of the seed particles, and preferably not more than 20 times the weight of the seed particles. Preferably the reaction mixture is no more concentrated than 15 wt% reactants relative to the amount of solvent. The seed method can achieve a smaller average particle diameter, preferably 250 nm or less, and more preferably 200 nm or less.
This invention is useful in electrophoretic image displays. Objects and advantages of this invention are further illustrated by the following examples, but the particular materials and amounts thereof recited in these examples, as well as other conditions and details, should not be construed to unduly limit this invention. Examples
Materials
The following materials were used in these examples. Where not otherwise noted, all chemicals and reagents may be available from Aldrich Chemical Co., Milwaukee, WI.
TRIGONOX™ 21C-50 (50%) is a trade designation for a thermal free radical polymerization initiator available from Akzo Nobel Chemicals, Inc., Watertown, Connecticut. FLUORINERT™ materials are fluorinated solvents available from 3M
Company, St. Paul, Minnesota. FLUORTNERT FC-75 is a perfluorinated C8 solvent, CAS No. [86508-42-1]. FLUORINERT FC-84 is a perfluorinated C7 solvent, CAS No. [86508-42-1].
FLUORAD™ materials are fluorinated surfactants/surface modifiers available from 3M Company, St. Paul, Minnesota. FLUORAD FC-740 is 50% fluoroaliphatic polymeric esters in naphtha, CAS No. [64742-94-5]. FLUORAD FC-171 is a mixture of 87-93% fluorinated alkylalkoxylate, CAS no. [68958-61-2]; 4-10 % fluorinated alkylsulfonamide, CAS no. [4151-50-2]; and 2-4 % fluorinated alkylsulfonamide, CAS no. [68958-60-1]. FLUORAD FC-722 is a 2% solution of fluorinated copolymer in perfluorinated C5-i8 solvent, CAS No. [86508-42-1]. FLUORAD FC-430 is a 98.5% solution of fluoroaliphatic polymeric esters in toluene. FLUORAD FC-189 is 2-(N- butylperfluorooctanesulfonamido)ethyl acrylate. FLUORAD FC-170C is 68 wt% perfluoroalkylsulfonamido oxyethylene adduct [29117-08-6], 12 wt% polyethylene glycol, 7 wt% water, approx. 5 wt %.perfluoroalkylsulfonamido oxyethylene adduct [56372-23-7], and approx. 5 wt. % perfluoroalkylsulfonamido oxyethylene adduct [68298-79-3].
Lithium bis(trifluoromethylsulfonyl)amide is available under the trade designation HQ-115 from 3M Company, St. Paul, Minnesota. lH,lH-perfluoroalkyl methacrylate is available under the trade designation L-1987 from 3M Company, St. Paul, Minnesota. lH,lH-perfluorooctyl acrylate is available from Exfluor Corp., Austin, TX. PEG (400) diacrylate is a polyethylene glycol diacrylate available from Polysciences, hie, Los Angeles, California.
Dibutyltin dilaurate, isocyanatoethyl methacrylate, vinyl trifluoroacetate, 3- mercapto-l,2-propanediol, 2,2'-azobis(isobutyronitrile), isobornyl methacrylate, methyl methacrylate, ethyl methacrylate , l-ethyl-3-methyl-lH-imidazolium chloride, 2,2,2- trifiuoroethyl acrylate, and dimethylaminoethyl methacrylate are available from Aldrich Chemical Co., Milwaukee, Wisconsin and other general chemical suppliers.
Mercaptopropyltrimethoxysilane was obtained from United Chemical Technologies, h e, Petrarch Systems, Bristol, Pennsylvania. OXSOL™ R 2000 is α, ,α-trifluoromethyltoluene, available from Occidental
Chemical Corp., Dallas, Texas.
FLUORAD™ FC-3275 is a blue dye in perfluorinated C7-C8 solvents available from 3M Company of St. Paul, Minnesota.
GENSOLVE™ 2000 is dichlorofluoromethane CAS No. 1717-00-6; also labeled as hydrochlorofluorocarbon HCFA-141b.
Synthesis of Fluoromacromer Solvents with Polymerizable Terminal Groups
Fluorocarbon macromers designated FMD-1, FMD-2, FMD-3 and FMD-4, were synthesized using the components listed in Table I and the procedure described following.
A mixture of the monomers indicated in Table I was dissolved in the indicated solvent (Fluorinert™ FC-75 or FC-84) to make a 50% (by weight) solution, in a three- neck flask equipped with a reflux condenser, nitrogen inlet tube and addition funnel. The specified amount of 3-mercapto-l,2-propanediol was added as a chain transfer agent. The mixture was flushed with nitrogen for 20 minutes. The specified amount of the indicated polymerization initiator (Trigonox 21C-50 or 2,2'-azobisisobutyronitrile) was added. The mixture was then polymerized for 12 hrs at 75 °C. A second increment of the initiator in the same amount was added and the mixture was polymerized for another 12 hrs at 75 °C. Next, the reaction temperature was raised to 85 °C for 1 lir to destroy residual initiator. The polymer dispersion was then cooled to room temperature. Finally, the terminal group monomer, isocyanatoethyl methacrylate (TEM), was added with thorough mixing in the indicated amount, which is stoicl iometrically equimolar to the chain transfer agent, followed by two drops of dibutyltin dilaurate to complete the reaction of the isocyanate with one of the two hydroxyl end groups of the polymer.
TABLE I
Figure imgf000014_0001
Synthesis of Charging Agent, l-ethyl-3 -methyl- lH-imidazolium bisftrifluoromethylsulfonylamide') l-Ethyl-3 -methyl- lH-imidazolium chloride (49.0 g) was dissolved in 285.0 g deionized water to form a 1M solution. 127.8 ml of this solution was combined with 36.7 g lithium bis(trifluoromethylsulfonyl)amide and 50 ml dichloromethane in a flask with a magnetic stir bar. The solution was allowed to stir overnight, then transferred to a separatory funnel, where the aqueous phase was washed three times with 10 ml of dichloromethane. The three dichloromethane phases were combined and the dichloromethane was removed under reduced pressure. The recovered material was used without further purification. Synthesis of Non-Film Forming White Acrylic Latex Particles
White (non-dye-bearing) acrylic latexes, designated LI, L2, L3, L4 and L5, were synthesized using the components listed in Table π and the procedure described following. A mixture of the indicated acrylic monomers, optionally including PEG 400 diacrylate crosslinker as indicated, was suspended in 500 ml of Fluorinert™ solvent FC-75 along with the indicated fluoromacromer solvent, FMD-1 or FMD-4, in a three- neck flask equipped with a reflux condenser, nitrogen inlet tube and addition funnel. Where indicated, a mixture of the indicated Fluorad™ surfactants was added to enhance the stability of the dispersion. Where indicated, a charging agent, l-ethyl-3- methyl-lH-imidazolium bis(trifluoromethylsulfonylamide), was added. A polymerization initiator, Trigonox™ 21C-50, was added in an amount of 0.1-0.2 % by weight of the reaction mixture. This reaction mixture was flushed with nitrogen for 20 minutes and then the mixture was polymerized for 12 hrs at 75 °C. A second increment of the initiator in the same amount was added and the mixture was polymerized for another 12 hrs at 75 °C. The resulting latex was then filtered through a thickly folded cheese cloth to remove agglomerated particles.
The resulting latexes contained a solids content of about 5 wt%. Solids content was measured by evaporating a known weight of the latex to dryness by heating to 100° C in a vacuum oven and weighing of the remaining dry solids.
Particle size and size distribution, reported in Table II, were measured using a Coulter N4 PLUS dynamic light scattering photometer (Coulter Corp., Miami, FL) with a measuring range of 3 nm to 3 μm. Particle size and size distributions were obtained at the high dilution range set by the instrument. Conductance, reported in Table TL, was measured using a Scientifica Model 627 conductivity meter (available from Scientifica of Princeton, New Jersey) using a stainless steel concentric cylinder probe. A frequency of 18 Hz was applied to the outer cylinder. The conductivity of the liquid sample was determined by measuring the current between the outer cylinder and the inner cylinder. Higher conductance is indicative of higher charge/mass ratio, which indicates that the particles may be more easily moved by application of an electric field. Film-forming characteristics were tested in a breadboard display device, which included a transparent indium tin oxide electrode coated on an essentially planar high refractive index display glass opposite an essentially planar metal counter electrode. The gap between electrodes was 5-10 μm. The volume between the display glass electrode and the counter electrode was filled with the latex to be tested and a voltage of 10 volts was applied for less than a second, driving the latex particles to the display glass. After the voltage was removed, non-film-forming latexes redispersed in the solvent, whereas film-forming latexes fully or partially remained on the display glass. Non-film-forming latexes redisperse completely (by appearance to the naked eye) after at least twenty cycles. Film forming latexes typically would not rediperse in the first or second cycle. Toner compositions are unable to redisperse after a single cycle, consistent with their role in electrophotographic processes.
Latexes L1-L5 were found to be non-film forming.
Figure imgf000016_0001
Addition of Charging Agent to Non-Film Forming Acrylic Latex Particle Dispersions Acrylic latexes LI, L2, L4 and L5 were diluted to 1 wt% dispersions in FC-75 solvent. Additional charging agent was added to the dispersion in the amount indicated and the conductivity was measured by the method described above.
TABLE III
Figure imgf000017_0001
Synthesis of Non-Film Forming Dye-Bearing Acrylic Latex Particles
Dye-bearing acrylic latexes, designated L6 (Cyan), L7 (Cyan), L8 (Red), L9 (Yellow), L10 (Yellow), LI 1 (Violet), L12 (Magenta), L13 (Cyan) and L14 (Magenta), were synthesized using the components listed in Table TV and the procedure described following.
A mixture of the indicated acrylic monomers, optionally including PEG 400 diacrylate crosslinker as indicated, was suspended in 500 ml of Fluorinert™ solvent FC-75 along with 2.0 g of fluoromacromer solvent FMD-1. (TBA = isobornyl acrylate, MMA = methyl methacrylate, EMA = ethyl methacrylate). For L6 (Cyan) only, 3 g of a mixture of Fluorad™ surfactants (2:3 by weight FC-430 and FC-171) was added to enhance the stability of the dispersion. The indicated hydrocarbon-soluble dye was dissolved in the monomer mixture along with a small quantity of Genesolve™ 2000 (essentially CH3CCI2F; Allied Signal, Morristown, NJ) to facilitate and accelerate the solvation of the dye. A polymerization initiator, Trigonox™ 21C-50, was added in an amount of 0.1-0.2 % by weight of the reaction mixture. This reaction mixture was flushed with nitrogen for 20 minutes and then the mixture was polymerized for 12 hrs at 75 °C. A second increment of the initiator in the same amount was added and the mixture was polymerized for another 12 hrs at 75 °C. The resulting latex was then filtered through a thickly folded cheese cloth to remove agglomerated particles. Dyes were modified as follows: PECHS salts of Basic Violet (C.I. 42555) and Basic Blue (C.I. 1) were made by exchanging cations for PECHS:
CF2-CF2 CF3-CF2-CF CF-SO3 "
CF2-CF2
Derivatized Solvent Yellow 18 (C.I. 12740) was a reactive dye incorporating a function polymerizable with the acrylic monomers. The derivatized dye was made as follows: 1 g of Solvent Yellow 18 (C.I. 12740) was suspended in -25 ml of FC-75 perfluorinated fluid by sonication. Isocyanatoethyl methacrylate (0.566g ) was added dropwise to the dye suspension under sonication, followed by two drops of dibutyltin dilaurate catalyst. After an hour under sonication and agitation, the suspension was filtered, washed with FC-84 and dried under vacuum below 40 °F, the dry solid being the derivatized dye.
It was found that the dyes were substantially entirely contained in the latex particles, presumably in the hydrocarbon polymer core. Unreacted dye was found in a coagulum obtained after filtering the latex through cheesecloth as described. The resulting latexes contained a solids content of about 5 wt%, measured as described above.
Particle size and conductance were measured as described above. Latexes L6-L14 were each tested and proved to be non-film forming.
TABLE IV
Figure imgf000019_0002
Figure imgf000019_0001
Synthesis of Very Fine Non-Film Forming White Acrylic Latex Particles by Seed Method
A latex of very fine white (non-dye-bearing) acrylic particles, designated LI 6, was synthesized using the seed method described following. 2.5 g of FMD-1 and 2.5 g methylstyrene (a mixture of 3- and 4-methyl isomers obtained from Aldrich Chemical Company, Milwaukee, WI, Cat. No. 30,898-6) were added to 250 ml of Fluorinert™ solvent FC-75, in a three-neck flask equipped with a reflux condenser, nitrogen inlet tube and addition funnel. One gram of the polymerization initiator, Trigonox™ 21C-50, was added. This reaction mixture was flushed with nitrogen for 15 minutes and then the mixture was polymerized for about 100 minutes at 80 °C with vigorous stirring using a magnetic stir bar. A white turbid suspension of seed polymer particles resulted. The temperature of the reaction mixture was lowered to 70 °C with continued stirring and another 1 part Trigonox™ 21C-50 was added. An additional 10 g of the methylstyrene was added dropwise via an addition funnel into the stirred reaction mixture over a period of 2 hours while the reaction temperature was kept at 70 °C. After addition of monomer was complete the polymerization was allowed to continue for another 16 hours. The resulting latex was then filtered through a thickly folded cheese cloth to remove agglomerated particles. The latex had an average particle size of 220nm and a conductance of 0.1 picomho/cm, measured as described above.
Synthesis of Very Fine Non-Film Forming Dye-Bearing Acrylic Latex Particles by Seed Method
The synthesis of LI 6, preceding, was repeated except that 0.15 g of Solvent Blue (C.L 97) dye were dissolved in the 10 g of methylstyrene monomer added dropwise to the seed suspension. The resulting cyan colored latex, designated LI 7 (Cyan), had an average particle size of 375 nm; and a conductance of 0.1 picomho/cm, measured as described above. Additional Synthesis of Very Fine Non-Film Forming Dye-Bearing Acrylic Latex Particles by Seed Method
The synthesis of very fine dye-bearing latex LI 8 (Cyan), using the seed method described following, was repeated three times. In a reaction flask, 7.5 g of FMD-1 and 2.5 g ethyl acrylate were added to 250 parts ml of Fluorinert™ solvent FC-75, in a three-neck flask equipped with a reflux condenser, nitrogen inlet tube and addition funnel. One gram of the polymerization initiator, Trigonox™ 21C-50, was added. This reaction mixture was flushed with nitrogen for 30-45 minutes. The temperature was rapidly raised to 80 °C and then the mixture was polymerized for 2 hrs with vigorous stirring using a magnetic stir bar.
After two hours, a mixture of 10 g of isobornyl acrylate and 0.2 g of Solvent Blue (C.L 97) dye was added dropwise via an addition funnel into the stirred reaction mixture over a period of 1 hour while the reaction temperature was kept at 70 °C. An additional 1 g of Trigonox™ 21C-50 was added. After addition of monomer was complete the polymerization was allowed to continue for another 16-20 hours. The resulting latex was then filtered through a thickly folded cheese cloth to remove agglomerated particles. Particle size and conductance were measured as described above. In three repetitions of this synthesis, the three resulting latexes were found to have average particle sizes of 140, 160 and 175nm respectively. Conductance was measured as 0.79 picomho/cm for one of the LI 8 (Cyan) latexes.
Synthesis of Perfluoropolyether Fluoromacromer Dispersant
A fluoromacromer dispersant designated FMD-5 based on a perfluoropolyether was synthesized as follows. The perfluoroether diol HO-CH2CF2-O-(CF2CF2O)n-CF2CH2-OH was synthesized, where n is a distribution (nominally 10) and the diol has an average molecular weight of 1250. Polyethylene glycol (ave. m.w. 600)(Aldrich Chemical Co., Milwaukee, Wis.) was mixed with approximately two equivalents of CH C(O)Cl at ambient temperature in the presence of two equivalents of triethylamine to form a diacetate. The diacetate was then fluorinated by direct fluorination, such as disclosed in U.S. Pat No 4,523,039 (Lagow et al.). The resulting fluorinated acetate was mixed with excess amount of methanol whereupon it reacted to give methyl esters such as CH3O(CO)CF2O-(CF2CF2O)n-2-CF2(CO)OCH3. These methyl esters were then reduced to the corresponding dihydroalcohols, such as HOCH CF2O-(CF2CF2O)n- -CF2CH2OH, by reaction with approximately two equivalents of NaBH . The resulting mixture was distilled under reduced pressure and a 1250 m.w. fraction collected.
To 35 g of this perfluoroether diol (m.w. 1250) in a covered amber jar was added dropwise 4.34 g (aprox. 1 equivalent) of isocyanatoethyl methacrylate (m.w. 155) to obtain a milky liquid. When the milky liquid turned clear, indicating the completion of the reaction between the hydroxyl and isocyanate, two drops of dibutyltin dilaurate were added to the reaction mixture.
Synthesis of Acrylic Latex Particles Using FMD-5 Perfluoropolyether Fluoromacromer Acrylic latexes designated LI 9 (Cyan) and L20 (Near- White) were synthesized as follows. For L19(Cyan), 5 g of FMD-5 was combined with 12.5 g methylstyrene (a mixture of 3- and 4-methyl isomers obtained from Aldrich Chemical Company, Milwaukee, WI, Cat. No. 30,898-6), 5 g of Gensolve™ 2000, 0.2 g Solvent Blue (C.L 97) and 250 g of Fluorinert™ solvent FC-75, in a three-neck flask equipped with a reflux condenser, nitrogen inlet tube and addition funnel. A polymerization initiator, Trigonox™ 21C-50, was added in the amount of 1 g. This reaction mixture was flushed with nitrogen for 30 minutes and then the mixture was polymerized for 6 hrs at 75 °C. A second increment of the initiator in the same amount was added and the mixture was polymerized for another 20 hrs at 75 °C. The resulting latex was then filtered through a thickly folded cheese cloth to remove agglomerated particles. The resulting cyan colored latex, designated LI 9 (Cyan), had an average particle size of 172 nm, measured as described above.
For L20 (Near- White), the same procedure was followed except that the cyan dye was replaced with 0.2 g of Magenta Solvent Dye (CAS 58559-02-7). The resulting latex, designated L20 (Near- White), was a near-white pale pink color and had an average particle size of 170 nm, measured as described above.
Both LI 9 (Cyan) and L20 (Near- White) are observed to be non-film-forming. Various modifications and alterations of this invention will become apparent to those skilled in the art without departing from the scope and principles of this invention, and it should be understood that this invention is not to be unduly limited to the illustrative embodiments set forth hereinabove. .

Claims

We claim:
1. A method of making a latex comprising dispersed particles comprising the steps of: a) in a highly fluorinated liquid solvent, polymerizing together a mixture of: i. 1 -2 parts by weight of one or more non-fluorinated free-radically- polymerizable monomers, and ii. 1-9 parts by weight of one or more highly fluorinated macromers terminated at one or more sites with free-radically-polymerizable groups, to form a dispersion of seed particles; and b) in a highly fluorinated liquid solvent, polymerizing together said seed particles with an additional 10-1,000 percent by weight, relative to the total weight of the seed particles, of one or more non-fluorinated free-radically- polymerizable monomers.
2. The method according to claim 1 wherein said latex comprises dispersed particles having an average particle size of 250 nm or less.
3. The method according to claim 1 wherein said latex comprises dispersed particles having an average particle size of 200 nm or less.
4. The method according to claim 1, 2 or 3 wherein said mixture additionally comprises one or more dyes.
5. The method according to claim 1, 2, 3 or 4 wherein said mixture additionally comprises a charging agent.
6. The method according to claim 5 wherein said charging agent is l-ethyl-3- methyl- 1 H-imidazolium bis(trifluoromethylsulfonylamide) .
7. The method according to any of claims 1 - 6 wherein said non-fluorinated free- radically polymerizable monomers are selected from (meth)acrylate monomers.
8. The method according to any of claims 1 - 6 wherein said non-fluorinated free- radically polymerizable monomers are selected from substituted or unsubstituted - styrene monomers.
9. The method according to any of claims 1 - 8 wherein said highly fluorinated macromers are selected from macromers according to Formula TV:
O O R1 (fcp)-O
Figure imgf000025_0001
wherein each R1 is independently selected from -H, -CH3, -F and -Cl; wherein each R6 is independently selected from substituted or unsubstituted C1-C10 alkyl, cyclic alkyl, or aryl groups, wherein each (fcp) is selected from: a) fluoropolymer chains comprising units according to formula V:
(-CR^CHz-)
I (V) CO2(CH2)nR2
wherein each R1 is independently selected from -H, -CH3, -F and -Cl; wherein each n is independently selected from integers from 1 to 10; wherein each R2 is selected independently from: highly fluorinated substituted or unsubstituted C1-C20 alkyl, cyclic alkyl, or aryl groups;
-N(R )SO2R , wherein each R is selected independently from H and substituted or unsubstituted C1-C8 alkyl, and wherein each R4 is selected independently from highly fluorinated substituted or unsubstituted C1-C20 alkyl, cyclic alkyl, or aryl groups; and b) fluoropolymer chains comprising -(CF2)aCFXO- units, wherein each a is independently selected from 0-3 and wherein each X is independently selected from -F, -CF3 or -CF2CF3; wherein each (fcp) optionally terminates in another unit according to formula TV above.
10. The method according to any of claims 1 - 8 wherein said highly fluorinated macromers are selected from macromers according to Formula IV: O O R1
II II I (rv)
(fcp)-OCNH-R6-OC-C=CH2
wherein each R1 is independently selected from -H, -CH3, -F and -Cl; wherein each Rδ is independently selected from substituted or unsubstituted C1-C10 alkyl, cyclic alkyl, or aryl groups, wherein each (fcp) is selected independently from fluoropolymer chains comprising -CF2CF2O- units, and wherein each (fcp) optionally terminates in another unit according to formula TV above.
11. The method according to any of claims 1 — 10 wherein said latex is non-fϊhn- forming.
12. A latex made according to the method of any of claims 1 - 11.
13. A latex of comprising: a) a highly fluorinated liquid solvent; and b) dispersed particles having an average particle size of 250 nm or less.
14. The latex according to claim 13 wherein said dispersed particles have an average particle size of 200 nm or less.
15. An electrophoretic display comprising the latex according to claim 12, 13 or 14, wherein said dispersed particles may be alternately a) removed from dispersion by application of an electric field, and b) redispersed by removal or reversal of said electric field.
PCT/US2000/033651 2000-06-28 2000-12-12 Fine latex and seed method of making Ceased WO2002000748A1 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP2002505870A JP2004501996A (en) 2000-06-28 2000-12-12 Fine latex and seed method for producing the same
AT00991406T ATE267221T1 (en) 2000-06-28 2000-12-12 FINE PARTICLE LATEX AND ITS PRODUCTION BY A SEED CRYSTAL PROCESS
EP00991406A EP1299440B1 (en) 2000-06-28 2000-12-12 Fine latex and seed method of making
AU2001232637A AU2001232637A1 (en) 2000-06-28 2000-12-12 Fine latex and seed method of making
DE60010938T DE60010938T2 (en) 2000-06-28 2000-12-12 FINE PART LATEX AND ITS PRODUCTION BY A IMPF CRYSTAL METHOD

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US09/604,889 2000-06-28
US09/604,889 US6372838B1 (en) 2000-06-28 2000-06-28 Fine latex and seed method of making

Publications (1)

Publication Number Publication Date
WO2002000748A1 true WO2002000748A1 (en) 2002-01-03

Family

ID=24421457

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2000/033651 Ceased WO2002000748A1 (en) 2000-06-28 2000-12-12 Fine latex and seed method of making

Country Status (9)

Country Link
US (2) US6372838B1 (en)
EP (1) EP1299440B1 (en)
JP (1) JP2004501996A (en)
KR (1) KR20030014279A (en)
CN (1) CN1229410C (en)
AT (1) ATE267221T1 (en)
AU (1) AU2001232637A1 (en)
DE (1) DE60010938T2 (en)
WO (1) WO2002000748A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004027506A1 (en) * 2002-09-18 2004-04-01 Sipix Imaging, Inc. Dispersion composition for electrophoretic displays
CN100368921C (en) * 2003-01-30 2008-02-13 希毕克斯影像有限公司 High-performance capsules for electrophoretic displays

Families Citing this family (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6452038B1 (en) * 2000-06-28 2002-09-17 3M Innovative Properties Company Fluoroalkyloxy dispersant
AU2003297458A1 (en) * 2002-12-20 2004-07-22 Exxonmobil Chemical Patents Inc. Polymerization processes
US7425601B2 (en) * 2002-12-20 2008-09-16 Exxonmobil Chemical Patents Inc. Polymers with new sequence distributions
DE60332866D1 (en) * 2002-12-20 2010-07-15 Exxonmobil Chem Patents Inc POLYMERS WITH NEW SEQUENCE DISTRIBUTIONS
WO2004058827A1 (en) * 2002-12-20 2004-07-15 Exxonmobil Chemical Patents Inc. Polymerization processes
US20060108710A1 (en) * 2004-11-24 2006-05-25 Molecular Imprints, Inc. Method to reduce adhesion between a conformable region and a mold
US7307118B2 (en) * 2004-11-24 2007-12-11 Molecular Imprints, Inc. Composition to reduce adhesion between a conformable region and a mold
US20050160934A1 (en) 2004-01-23 2005-07-28 Molecular Imprints, Inc. Materials and methods for imprint lithography
US7981984B2 (en) * 2004-06-21 2011-07-19 Exxonmobil Chemical Patents Inc. Polymerization process
EP1765885A1 (en) * 2004-06-21 2007-03-28 Exxonmobil Chemical Patents Inc. Polymer recovery method
WO2006009942A1 (en) * 2004-06-21 2006-01-26 Exxonmobil Chemical Patents Inc. Polymerization process
US7662892B2 (en) 2004-06-21 2010-02-16 Exxonmobil Chemical Patents Inc. Impact copolymers
US7799882B2 (en) * 2005-06-20 2010-09-21 Exxonmobil Chemical Patents Inc. Polymerization process
US8142703B2 (en) 2005-10-05 2012-03-27 Molecular Imprints, Inc. Imprint lithography method
US20070093572A1 (en) * 2005-10-20 2007-04-26 Jayprakash Bhatt White ink
US20080110557A1 (en) * 2006-11-15 2008-05-15 Molecular Imprints, Inc. Methods and Compositions for Providing Preferential Adhesion and Release of Adjacent Surfaces
US20100109195A1 (en) 2008-11-05 2010-05-06 Molecular Imprints, Inc. Release agent partition control in imprint lithography
US8593719B2 (en) * 2009-02-09 2013-11-26 Merck Patent Gmbh Particles for electrophoretic displays
JP7346411B2 (en) * 2018-07-18 2023-09-19 大阪有機化学工業株式会社 Curable resin composition, (meth)acrylic elastomer and sheet

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0594472A2 (en) * 1992-09-18 1994-04-27 Minnesota Mining And Manufacturing Company Liquid toners for use with perfluorinated solvents
EP0683436A1 (en) * 1994-05-17 1995-11-22 Minnesota Mining And Manufacturing Company Liquid toners utilizing highly fluorinated solvents
US5573711A (en) * 1994-05-26 1996-11-12 Copytele, Inc. Planar fluorinated dielectric suspensions for electrophoretic image displays and related methods
WO1997035904A1 (en) * 1996-03-27 1997-10-02 Novartis Ag Process for manufacture of a porous polymer from a mixture

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4094911A (en) 1969-03-10 1978-06-13 Minnesota Mining And Manufacturing Company Poly(perfluoroalkylene oxide) derivatives
US4523039A (en) 1980-04-11 1985-06-11 The University Of Texas Method for forming perfluorocarbon ethers
US4894484A (en) 1985-11-08 1990-01-16 Exfluor Research Corporation Pyrolysis of perfluoropolyethers
JP2786856B2 (en) 1988-05-17 1998-08-13 株式会社リコー Electrophotographic developer
DE4006097A1 (en) 1990-02-27 1991-08-29 Hoechst Ag ETHYLENICALLY UNSATURATED, FLUORINE URETHER DERIVATIVES AND METHOD FOR THE PRODUCTION THEREOF
US5885564A (en) * 1993-08-13 1999-03-23 Lancaster Group Gmbh Functional oxygenated composition containing phospholipids and fluorocarbon
US5604070A (en) 1995-02-17 1997-02-18 Minnesota Mining And Manufacturing Company Liquid toners with hydrocarbon solvents
DE69611161T2 (en) 1995-04-04 2001-05-17 Novartis Ag, Basel POLYMERIZABLE PERFLUOROALKYL ETHER SILOXANE MACROMER
US5681881A (en) 1996-05-24 1997-10-28 Minnesota Mining And Manufacturing Company Fluoroelastomer compositions
US5919293A (en) 1997-10-31 1999-07-06 Hewlett-Packard Company Use of perfluorinated compounds as a vehicle component in ink-jet inks

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0594472A2 (en) * 1992-09-18 1994-04-27 Minnesota Mining And Manufacturing Company Liquid toners for use with perfluorinated solvents
EP0683436A1 (en) * 1994-05-17 1995-11-22 Minnesota Mining And Manufacturing Company Liquid toners utilizing highly fluorinated solvents
US5573711A (en) * 1994-05-26 1996-11-12 Copytele, Inc. Planar fluorinated dielectric suspensions for electrophoretic image displays and related methods
WO1997035904A1 (en) * 1996-03-27 1997-10-02 Novartis Ag Process for manufacture of a porous polymer from a mixture

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004027506A1 (en) * 2002-09-18 2004-04-01 Sipix Imaging, Inc. Dispersion composition for electrophoretic displays
US6958849B2 (en) 2002-09-18 2005-10-25 Sipix Imaging Inc. Electrophoretic display with improved temperature latitude and switching performance
KR100938797B1 (en) * 2002-09-18 2010-01-27 사이픽스 이미징, 인코포레이티드 Dispersion Composition for Electrophoretic Display
CN100368921C (en) * 2003-01-30 2008-02-13 希毕克斯影像有限公司 High-performance capsules for electrophoretic displays

Also Published As

Publication number Publication date
JP2004501996A (en) 2004-01-22
ATE267221T1 (en) 2004-06-15
KR20030014279A (en) 2003-02-15
US20020132910A1 (en) 2002-09-19
US6372838B1 (en) 2002-04-16
DE60010938T2 (en) 2005-05-19
EP1299440B1 (en) 2004-05-19
AU2001232637A1 (en) 2002-01-08
EP1299440A1 (en) 2003-04-09
DE60010938D1 (en) 2004-06-24
CN1454225A (en) 2003-11-05
CN1229410C (en) 2005-11-30

Similar Documents

Publication Publication Date Title
EP1299440B1 (en) Fine latex and seed method of making
EP1294680B1 (en) Fluoroalkyloxy dispersant
EP0683436B1 (en) Liquid toners utilizing highly fluorinated solvents
JP6756711B2 (en) Particles for electrophoretic display
US6384124B1 (en) Non-film-forming electrophoretic latexes in fluorocarbon solvents
JPS58105235A (en) Liquid developer used for electrostatic image
US6562889B2 (en) Dispersant in non-polar solvent
US20060142470A1 (en) Toner, method for producing the same, image formation method and image formation apparatus
JPH03113466A (en) Liquid developer for electrostatic photography
JPH04281468A (en) Liquid developer for electrostatic photography

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AE AG AL AM AT AT AU AZ BA BB BG BR BY BZ CA CH CN CR CU CZ CZ DE DE DK DK DM DZ EE EE ES FI FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ PL PT RO RU SD SE SG SI SK SK SL TJ TM TR TT TZ UA UG UZ VN YU ZA ZW

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE TR BF BJ CF CG CI CM GA GN GW ML MR NE SN TD TG

DFPE Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101)
121 Ep: the epo has been informed by wipo that ep was designated in this application
WWE Wipo information: entry into national phase

Ref document number: 2000991406

Country of ref document: EP

Ref document number: 1020027017800

Country of ref document: KR

Ref document number: 008196893

Country of ref document: CN

WWP Wipo information: published in national office

Ref document number: 1020027017800

Country of ref document: KR

WWP Wipo information: published in national office

Ref document number: 2000991406

Country of ref document: EP

REG Reference to national code

Ref country code: DE

Ref legal event code: 8642

WWG Wipo information: grant in national office

Ref document number: 2000991406

Country of ref document: EP