US20090221739A1 - Process for the Post-Modification of Homo and Copolymers Prepared by Controlled Free Radical Polymerization Processes - Google Patents

Process for the Post-Modification of Homo and Copolymers Prepared by Controlled Free Radical Polymerization Processes Download PDF

Info

Publication number
US20090221739A1
US20090221739A1 US11/794,707 US79470706A US2009221739A1 US 20090221739 A1 US20090221739 A1 US 20090221739A1 US 79470706 A US79470706 A US 79470706A US 2009221739 A1 US2009221739 A1 US 2009221739A1
Authority
US
United States
Prior art keywords
alkyl
alcohol
polymer
process according
vinyl
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.)
Abandoned
Application number
US11/794,707
Other languages
English (en)
Inventor
Ralf Knischka
Ernst Eckstein
Clemens Auschra
Akira Matsumoto
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.)
BASF Corp
Original Assignee
Individual
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 Individual filed Critical Individual
Assigned to CIBA SPECIALTY CHEMICALS CORP. reassignment CIBA SPECIALTY CHEMICALS CORP. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: MATSUMOTO, AKIRA, ECKSTEIN, ERNST, AUSCHRA, CLEMENS, KNISCHKA, RALF
Publication of US20090221739A1 publication Critical patent/US20090221739A1/en
Abandoned legal-status Critical Current

Links

Classifications

    • 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
    • C08F2/00Processes of polymerisation
    • C08F2/38Polymerisation using regulators, e.g. chain terminating agents, e.g. telomerisation
    • 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
    • C08F20/00Homopolymers and copolymers 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
    • 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
    • C08F4/00Polymerisation catalysts
    • 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
    • C08F8/00Chemical modification by after-treatment
    • C08F8/14Esterification
    • 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
    • C08F8/00Chemical modification by after-treatment
    • C08F8/30Introducing nitrogen atoms or nitrogen-containing groups
    • 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
    • C08F8/00Chemical modification by after-treatment
    • C08F8/46Reaction with unsaturated dicarboxylic acids or anhydrides thereof, e.g. maleinisation
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G81/00Macromolecular compounds obtained by interreacting polymers in the absence of monomers, e.g. block polymers
    • C08G81/02Macromolecular compounds obtained by interreacting polymers in the absence of monomers, e.g. block polymers at least one of the polymers being obtained by reactions involving only carbon-to-carbon unsaturated bonds
    • C08G81/024Block or graft polymers containing sequences of polymers of C08C or C08F and of polymers of C08G
    • C08G81/025Block or graft polymers containing sequences of polymers of C08C or C08F and of polymers of C08G containing polyether sequences
    • 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
    • C09D17/00Pigment pastes, e.g. for mixing in paints
    • 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
    • C09D7/00Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
    • C09D7/40Additives
    • C09D7/43Thickening agents
    • 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
    • C09D7/00Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
    • C09D7/40Additives
    • C09D7/45Anti-settling agents
    • 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
    • C09D7/00Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
    • C09D7/40Additives
    • C09D7/47Levelling agents
    • 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
    • C09D7/00Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
    • C09D7/40Additives
    • C09D7/65Additives macromolecular
    • 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
    • C08F2438/00Living radical polymerisation
    • C08F2438/02Stable Free Radical Polymerisation [SFRP]; Nitroxide Mediated Polymerisation [NMP] for, e.g. using 2,2,6,6-tetramethylpiperidine-1-oxyl [TEMPO]
    • 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
    • C08F2810/00Chemical modification of a polymer
    • C08F2810/30Chemical modification of a polymer leading to the formation or introduction of aliphatic or alicyclic unsaturated groups

Definitions

  • the instant invention pertains to the preparation of polymers or copolymers wherein in a first step a controlled free radical polymerization process is carried out and in a second step the resulting polymer is modified by specific polymer analogous reactions.
  • the final modified polymer or copolymer is useful as a dispersant for pigments, as leveling agent or as rheology modifier for coatings or related applications.
  • Further aspects of the invention are the thus prepared polymers or copolymers, a pigment concentrate containing the polymer or copolymer and a coating material containing the pigment concentrate.
  • Polymeric pigment dispersants are an essential part of new water based or solvent based high solids formulation technology. There is, therefore, an increasing activity in developing new products in these coating areas. So far, only a few classes of polymeric dispersants have been established in the market. In less demanding coating applications, still a lot of low molecular weight surfactants are used. In more demanding applications, e.g. automotive & industrial coatings, polymeric pigment dispersants have to be used to avoid the problems associated with low molecular weight surfactants (water sensitivity, corrosion, foam).
  • the controlled free radical polymerisation is a tool to tailor the microstructure of polymers (e.g. blockcopolymers) in a way that is favorable for dispersing and stabilizing pigments in the mill-base.
  • the combination of CFRP with subsequent post-modification of the stabilizing block allows enlarging the possible groups that can be used as pigment dispersants. With one CFRP-process a large row of different polymer materials for either waterborne or also solvent-borne high solids systems becomes available.
  • polymers or copolymers can be prepared in an easy manner, which otherwise would not be available or can be prepared only with complex reactions.
  • the inventive process comprises a selective polymer-analogous transesterification on polymers, which have been synthesized via nitroxide-mediated polymerization to provide well-defined polymer architectures.
  • This process provides polymers with distinct structural differences compared to polymers with same monomer composition, but synthesized directly from corresponding monomers without post-transesterification.
  • Monomer sequence In direct radical polymerization of two different monomers the monomer sequence statistics along the polymer chain is governed by the copolymerization parameters which in most cases will cause deviation from ideal random distribution of the different monomers. Using the inventive process, the monomer distribution which result from the transesterification step, is only governed by the transesterification reaction and can be expected to provide a more uniform i.e. random distribution along the polymer chain. 2) Residual monomers: Controlled polymerization processes can not be conducted to 100% conversion without significant decrease in livingness of the polymer chains. In well-defined block copolymer synthesis, it is therefore necessary to remove the non-reacted monomers of the first block, before the second block is prolonged with a different monomer.
  • Evaporation at reduced pressure is the easiest way to remove non-reacted monomers, but works only well for monomers with boiling point below 200° C.
  • acrylates of long chain alcohols like C12-C15-alcohols or MPEG-alcohols can not be removed form polyacrylates by distillation. Therefore it is not possible to make block copolymers of such long chain acrylates with pure block structure free of residual monomers.
  • the inventive process via transesterification circumvents the problem of residual non-removable monomers and associated problems of block contamination, is therefore capable to provide polymers with higher level of structural perfection.
  • Acrylate monomers based on unsaturated alcohols like allyl alcohol or oleyl alcohol usually react as crosslinkers.
  • unsaturated alcohols like allyl alcohol or oleyl alcohol
  • conventional radical polymerization as well as in controlled polymerization such acrylates will lead to branching and/or crosslinking, i.e. will prevent the formation of structurally clean linear polymer chains.
  • the inventive process of transesterification allows to introduce unsaturated alcohols to preformed controlled polymers with clean linear chain structure, i.e. provides access to well-defined structures e.g. block copolymers otherwise not accessible by direct radical polymerization.
  • One aspect of the invention is a process for the preparation of a modified polymer or copolymer comprising the steps
  • X represents a group having at least one carbon atom and is such that the free radical X• derived from X is capable of initiating polymerization;
  • At least one monomer used in the steps a1) or a2) is a C 1 -C 6 alkyl or hydroxy C 1 -C 6 alkyl ester of acrylic or methacrylic acid; and a second step
  • the first polymerization step is carried out according to the polymerization reactions a1) (claim 2 ).
  • the second step b) is a transesterification reaction, hydrolysis or an anhydride modification. Particularly preferred is a transesterification reaction (claim 3 ).
  • the transesterification preferably comprises the removal of the C 1 -C 6 alcohol byproduct by distillation.
  • step a1 or a2 of the above described process is carried out twice and a block copolymer is obtained wherein in the first or second radical polymerization step the monomer or monomer mixture contains 50 to 100% by weight, based on total monomers, of a C 1 -C 6 alkyl or hydroxyalkyl ester of acrylic or methacrylic acid and in the second or first radical polymerization step respectively, the ethylenically unsaturated monomer contains no primary or secondary ester bond (claim 4 ).
  • the monomer or monomer mixture contains from 50 to 100% by weight based on total monomers of a C 1 -C 6 alkyl or hydroxyalkyl ester of acrylic or methacrylic acid and in the second polymerization step the ethylenically unsaturated monomer is 4-vinyl-pyridine or pyridinium-ion, 2-vinyl-pyridine or pyridinium-ion, vinyl-imidazole or imidazolinium-ion, dimethylacrylamide, 3-dimethylaminopropylmethacrylamide, styrene, ⁇ -methyl styrene, ⁇ -methyl styrene or p-tert-butyl-styrene (claim 5 ).
  • the block copolymer is a gradient block copolymer (claim 6 ).
  • the polymer or copolymer is prepared by controlled free radical polymerization (CFRP).
  • CFRP controlled free radical polymerization
  • U.S. Pat. No. 4,581,429 discloses a free radical polymerization process by controlled or “living” growth of polymer chains, which produces defined oligomeric homopolymers and copolymers, including block and graft copolymers.
  • initiators of the partial formula R′R′′N—O—X In the polymerization process the free radical species R′R′′N—O• and •X are generated.
  • •X is a free radical group, e.g. a tert.-butyl or cyanoisopropyl radical, capable of polymerizing monomer units containing ethylene groups.
  • acyclic ring system may be part of a cyclic ring system or substituted to form a acyclic structure.
  • Suitable nitroxylethers and nitroxyl radicals are principally known from U.S. Pat. No. 4,581,429 or EP-A-621 878.
  • nitroxylethers and nitroxyl radicals are described in WO 02/4805 (Ciba) and in WO 02/100831 (Ciba).
  • Nitroxylethers and nitroxyl radicals with more than one nitroxyl group in the molecule are for example described in U.S. Pat. No. 6,573,347 (Ciba), WO 01/02345 (Ciba) and WO 03/004471 (Ciba) These compounds are ideally suitable when branched, star or comb (co)polymers are prepared.
  • alkoxyamine and nitroxylether are used as equivalents.
  • the structural element is part of a 5 or 6-membered heterocyclic ring, which optionally has an additional nitrogen or oxygen atom in the ring system.
  • Substituted piperidine, morpholine and piperazine derivatives are particularly useful.
  • G 1 , G 2 , G 3 , G 4 are independently C 1 -C 6 alkyl or G 1 and G 2 or G 3 and G 4 , or G 1 and G 2 and G 3 and G 4 together form a C 5 -C 12 cycloalkyl group;
  • G 5 , G 6 independently are H, C 1 -C 18 alkyl, phenyl, naphthyl or a group COOC 1 -C 18 alkyl;
  • X is selected from the group consisting of —CH 2 -phenyl, CH 3 CH-phenyl, (CH 3 ) 2 C-phenyl, (C 5 -C 6 cycloalkyl) 2 CCN, (CH 3 ) 2 CCN,
  • structural element of formula (I) is of formula A, B or O,
  • nitroxylethers are those of formula (Ic), (Id), (Ie), (If), (Ig) or (Ih)
  • R 201 , R 202 , R 203 and R 204 independently of each other are C 1 -C 18 alkyl, C 3 -C 18 alkenyl, C 3 -C 18 alkinyl, C 1 -C 18 alkyl, C 3 -C 18 alkenyl, C 3 -C 18 alkinyl which are substituted by OH, halogen or a group —O—C(O)—R 205 , C 2 -C 18 alkyl which is interrupted by at least one O atom and/or NR 205 group, C 3 -C 12 cycloalkyl or C 6 -C 10 aryl or R 201 and R 202 and/or R 203 and R 204 together with the linking carbon atom form a C 3 -C 12 cycloalkyl radical; R 205 , R 206 and R 207 independently are hydrogen, C 1 -C 18 alkyl or C 6 -C 10 aryl; R 208 is hydrogen, OH, C 1
  • R 201 , R 202 , R 203 and R 201 are ethyl, propyl or butyl and the remaining are methyl; or
  • R 201 and R 202 or R 203 and R 204 together with the linking carbon atom form a C 5 -C 6 cycloalkyl radical and one of the remaining substituents is ethyl, propyl or butyl.
  • X is CH 3 CH-phenyl.
  • G 11 , G 12 , G 13 and G 14 are independently C 1 -C 4 alkyl or G 11 and G 12 together and G 13 and G 14 together, or G 11 and G 12 together or G 13 and G 14 together are pentamethylene;
  • G 15 and G 16 are each independently of the other hydrogen or C 1 -C 4 alkyl;
  • X is as defined above;
  • k is 1, 2, 3, or 4 Y is O or NR 302 or when k is 1 and R 301 represents alkyl or aryl Y is additionally a direct bond;
  • R 302 is H, C 1 -C 18 alkyl or phenyl; if k is 1 R 301 is H, straight or branched C 1 -C 18 alkyl, C 3 -C 18 alkenyl or C 3 -C 18 alkinyl, which may be unsubstituted or substituted, by one or more OH, C 1 -C 8 alkoxy, carboxy, C 1 -C 8 alkoxycarbon
  • G 16 is hydrogen and G 15 is hydrogen or C 1 -C 4 alkyl, in particular methyl, and G 11 and G 13 are methyl and G 12 and G 14 are ethyl or propyl or G 11 and G 12 are methyl and G 13 and G 14 are ethyl or propyl.
  • the 4 imino compounds of formula III can be prepared for example according to E. G. Rozantsev, A. V. Chudinov, V. D. Sholle.:Izv. Akad. Nauk. SSSR, Ser. Khim. (9), 2114 (1980), starting from the corresponding 4-oxonitroxide in a condensation reaction with hydroxylamine and subsequent reaction of the OH group.
  • the compounds are described WO 02/100831 (Ciba)
  • alkyl radicals in the various substituents may be linear or branched.
  • alkyl containing 1 to 18 carbon atoms are methyl, ethyl, propyl, isopropyl, butyl, 2-butyl, isobutyl, t-butyl, pentyl, 2-pentyl, hexyl, heptyl, octyl, 2-ethylhexyl, t-octyl, nonyl, decyl, undecyl, dodecyl, tridecyl, tetradecyl, hexadecyl and octadecyl.
  • Alkenyl with 3 to 18 carbon atoms is a linear or branched radical as for example propenyl, 2-butenyl, 3-butenyl, isobutenyl, n-2,4-pentadienyl, 3-methyl-2-butenyl, n-2-octenyl, n-2-dodecenyl, iso-dodecenyl, oleyl, n-2-octadecenyl or n-4-octadecenyl.
  • alkenyl with 3 to 12, particularly preferred with 3 to 6 carbon atoms.
  • Alkinyl with 3 to 18 is a linear or branched radical as for example propinyl (—CH 2 —C ⁇ CH), 2-butinyl, 3-butinyl, n-2-octinyl, or n-2-octadecinyl. Preferred is alkinyl with 3 to 12, particularly preferred with 3 to 6 carbon atoms.
  • hydroxy substituted alkyl examples are hydroxy propyl, hydroxy butyl or hydroxy hexyl.
  • halogen substituted alkyl examples include dichloropropyl, monobromobutyl or trichlorohexyl.
  • C 2 -C 18 alkyl interrupted by at least one O atom is for example —CH 2 CH 2 —O—CH 2 —CH 3 , —CH 2 —CH 2 —O—CH 3 — or —CH 2 CH 2 —O—CH 2 —CH 2 —CH 2 O—CH 2 —CH 3 —. It is preferably derived from polyethlene glycol.
  • a general description is —((CH 2 ) a —O) b —H/CH 3 , wherein a is a number from 1 to 6 and b is a number from 2 to 10.
  • C 2 -C 18 alkyl interrupted by at least one NR 205 group may be generally described as —((CH 2 ) a —NR 205 ) b —H/CH 3 , wherein a, b and R 205 are as defined above.
  • C 3 -C 12 cycloalkyl is typically, cyclopropyl, cyclopentyl, methylcyclopentyl, dimethylcyclopentyl, cyclohexyl, methylcyclohexyl or trimethylcyclohexyl.
  • C 6 -C 10 aryl is for example phenyl or naphthyl, but also comprised are C 1 -C 4 alkyl substituted phenyl, C 1 -C 4 alkoxy substituted phenyl, hydroxy, halogen or nitro substituted phenyl.
  • alkyl substituted phenyl are ethylbenzene, toluene, xylene and its isomers, mesitylene or isopropylbenzene.
  • Halogen substituted phenyl is for example dichlorobenzene or bromotoluene.
  • Alkoxy substituents are typically methoxy, ethoxy, propoxy or butoxy and their corresponding isomers.
  • C 7 -C 9 -phenylalkyl is benzyl, phenylethyl or phenylpropyl.
  • C 5 -C 10 heteroaryl is for example pyrrol, pyrazol, imidazol, 2,4, dimethylpyrrol, 1-methylpyrrol, thiophene, furane, furfural, indol, cumarone, oxazol, thiazol, isoxazol, isothiazol, triazol, pyridine, ⁇ -picoline, pyridazine, pyrazine or pyrimidine.
  • R is a monovalent radical of a carboxylic acid, it is, for example, an acetyl, propionyl, butyryl, valeroyl, caproyl, stearoyl, lauroyl, acryloyl, methacryloyl, benzoyl, cinnamoyl or ⁇ -(3,5-di-tert-butyl-4-hydroxyphenyl)propionyl radical.
  • C 1 -C 18 alkanoyl is for example, formyl, propionyl, butyryl, octanoyl, dodecanoyl but preferably acetyl and C 3 -C 5 alkenoyl is in particular acryloyl.
  • polymerization process a1) is very suitable.
  • process a1) the nitroxylether according to the structures outlined above splits between the O—X bond.
  • the regulating fragment in formula (I) corresponds to the O—N fragment and the initiating fragment (In) corresponds to the C centered radical of the group X.
  • nitroxylethers and nitroxyl radicals are those of formulae
  • the polymer or copolymer is prepared with a compound of formula (O1)
  • the initiator compound is present in an amount of from 0.01 mol-% to 30 mol-%, more preferably in an amount of from 0.1 mol-% to 20 mol-% and most preferred in an amount of from 0.1 mol-% to 10 mol-% based on the monomer or monomer mixture.
  • the free radical initiator is preferably an azo compound, a peroxide, perester or a hydroperoxide.
  • radical sources are 2,2′-azobisisobutyronitrile, 2,2′-azobis(2-methyl-butyronitrile), 2,2′-azobis(2,4-dimethylvaleronitrile), 2,2′-azobis(4-methoxy-2,4-dimethylvaleronitrile), 1,1′-azobis(1-cyclohexanecarbonitrile), 2,2′-azobis(isobutyramide) dihydrate, 2-phenylazo-2,4-dimethyl-4-methoxyvaleronitrile, dimethyl-2,2′-azobisisobutyrate, 2-(carbamoylazo)isobutyronitrile, 2,2′-azobis(2,4,4-trimethylpentane), 2,2′-azobis(2-methylpropane), 2,2′-azobis(N,N′-dimethyleneisobutyramidine), free base or hydrochloride, 2,2′-azobis(2-amidinopropane), free base or hydrochloride, 2,
  • the radical source is preferably present in an amount of from 0.01 mol-% to 30 mol-%, more preferred in an amount of from 0.1 mol-% to 20 mol-% and most preferred in an amount of from 0.5 mol-% to 10 mol-% based on the monomer or monomer mixture.
  • the molar ratio of the radical source to the nitroxyl radical may be from 1:10 to 10:1, preferably from 1:5 to 5:1 and more preferably from 1:2 to 2:1.
  • the polymer or copolymer can also be prepared in a controlled way by atom transfer radical polymerization (ATRP). This type of polymerization is, for example, described in WO 96/30421.
  • ATRP atom transfer radical polymerization
  • RAFT Reversible addition fragmentation chain transfer polymerization
  • the polymer or copolymer prepared according to steps a1) or a2) has preferably a polydispersity index of 1.0 to 2.2, more preferably from 1.1 to 1.9 and most preferably from 1.1 to 1.5.
  • the second reaction step i.e. the polymer analogous reaction
  • the polymer analogous reaction is a transesterification reaction, an amidation, hydrolysis or anhydride modification or a combination thereof.
  • Hydrolysis means the cleavage of an ester bond under alkaline or acidic conditions and can be carried out when the polymer or copolymer contains ester functionalities.
  • the degree of hydrolysis may vary in a wide range and depends on reaction time and conditions. For example 5 to 100%, preferably 10% to 70% of the ester functionalities may be hydrolized, to form the free acid group, from which also a salt can be prepared.
  • the metal ion is preferably an alkali metal ion, such as Li + , Na + or Ka + or an ammonium cation, such as NH 4 + or NR 404 , wherein R 404 is hydrogen or C 1 -C 18 alkyl.
  • Anhydride modification can be carried out when the polymer or copolymer contains hydroxyl functionalities.
  • the hydroxyl functionalities come for example from hydroxyl functional monomers, such as hydroxyethyl acrylate or methacrylate.
  • Virtually all aliphatic or aromatic anhydrides can be used in the modification process. Examples for anhydrides are maleic acid anhydride, pyromelitic acid anhydride, cyclohexyldiacid anhydride, succinic acid anhydride, camphoric acid anhydride.
  • Transesterification means to replace the alcohol radical in an ester group of the polymer or copolymer by another alcohol radical.
  • the alcohol radical to be replaced is methanol, ethanol, propanol or butanol.
  • the transesterification reaction is carried out at elevated temperatures, typically 70-200° C., by reacting the CFRP polymer with the corresponding alcohol using well-known catalysts, such as tetra-isopropyltitanate, tetra-butyltitanate, alkali- or earth alkali alcoholates like NaOMe or LiOMe.
  • the low boiling product alcohol is removed from the transterification reaction mixture by distillation. If needed, catalyst residues may be removed by adsorption or extraction or otherwise processed or inactivated by known methods, like hydrolysis with water or acids.
  • the choice of the replacing alcohol is important.
  • the replacing alcohol controls the properties of the resulting copolymer.
  • a polar replacing alcohol such as alcohols having e.g. the following formula R—[O—CH 2 —CH 2 —] n —OH, e.g. MPEG-OH
  • R—[O—CH 2 —CH 2 —] n —OH e.g. MPEG-OH
  • solubility depends on the amount of transesterified monomer units. At least 40% of the units should be transesterified to obtain the desired effect.
  • non polar alcohols like higher molecular weight branched aliphatic alcohols can be beneficial.
  • alcohols containing siloxane groups are preferred, e.g. with the following formula
  • solid copolymer If a solid copolymer is required, solid alcohols or polar alcohols which are able to raise the glass transition temperature (Tg) or impart side chain crystallinity should be used.
  • Tg glass transition temperature
  • polar alcohols which are able to raise the glass transition temperature (Tg) or impart side chain crystallinity should be used.
  • An example is behenyl alcohol.
  • the replacing alcohol radical is typically an aliphatic C 6 -C 36 alcohol or a precursor of an alcohol, having at least one —OH group.
  • the alcohol may also be interrupted by 1 to 20 O or N atoms or substituted by halogen, perfluoralkyl, NH 2 , NH(C 1 -C 18 alkyl), N(C 1 -C 18 alkyl) 2 , COO(C 1 -C 18 alkyl), CON(C 1 -C 18 alkyl) 2 , CONH(C 1 -C 18 alkyl), CONH 2 , COOH, COO ⁇ , O(C 1 -C 18 alkyl) or with a Si, P or S containing group, for example alkylhydroxysilicones.
  • the alcohol may also contain heterocylic ring structures, such as 1-(2-hydroxyethyl)-2-pyrrolidinone, 1-(2-hydroxyethyl)-2-imidazolidinone, 2-(2-hydroxyethyl)pyridine, N-2-hydroxyethyl)phtalimide, 4-(2-hydroxyethyl)morpholine, 1-(2-hydroxyethyl)piperazine, N-hydroxymethylphthalimide, 3-hydroxymethylpyridine or (4-pyridyl)-1-propanol.
  • heterocylic ring structures such as 1-(2-hydroxyethyl)-2-pyrrolidinone, 1-(2-hydroxyethyl)-2-imidazolidinone, 2-(2-hydroxyethyl)pyridine, N-2-hydroxyethyl)phtalimide, 4-(2-hydroxyethyl)morpholine, 1-(2-hydroxyethyl)piperazine, N-hydroxymethylphthalimide, 3-hydroxymethylpyridine or (4-pyridyl)-1
  • the alcohols which are interrupted by O or N atoms are not limited to 36 C atoms. These can be oligomeric or polymeric alcohols also. Examples of alcohols interrupted by O atoms are methoxypolyethyleneglycols or all kinds of adducts of ethyleneoxide and/or propyleneoxide (EO/PO). Such EO/PO-adducts can be random or block type structures.
  • the alcohol is an unsubstituted linear or branched C 8 -C 36 alkyl mono alcohol or a mono alcohol derived from ethylenoxide, propylenoxide or mixtures thereof with up to 100 C atoms. (Claim 11 ).
  • fatty acid alcohol ethoxylates alkylphenolethoxylates, alkoxylates of all kinds of monofunctional alcohols or phenols or secondary amines.
  • the alkoxylate is an ethoxylate of a primary alcohol or alkylphenol of structure (A):
  • R is saturated or unsaturated, linear or branched chain alkyl with 1-22 carbon atoms, or alkylaryl or dialkylaryl with up to 24 carbon atoms and n is 1 to 50.
  • the alcohol is an unsubstituted linear or branched C 8 -C 36 alkyl mono alcohol. (Claim 13 ).
  • An example is iso C12-C15 alcohol.
  • Non-polar polymers or copolymers are obtained.
  • the macroalcohol is a primary OH-functional silicone oligomer.
  • R is C 1 -C 18 alkyl, phenyl or C 7 -C 15 aralkyl; n is 1 to 50 and R′ is a linking group with 1 to 20 carbon atoms. (Claim 14 ).
  • Typical linking groups are C 1 -C 18 alkylene, phenylene or C 1 -C 18 alkylene interrupted by 1 to 6 oxygen atoms.
  • the alcohol is a partly or fully fluorinated primary alcohols.
  • examples of commercial fluorinated alcohol mixtures are: Zonyl BA®, Zonyl BA-L®, Zonyl BA-LD®, Zonyl BA-N® from Du Pont (claim 15 ).
  • Aryl is phenyl or naphthyl, preferably phenyl.
  • Precursors of alcohols are for example macroalcohols, such as poly- ⁇ -caprolactone oligomers or ⁇ -caprolactone adducts and similar lactone adducts (e.g. based on valerolactone) or mixed adducts of ⁇ -caprolactone and valerolactone.
  • Typical lactone adducts are adducts of ⁇ -caprolactone to long chain fatty alcohols of structure:
  • R is saturated or unsaturated, linear or branched chain alkyl with 8-22 carbon atoms or alkylaryl or dialkylaryl with up to 24 carbon atoms and n is 1 to 50.
  • macroalcohols based on polyolefins which have typically molecular weights up to 5000, preferably up to 2000.
  • Yet another embodiment are unsaturated alcohols containing carbon-carbon double bonds or carbon triple bonds.
  • An example is oleyl alcohol.
  • Regarding triple bond preferred are primary alkinols like propargyl alcohol and higher homologues like alkylsubstituted propargylalcohol.
  • the alcohol is a primary or secondary alcohol. Most preferred are primary alcohols or alcohol mixtures.
  • the alcohol or alcohol mixture is non-volatile and has a boiling point or range of at least 100° C., more preferably of at least 200° C.
  • the alcohol is a monoalcohol.
  • amidation there is understood the modification of the ester function of a polyacrylate with an amine under the formation of an amide bond.
  • the amine is a monofunctional primary or secondary amine, most preferably a primary aliphatic or aromatic amine.
  • the reaction of the amine with the ester function of the CFRP polymer is typically conducted at elevated temperatures of 70-200° C., optionally in presence of catalysts. In a preferred process, the resulting alcohol is removed during the amidation reaction by distillation.
  • the amine has a high boiling point or boiling range of above 100° C.
  • Typical amines are primary aliphatic or aromatic amines with up to 36 carbon atoms, linear, branched or cyclic.
  • the amine may contain heteroatoms O or N.
  • oligomers and macroamines with a single primary amine and molecular weights of up to 5000.
  • Typical examples are primary amine end-functional alkoxylates.
  • Especially preferred are also primary amines containing other polar groups like ether, ester and amide groups.
  • An ⁇ is a anion of a monovalent organic or inorganic acid; Me is a monovalent metal atom or the ammonium ion. Z is oxygen or sulfur (claim 10 ).
  • R b as C 2 -C 100 alkoxy interrupted by at least one O atom are of formula
  • R c is C 1 -C 25 alkyl, phenyl or phenyl substituted by C 1 -C 18 alkyl
  • R d is hydrogen or methyl
  • v is a number from 1 to 50.
  • These monomers are for example derived from non ionic surfactants by acrylation of the corresponding alkoxylated alcohols or phenols.
  • the repeating units may be derived from ethylene oxide, propylene oxide or mixtures of both.
  • An ⁇ wherein An ⁇ and R a have the meaning as defined above and R a is methyl, benzyl or benzoylbenzyl.
  • An ⁇ is preferably Cl ⁇ , Br ⁇ or ⁇ O 3 S—O—CH 3 .
  • Me + is an alkali metal cation or the ammonium cation.
  • Useful are also silicone functional (meth)acrylates.
  • R a is hydrogen or methyl
  • R b is NH 2 , gycidyl, unsubstituted or with hydroxy substituted C 1 -C 4 alkoxy, unsubstituted C 1 -C 4 alkylamino, di(C 1 -C 4 alkyl)amino, hydroxy-substituted C 1 -C 4 alkylamino or hydroxy-substituted di(C 1 -C 4 alkyl)amino
  • Z is oxygen.
  • the ethylenically unsaturated monomer is selected from the group consisting of ethylene, propylene, n-butylene, i-butylene, styrene, substituted styrene, conjugated dienes, acrolein, vinyl acetate, vinylpyrrolidone, vinylimidazole, maleic anhydride, (alkyl)acrylic acid-anhydrides, (alkyl)acrylic acid salts, (alkyl)acrylic esters, (alkyl)acrylonitriles, (alkyl)acrylamides, vinyl halides or vinylidene halides.
  • the ethylenically unsaturated monomer is styrene, substituted styrene, methylacrylate, ethylacrylate, butylacrylate, isobutylacrylate, tert. butylacrylate, hydroxyethylacrylate, hydroxypropylacrylate, dimethylaminoethylacrylate, methyl(meth)acrylate, ethyl-(meth)acrylate, butyl(meth)acrylate, hydroxyethyl(meth)acrylate, hydroxypropyl(meth) acrylate, dimethylaminoethyl(meth)acrylate, acrylonitrile, methacrylonitrile, acrylamide, methacrylamide or dimethylaminopropyl-methacrylamide.
  • Very suitable monomers are for example styrene, C 1 -C 8 alkylesters of acrylic or methacrylic acid, such as n-butylacrylate or methacrylate, acrylonitrile or methacrylonitrile, in particular styrene, acrylonitrile and n-butylacrylate.
  • R a is hydrogen or C 1 -C 4 alkyl
  • R b is NH 2 , O ⁇ (Me + ), glycidyl, unsubstituted C 1 -C 18 alkoxy, C 2 -C 100 alkoxy interrupted by at least one N and/or O atom, or hydroxy-substituted C 1 -C 18 alkoxy, unsubstituted C 1 -C 18 alkylamino, di(C 1 -C 18 alkyl)amino, hydroxy-substituted C 1 -C 18 alkylamino or hydroxy-substituted di(C 1 -C 18 alkyl)amino, —O—CH 2 —CH 2 —N(CH 3 ) or —O—CH 2 —CH 2 N + H(CH 3 ) 2 An ⁇ ; An ⁇ is a anion of a monovalent organic or inorganic acid; Me is a monovalent metal atom or the ammonium
  • All possible polymer chain structures are comprised: e.g. linear or branched. If the monomers are selected from chemically different monomers, all possible monomer sequence structures are comprised, e.g. random-, blocklike, multiblock-, tapered- or gradient arrangement of the different monomers.
  • block copolymers which are prepared in such a way, that the intersection between the two blocks is not a sharp boundary, but represents a continuous transition from one type of monomer to another type of monomer, i.e. both monomers extending to both blocks.
  • This type of polymers can be obtained when the polymerization process is carried out for example in one step using monomers of different copolymerization parameters or by a multistep procedure, in which the monomer composition is stepwise changed by addition of appropriate amounts of another type of monomer.
  • Another preferred procedure for the synthesis of gradient polymers is by using continuous feed processes, in which for example the controlled polymerization is started with a first monomer and before complete conversion, a second monomer is continuously fed to the reaction mixture, thus realizing a continuous transition along the polymer chains.
  • the monomer or monomer mixture of the first radical polymerization contains from 50 to 100% by weight based on total monomers of a C 1 -C 4 alkyl or hydroxyalkyl ester of acrylic or methacrylic acid and the second radical polymerization contains a monomer or monomer mixture possessing no primary or secondary ester bond.
  • Suitable monomers for the second radical polymerization do not react in the postmodification reaction, such as vinyl aromatic monomers or vinyl-aza-heterocycles.
  • Examples are 4-vinyl-pyridine(pyridinium-ion), 2-vinyl-pyridine(pyridinium-ion), vinyl-imida-zole(imidazolinium-ion), dimethylacrylamide, acrylnitrile, 3-dimethylaminopropylmethacrylamide, styrene or substituted styrenes.
  • the monomer or monomer mixture contains from 50 to 100% by weight based on total monomers of a C 1 -C 6 alkyl or hydroxyalkyl ester of acrylic or methacrylic acid and in the second polymerization the ethylenically unsaturated monomer is 4-vinyl-pyridine or pyridinium-ion, 2-vinyl-pyridine or pyridinium-ion, vinyl-imidazole or imidazolinium-ion, dimethylacrylamide, 3-dimethylaminopropylmethacrylamide, styrene, ⁇ -methyl styrene, ⁇ -methyl styrene or p-tert-butyl-styrene.
  • the monomers of the controlled polymer prepared according to a first step a1) or a2) contain aminic or acid groups, is than modified in a second step by a transesterification reaction, an amidation, hydrolysis or anhydride modification and thereafter the aminic or acid groups of the modified controlled polymer are converted to salt structures by reaction with a salt forming component.
  • Typical salt forming components for amino groups are for example organic or inorganic acids or alkylhalogenides, especially such salt forming components, which are based on organic cyclic acids or cyclic alkylhalogenides.
  • Typical examples of such salt forming components are described in EP 1275689 (Ciba) and WO 03/046029 (Ciba)
  • Typical salt forming components for acid groups on the modified controlled polymer are inorganic bases, such as NaOH, KOH, NH4OH or volatile aminoalcohols, such as 2-di-methylaminoethanol or 2-amino-2-methylpropanol (AMP), which are frequently used in coatings.
  • inorganic bases such as NaOH, KOH, NH4OH or volatile aminoalcohols, such as 2-di-methylaminoethanol or 2-amino-2-methylpropanol (AMP), which are frequently used in coatings.
  • the polymer or copolymer shows a good solubility at low temperatures and a decreasing solubility at high temperatures. This effect is for example described by Hammouda, B.; Ho, D.; Kline, S in Macromolecules (2002), 35(22), 8578-8585).
  • the process is carried out such, that the resulting polymer shows a lower critical solution temperature in water or water rich solvent mixtures.
  • modified polymers with an LCST temperature range at 20% polymer by weight based on the water or water mixture between 25° C. and 80° C.
  • Polymeric pigment dispersants are an essential part, particularly of new waterbased formulation technology.
  • the controlled free radical polymerisation (CFRP) is a tool to tailor the microstructure of polymers (e.g. block-copolymers) in a way that is favorable for the dispersion and stabilization of pigments in the millbase.
  • CFRP controlled free radical polymerisation
  • the combination of CFRP with subsequent postmodification of the stabilizing block allows enlarging the possible groups that can be used in pigment dispersants.
  • Another aspect of the invention is a polymer or copolymer obtainable in a process as described above. (Claim 16 ). As outlined on page 2 of the description the process according to claim 1 provides polymers with distinct structural differences compared to polymers with same monomer composition, but synthesized directly from corresponding monomers without post-transesterification.
  • a further aspect of the invention is a pigment concentrate comprising
  • Pigments may be organic or inorganic and are, for example, from the 1-aminoanthraquinone, anthanthrone, anthrapyrimidine, azo, azomethine, quinacridone, quinacridonequinone, quinophthalone, dioxazine, diketopyrrolopyrrole, flavanthrone, indanthrone, isoindoline, isoindolinone, isoviolanthrone, perinone, perylene, phthalocyanine, pyranthrone or thioindigo series, including those, where applicable, in the form of metal complexes or lakes.
  • Azos may be, for example, mono- or dis-azo pigments from any known sub-class, obtainable, for example, by coupling, condensation or lake formation.
  • organic pigments include Colour Index Pigment Yellow 3, 12, 13, 14, 17, 24, 34, 42, 53, 62, 74, 83, 93, 95, 108, 109, 110, 111, 119, 123, 128, 129, 139, 147, 150, 164, 168, 173, 174, 184, 188, 191, 191:1, 193, 199, Pigment Orange 5, 13, 16, 34, 40, 43, 48, 49, 51, 61, 64, 71, 73, Pigment Red 2, 4, 5, 23, 48:1, 48:2, 48:3, 48:4, 52:2, 53:1, 57, 57:1, 88, 89, 101, 104, 112, 122, 144, 146, 149, 166, 168, 177, 178, 179, 181, 184, 190, 192, 194, 202, 204, 206, 207, 209, 214, 216, 220, 221, 222, 224, 226, 254, 255, 262,
  • phthalocyanine pigments Preference is given to phthalocyanine pigments, azobenzimidazolone, disazo and polycyclic pigments and also to isoindolinones, perylenes carbon black and diketopyrrolopyrroles.
  • the pigment being a quinacridone, dioxazine, perylene, diketopyrrolopyrrole or disazo condensation pigment.
  • Quinacridones are preferably prepared by oxidation of dihydroquinacridones using hydrogen peroxide, as described, for example, in U.S. Pat. No. 5,840,901 or WO-02/077104.
  • the pigments may be single chemical compounds or mixtures of a plurality of components, including solid solutions or mixed crystals containing a plurality of chemical compounds. Preference is given to uniformly crystalline pigments as they usually yield greater color saturation than physical mixtures and mixed phases. If duller shades are nevertheless desired in the final application, this may be achieved by toning down with colorants of different color in a manner known per se.
  • the pigment concentrate may contain additional solvents, in particular water.
  • composition comprising
  • thermoplastic a thermoplastic, a chemically or structurally crosslinked polymer and b) a polymer or copolymer prepared according to the process of claim 1 or 4 .
  • component a) is a film forming binder material.
  • component a) is a film forming binder material.
  • laim 20 is a film forming binder material.
  • the above composition contains in addition an organic or inorganic pigment or mixtures thereof. (Claim 21 )
  • Film forming physically drying binder resins are typically derived from ⁇ , ⁇ -unsaturated acids and derivatives thereof such as polyacrylates and polymethacrylates; polymethyl methacrylates, polyacrylamides and polyacrylonitriles. Examples are thermoplastic polyacrylates (TPA).
  • TPA thermoplastic polyacrylates
  • Another class is for example derived from natural polymers such as cellulose acetate or butyrate. Also suitable are physically drying alkyd resins or nitrocellulose lacquers.
  • Thermally cross linking film forming binder resins are for example those given below.
  • These resins are typically crosslinked with melamine resins or (poly)isocyanate resins and known as thermosetting acrylics.
  • cross linking alkyd resins which can be used as film forming binder resins in the present invention are the conventional stoving lacquers which are used in particular for coating automobiles (automobile finishing lacquers), for example lacquers based on alkyd/melamine resins and alkyd/acrylic/melamine resins (see H. Wagner and H. F. Sarx, “Lackkunstharze” (1977), pages 99-123).
  • Other crosslinking agents include glycouril resins, blocked isocyanates or epoxy resins.
  • the coating compositions may be applied on wood, metal or plastic substrates.
  • the instant coating compositions are particularly suitable both for metal finish coatings and solid shade finishes of automobiles, especially in the case of retouching finishes, as well as various coil coating applications.
  • the coating compositions in accordance with the invention are preferably applied in the conventional manner by two methods, either by the single-coat method or by the two-coat method. In the latter method, a pigment-containing base coat is applied first and then a covering coat of clear lacquer over it.
  • Powder coating composition can be prepared by reacting glycidyl methacrylate with selected alcohol components.
  • Powder coating is a known technology and is described, for example, in “Ullmann's Encyclopedia of Industrial Chemistry, Fifth, Completely Revised Edition, Volume A 18”, pages 438 to 444 (1991).
  • a powder is generally fluidized with supply of air, electrostatically charged and applied to an earthed, preferably metallic substrate.
  • the substrate is subsequently heated, in the course of which the adhering powder melts, coalesces and forms a coherent film on the metal surface. Since powder coating requires no solvent, this technology is especially friendly to the environment.
  • thermoplastic or stovable, crosslinkable polymers which are applied in powder form to predominantly metallic substrates.
  • the manner in which the powder is brought into contact with the workpiece to be coated characterizes the various application techniques, for example electrostatic powder spraying with corona or triboelectric pistols, electrostatic fluidized-bed sintering or by using magnetic brush technology.
  • organic film-forming binders for powder coatings are stoving systems based on, for example, epoxy resins, polyester-hydroxyalkylamides, polyester-glycolurils, epoxypolyester resins, polyester-triglycidyl isocyanurates, hydroxy-functional polyester-blocked polyisocyanates, hydroxy-functional polyester-uretdiones, acrylate resins with hardener or mixtures of such resins.
  • film-forming binders having thermoplastic properties for example polyethylene, polypropylene, polyamides, polyvinyl chlorides, polyvinylidene dichloride or polyvinylidene difluoride.
  • inventive compositions containing the modified controlled polymers as dispersants or rheology modifiers also comprise coating related applications outside paints, like for example printing inks, ink jet inks, liquid colorants for plastics, casting resins, gel coats, filled unsaturated polyester resins like SMC or BMC (sheet molding compounds, bulk molding compounds) or gel coats and also comprise compositions for electronic applications like pigment dispersions for color filters.
  • coating related applications outside paints like for example printing inks, ink jet inks, liquid colorants for plastics, casting resins, gel coats, filled unsaturated polyester resins like SMC or BMC (sheet molding compounds, bulk molding compounds) or gel coats and also comprise compositions for electronic applications like pigment dispersions for color filters.
  • thermoplastic or structurally crosslinked polymers wherein the instant dispersants or rheology modifiers, for example, together with pigments are useful are given below.
  • Polymers of monoolefins and diolefins for example polypropylene, polyisobutylene, polybut-1-ene, poly-4-methylpent-1-ene, polyvinylcyclohexane, polyisoprene or polybutadiene, as well as polymers of cycloolefins, for instance of cyclopentene or norbornene, polyethylene (which optionally can be crosslinked), for example high density polyethylene (HDPE), high density and high molecular weight polyethylene (HDPE-HMW), high density and ultrahigh molecular weight polyethylene (HDPE-UHMW), medium density polyethylene (MDPE), low density polyethylene (LDPE), linear low density polyethylene (LLDPE), (VLDPE) and (ULDPE).
  • Polyolefins i.e. the polymers of monoolefins exemplified in the preceding paragraph, preferably polyethylene and polypropylene, can be prepared by different, and especially by the following, methods:
  • Homopolymers and copolymers from 1.)-4.) may have any stereostructure including syndiotactic, isotactic, hemi-isotactic or atactic; where atactic polymers are preferred. Stereoblock polymers are also included.
  • Homopolymers and copolymers may have any stereostructure including syndiotactic, isotactic, hemi-isotactic or atactic; where atactic polymers are preferred. Stepreoblock polymers are also included. 6a.
  • Copolymers including aforementioned vinyl aromatic monomers and comonomers selected from ethylene, propylene, dienes, nitriles, acids, maleic anhydrides, maleimides, vinyl acetate and vinyl chloride or acrylic derivatives and mixtures thereof, for example styrene/butadiene, styrene/acrylonitrile, styrene/ethylene (interpolymers), styrene/alkyl methacrylate, styrene/butadiene/alkyl acrylate, styrene/butadiene/alkyl methacrylate, styrene/maleic anhydride, styrene/acrylonitrile/methyl acrylate; mixtures of high impact strength of styrene copolymers and another polymer, for example a polyacrylate, a diene polymer or an ethylene/propylene/diene terpolymer; and block copolymers of sty
  • 6b Hydrogenated aromatic polymers derived from hydrogenation of polymers mentioned under 6.), especially including polycyclohexylethylene (PCHE) prepared by hydrogenating atactic polystyrene, often referred to as polyvinylcyclohexane (PVCH).
  • PCHE polycyclohexylethylene
  • PVCH polyvinylcyclohexane
  • 6c Hydrogenated aromatic polymers derived from hydrogenation of polymers mentioned under 6a.).
  • Homopolymers and copolymers may have any stereostructure including syndiotactic, isotactic, hemi-isotactic or atactic; where atactic polymers are preferred. Stereoblock polymers are also included.
  • Graft copolymers of vinyl aromatic monomers such as styrene or ⁇ -methylstyrene, for example styrene on polybutadiene, styrene on polybutadiene-styrene or polybutadiene-acrylonitrile copolymers; styrene and acrylonitrile (or methacrylonitrile) on polybutadiene; styrene, acrylonitrile and methyl methacrylate on polybutadiene; styrene and maleic anhydride on polybutadiene; styrene, acrylonitrile and maleic anhydride or maleimide on polybutadiene; styrene and maleimide on polybutadiene; styrene and alkyl acrylates or methacrylates on polybutadiene; styrene and acrylonitrile on ethylene/propylene/diene terpolymers; st
  • Halogen-containing polymers such as polychloroprene, chlorinated rubbers, chlorinated and brominated copolymer of isobutylene-isoprene (halobutyl rubber), chlorinated or sulfochlorinated polyethylene, copolymers of ethylene and chlorinated ethylene, epichlorohydrin homo- and copolymers, especially polymers of halogen-containing vinyl compounds, for example polyvinyl chloride, polyvinylidene chloride, polyvinyl fluoride, polyvinylidene fluoride, as well as copolymers thereof such as vinyl chloride/vinylidene chloride, vinyl chloride/vinyl acetate or vinylidene chloride/vinyl acetate copolymers.
  • halogen-containing polymers such as polychloroprene, chlorinated rubbers, chlorinated and brominated copolymer of isobutylene-isoprene (halobutyl rubber), chlorinated
  • Polymers derived from ⁇ , ⁇ -unsaturated acids and derivatives thereof such as polyacrylates and polymethacrylates; polymethyl methacrylates, polyacrylamides and polyacrylonitriles, impact-modified with butyl acrylate.
  • Copolymers of the monomers mentioned under 9) with each other or with other unsaturated monomers for example acrylonitrile/butadiene copolymers, acrylonitrile/alkyl acrylate copolymers, acrylonitrile/alkoxyalkyl acrylate or acrylonitrile/vinyl halide copolymers or acrylonitrile/alkyl methacrylate/butadiene terpolymers.
  • acrylonitrile/butadiene copolymers for example acrylonitrile/butadiene copolymers, acrylonitrile/alkyl acrylate copolymers, acrylonitrile/alkoxyalkyl acrylate or acrylonitrile/vinyl
  • Homopolymers and copolymers of cyclic ethers such as polyalkylene glycols, polyethylene oxide, polypropylene oxide or copolymers thereof with bisglycidyl ethers.
  • Polyacetals such as polyoxymethylene and those polyoxymethylenes which contain ethylene oxide as a comonomer; polyacetals modified with thermoplastic polyurethanes, acrylates or MBS. 14. Polyphenylene oxides and sulfides, and mixtures of polyphenylene oxides with styrene polymers or polyamides. 15. Polyurethanes derived from hydroxyl-terminated polyethers, polyesters or polybutadienes on the one hand and aliphatic or aromatic polyisocyanates on the other, as well as precursors thereof. 16.
  • Polyamides and copolyamides derived from diamines and dicarboxylic acids and/or from aminocarboxylic acids or the corresponding lactams for example polyamide 4, polyamide 6, polyamide 6/6, 6/10, 6/9, 6/12, 4/6, 12/12, polyamide 11, polyamide 12, aromatic polyamides starting from m-xylene diamine and adipic acid; polyamides prepared from hexamethylenediamine and isophthalic or/and terephthalic acid and with or without an elastomer as modifier, for example poly-2,4,4-trimethylhexamethylene terephthalamide or poly-m-phenylene isophthalamide; and also block copolymers of the aforementioned polyamides with polyolefins, olefin copolymers, ionomers or chemically bonded or grafted elastomers; or with polyethers, e.g.
  • polyethylene glycol polypropylene glycol or polytetramethylene glycol
  • polyamides or copolyamides modified with EPDM or ABS polyamides condensed during processing (RIM polyamide systems).
  • Polyesters derived from dicarboxylic acids and diols and/or from hydroxycarboxylic acids or the corresponding lactones for example polyethylene terephthalate, polybutylene terephthalate, poly-1,4-dimethylolcyclohexane terephthalate, polyalkylene naphthalate (PAN) and polyhydroxybenzoates, as well as block copolyether esters derived from hydroxyl-terminated polyethers; and also polyesters modified with polycarbonates or MBS. 19. Polycarbonates and polyester carbonates.
  • Monomers butylacrylate (BA), hydroxyethylacrylate (HEA), hydroxypropylacrylate (HPA) 4-vinyl-pyridine (4-VP).
  • Modification agents cyclohexylacid anhydride (CHAA), succinic acid anhydride (SAA), methoxy-poly-ethyleneglycole (MPEG 550-OH), HCl, NaOH.
  • Solvents methoxypropylacetate (MPA), Xylene, methoxypropanol (MP), polystyrene (PS), tetrahydrofurane (THF), polyethyleneoxide (POE/PEG).
  • initiator is 2-bromoethylpropionate (MBP)
  • the catalyst is CuBr/CuBr 2
  • the ligand is N,N,N′,N′′,N′′-pentamethyldiethyltriamine (PMDETA).
  • NOR Initiator/regulator is compound O1
  • n-Butylacrylate (n-BA, 128.17 g/mol), 8.55 g compound O1 (317.48 g/mol) and 122.139 of MPA were added, three times degassed with N 2 /vacuum and polymerized at 135° C. under N 2 until a conversion of around 8 mol % is reached. 338.89 g of n-BA is slowly added to the reaction with the dropping funnel and polymerized at 135° C. under N 2 until a conversion of around 48 mol %. Residual monomers and solvents were distilled of at 80° C. and 12 mbar.
  • the degree of polymerization is 75.
  • LCST lower critical solution temperature
  • a 35 wt % solution of the endproduct polymer in water is a clear solution at room temperature, but becomes turbid at elevated temperatures above 70° C.
  • the resulting polymer also formed clear 10 wt % solutions in following organic solvents: butyl acetate, methoxypropylacetate, methoxypropanol, butylglycol and xylene.
  • the 50 wt % solids solution in water displays an LCST of 67° C.
  • the polymer A6 gives clear solutions 10 wt % in following organic solvents: butyl acetate, methoxypropylacetate, methoxypropanol, butylglycol and xylene.
  • organic solvents butyl acetate, methoxypropylacetate, methoxypropanol, butylglycol and xylene.
  • pigment dispersant part of the polymer A6 was dissolved in water to give a clear 50 wt % solids solution, other parts of the polymer were dissolved in various other organic solvents.
  • the 50 wt % solids solution in water displays an LCST of 70° C.
  • the MPA was distilled under reduced pressure before adding 0.28 g catalyst solution (Ti(AcAc)2(iOPr)2 Titan-bis-acetylacetonato-bis-isopropylate, 75 wt % in isopropanol).
  • 0.28 g catalyst solution Ti(AcAc)2(iOPr)2 Titan-bis-acetylacetonato-bis-isopropylate, 75 wt % in isopropanol.
  • the transesterification was started by slowly distilling off n-Butanol under reduced pressure and increasing the temperature to 145° C. Two additional portions each of 0.28 g catalyst solution were added after 1 h and 2 h later. After 4 h total reaction time the transesterification was terminated after no further n-butanol formation was observed.
  • the resultant very high viscous block copolymer was diluted with MPA to a clear 60 wt % solution.
  • the transesterification was started by slowly distilling off n-Butanol under reduced pressure and increasing the temperature to 145° C. Two additional portions each of 0.15 g catalyst solution were added after 2 h and 4 h later. After 6 h total reaction time the reaction was terminated after no further n-butanol formation was observed.
  • the resultant high viscous block copolymer was diluted with MPA to a clear 60 wt % solution.
  • the transesterification was started by slowly distilling off n-Butanol under reduced pressure and increasing the temperature to 145° C. Two additional portions each of 0.15 g catalyst solution were added after 2 h and 4 h later. After 6 h total reaction time the reaction was terminated after no further n-butanol formation was observed.
  • the transesterification was started by slowly distilling off n-Butanol under reduced pressure and increasing the temperature to 145° C. Two additional portions each of 0.15 g catalyst solution were added after 2 h and 4 h later. After 6 h total reaction time the reaction was terminated after no further n-butanol formation was observed.
  • the transesterification was started by slowly distilling off n-Butanol under reduced pressure and increasing the temperature to 145° C. Two additional portions each of 0.43 g catalyst solution were added after 2 h and 4 h later. After 6 h total reaction time the reaction was terminated after no-further n-butanol formation was observed.
  • Resin free organic pigment concentrate based on the inventive pigment dispersants and Irgalite Blue PG were prepared according to the following Table 1.
  • the organic pigment concentrates from Table 1 are ground for 3 hours with glass beads (2 mm/mb) in a Scandex shaking equipment.
  • the pigment concentrates based on Irgalite Blue PG are then let down to full tone paints by mixing for 12 h on a roll mill according to the following table.
  • Viscosity of pigment concentrate and full tone transparency of dry full tone and gloss at 20° after letdown is measured.
  • the powder coating composition is based on a carboxy-functional polyester, components 1 to 6 (formulation containing the levelling agent) as indicated in Table 1.
  • the components are mixed using a planetary stirrer.
  • the mixture is then extruded on a prism extruder at 300 revolutions/minute at 110° C. and is rolled out.
  • the powder coating composition is coarsely comminuted using a bench cutter and is ground in a Retsch ZM-1 ultracentrifugal mill with a 0.75 mm annular-perforation screen at 15,000 revolutions/minute.
  • the powder is passed through a 125 ⁇ m sieve on a centrifugal sieving machine having an average particle size of from 30 to 50 ⁇ m.
  • the finished powder coating composition is sprayed electrostatically to a coat thickness of 70 to 80 ⁇ m onto aluminium panels using an ESB-Wagner corona cup gun at 60 kV.
  • the coated panels are cured in an electric oven at 200° C. for 10 minutes.
  • Levelling agent 7.0 f 3.5 g) Total: 1000 1010 a) Almatex ® PD7610 from Anderson, USA b) Dodecanedioic acid from DuPont, Germany c) Tinuvin ® 144 from Ciba Specialty Chemicals, Basel, Switzerland d) Tinuvin ® 405 from Ciba Specialty Chemicals, Basel, Switzerland e) Benzoin f) Additol ® XL 490 from UCB Surface Specialties, USA g) A17
  • inventive block copolymer A17 shows comparable performance at lower dosage compared to a commercial benchmark levelling agent.
  • inventive block copolymer A17 has a solid 100% active product form, which is more convenient in handling and what offers significant advantages in production of powder paints.
  • Usual commercial polyacrylate levelling agents are either liquid or sticky resins or are adsorbed on solid silica carrier.
  • polyacrylate pigment dispersants are not fully soluble in non-polar solvents like pure aliphatic hydrocarbons.
  • the solubility of the inventive copolymers was tested in an aliphatic hydrocarbon solvent Shell Catenex 925, which serves as a model for extreme non-polar formulations.
  • inventive copolymers A11, A13 and A15 showed full solubility. This is in contrast to typical commercial polyacrylate dispersants like Efka-4401, which was tested in comparison and formed turbid inhomogeneous mixture.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Medicinal Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Polymers & Plastics (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Wood Science & Technology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Graft Or Block Polymers (AREA)
  • Polymerization Catalysts (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Pigments, Carbon Blacks, Or Wood Stains (AREA)
  • Paints Or Removers (AREA)
US11/794,707 2005-01-11 2006-01-02 Process for the Post-Modification of Homo and Copolymers Prepared by Controlled Free Radical Polymerization Processes Abandoned US20090221739A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP05100102.2 2005-01-11
EP05100102 2005-01-11
PCT/EP2006/050000 WO2006074969A1 (en) 2005-01-11 2006-01-02 Process for the post-modification of homo and copolymers prepared by controlled free radical polymerization processes

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP2006/050000 A-371-Of-International WO2006074969A1 (en) 2005-01-11 2006-01-02 Process for the post-modification of homo and copolymers prepared by controlled free radical polymerization processes

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US13/112,280 Continuation US20110224375A1 (en) 2005-01-11 2011-05-20 Process for the post-modification of homo and copolymers prepared by controlled free radical polymerization processes

Publications (1)

Publication Number Publication Date
US20090221739A1 true US20090221739A1 (en) 2009-09-03

Family

ID=34938499

Family Applications (3)

Application Number Title Priority Date Filing Date
US11/794,707 Abandoned US20090221739A1 (en) 2005-01-11 2006-01-02 Process for the Post-Modification of Homo and Copolymers Prepared by Controlled Free Radical Polymerization Processes
US13/112,280 Abandoned US20110224375A1 (en) 2005-01-11 2011-05-20 Process for the post-modification of homo and copolymers prepared by controlled free radical polymerization processes
US13/660,260 Active US8658741B2 (en) 2005-01-11 2012-10-25 Process for the post-modification of homo and copolymers prepared by controlled free radical polymerization processes

Family Applications After (2)

Application Number Title Priority Date Filing Date
US13/112,280 Abandoned US20110224375A1 (en) 2005-01-11 2011-05-20 Process for the post-modification of homo and copolymers prepared by controlled free radical polymerization processes
US13/660,260 Active US8658741B2 (en) 2005-01-11 2012-10-25 Process for the post-modification of homo and copolymers prepared by controlled free radical polymerization processes

Country Status (8)

Country Link
US (3) US20090221739A1 (enExample)
EP (1) EP1861429B1 (enExample)
JP (1) JP5225689B2 (enExample)
KR (1) KR101322668B1 (enExample)
CN (1) CN100577692C (enExample)
BR (1) BRPI0606305A2 (enExample)
RU (1) RU2401281C2 (enExample)
WO (1) WO2006074969A1 (enExample)

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20100010103A1 (en) * 2006-12-20 2010-01-14 Schmidt Scott C Polymer encapsulation and/or binding
US20100116010A1 (en) * 2007-05-10 2010-05-13 Clariant International Ltd Aqueous pigment preparations
US20110107803A1 (en) * 2007-08-23 2011-05-12 Clariant Finance (Bvi) Limited Aqueous Pigment Preparations Comprising Anionic Additives Based on Allyl Ether and Vinyl Ether
US20110118384A1 (en) * 2008-05-09 2011-05-19 Basf Se Pearlescent pigments coated with a metal oxide/hydroxide layer and an acrylic copolymer
US20110144260A1 (en) * 2008-06-23 2011-06-16 Basf Se Pigment dispersants with modified copolymers
US20110184097A1 (en) * 2008-08-16 2011-07-28 Clariant Finance (Bvi) Limited Dry Pigment Preparations Comprising Anionic Additives
US20110185781A1 (en) * 2007-08-23 2011-08-04 Clariant Finance (Bvi) Limited Aqueous Pigment Preparations Having Nonionic Additives on the Basis of Alyl and Vinyl Ether
US20120172498A1 (en) * 2009-01-19 2012-07-05 Basf Se Black pigment dispersion
US8221537B2 (en) * 2007-05-10 2012-07-17 Clariant Finance (Bvi) Limited Water-based pigment preparations
US20140298591A1 (en) * 2011-10-25 2014-10-09 Basf Se Use of comb or block copolymers as soil antiredeposition agents and soil release agents in laundry processes
US20150017511A1 (en) * 2011-12-20 2015-01-15 Treofan Germany Gmbh & Co. Kg Highly porous separator film having a coating and a disconnecting function
US20150280195A1 (en) * 2011-12-08 2015-10-01 Treofan Germany Gmbh & Co.Kg Highly-porous separator film with a coating
US9164407B2 (en) 2013-05-14 2015-10-20 Konica Minolta, Inc. Electrostatic latent image developer
US9309391B2 (en) 2010-06-29 2016-04-12 Basf Se Process for improving the flow of properties of polymer melts
US9707524B2 (en) 2008-10-28 2017-07-18 Arkema Inc. Water flux polymer membranes
US20230192962A1 (en) * 2020-04-14 2023-06-22 Basf Se An amine-modified polymer, a controlled free radical polymerization for preparing the same and implementations thereof

Families Citing this family (37)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2038701B1 (en) 2006-07-06 2017-04-12 Basf Se Encapsulated dispersions comprising electrophoretically mobile organic colorants
JP5425623B2 (ja) * 2006-07-11 2014-02-26 チバ ホールディング インコーポレーテッド カラーフィルター組成物
MX2010002217A (es) 2007-09-07 2010-03-17 Basf Se Dispersiones encapculadas que contienen colorantes organicos que pueden moverse por medios electroforeticos.
EP2235146B1 (en) 2007-12-18 2016-04-20 Basf Se Biodiesel cold flow improver
KR101560854B1 (ko) * 2008-02-22 2015-10-15 바스프 에스이 플루오로 레벨링제
CN102482383B (zh) * 2009-07-01 2014-07-30 株式会社普利司通 通过自由基引发聚合制备羟芳基-官能化共聚体的方法
US9051478B2 (en) 2010-07-22 2015-06-09 Basf Se Additive combination for sealants applications
CN102199261B (zh) * 2011-04-13 2012-09-19 山东交通学院 聚乙二醇-b-聚苯乙烯-b-聚全氟己基乙基丙烯酸酯及其制备方法
WO2013124830A1 (en) 2012-02-24 2013-08-29 Basf Se Novel polymer dispersants
JP5835054B2 (ja) * 2012-03-28 2015-12-24 日本ゼオン株式会社 静電荷像現像用カラートナーの製造方法
EP2978786A1 (en) * 2013-03-27 2016-02-03 Basf Se Block copolymers as soil release agents in laundry processes
CN105283489B (zh) 2013-06-07 2019-02-12 巴斯夫欧洲公司 聚合物分散剂
JP2016530362A (ja) 2013-07-22 2016-09-29 ビーエーエスエフ ソシエタス・ヨーロピアBasf Se 新規ポリマー及びそれらの分散剤としての使用
FR3040171B1 (fr) * 2015-08-17 2017-08-25 Ecole Superieure Physique & Chimie Ind Ville De Paris Composition comprenant un reseau de polymeres reticules, prepare par copolymerisation radicalaire, comprenant des liaisons pendantes et des points de reticulation echangeables par reaction d'echange aldehyde-imine et/ou par reaction d'echange imine-imine, procede de preparation et utilisation
CN107922749B (zh) 2015-08-20 2020-09-04 巴斯夫欧洲公司 用于销售点使用的通用颜料制剂
ES2886849T3 (es) 2017-04-21 2021-12-21 Basf Colors & Effects Gmbh Procedimiento para preparar una dispersión acuosa de partículas que contienen pigmentos
US11130879B2 (en) * 2017-12-28 2021-09-28 Axalta Coating Systems Ip Co., Llc Dispersants, coating compositions including dispersants, and methods of forming the same
CN108417836B (zh) * 2018-01-31 2021-05-04 闽南师范大学 一种锂离子电池的电极粘结剂及其制备方法
CN112384581A (zh) * 2018-06-11 2021-02-19 宣伟投资管理有限公司 包含水分散性丙烯酸类嵌段共聚物的包装涂层
CN108727892A (zh) * 2018-06-15 2018-11-02 鲁东大学 一种纤维素基流平剂的制备方法
US12024595B2 (en) 2018-08-16 2024-07-02 Basf Se Polymer composition
JP7399161B2 (ja) 2018-10-18 2023-12-15 ベーアーエスエフ・エスエー 有機ir吸収顔料を含むマイクロ粒子組成物
JP6829286B2 (ja) * 2019-03-22 2021-02-10 大日精化工業株式会社 水性顔料分散液
EP3965983A1 (en) 2019-05-06 2022-03-16 Basf Se Compositions, comprising silver nanoplatelets
CA3180245A1 (en) 2020-04-23 2021-10-28 Sicpa Holding Sa Process for producing dichroic security features for securing value documents
WO2021213942A1 (en) 2020-04-23 2021-10-28 Basf Se Compositions, comprising platelet-shaped transition metal particles
KR102353641B1 (ko) * 2020-10-14 2022-01-21 한국화학연구원 불소계 고분자의 제조 방법, 불소계 고분자, 및 이를 포함하는 고분자막
JP7625243B2 (ja) * 2020-10-16 2025-02-03 山陽色素株式会社 黒色顔料分散体
CA3197947A1 (en) 2020-11-10 2022-05-19 Nikolay A. Grigorenko Compositions, comprising silver nanoplatelets
TWI883290B (zh) 2020-11-10 2025-05-11 瑞士商西克帕控股有限公司 用於製造二色性保密特徵的uv-vis輻射可固化保密墨水
TWI884334B (zh) * 2020-11-10 2025-05-21 瑞士商西克帕控股有限公司 用於製造二色性保密特徵的uv-vis輻射可固化保密墨水
WO2022167377A1 (en) 2021-02-03 2022-08-11 Basf Se Compositions, comprising silver nanoplatelets
CN117062872A (zh) 2021-03-26 2023-11-14 巴斯夫欧洲公司 作为分散剂的包含聚丙烯酸系嵌段共聚物和芳族基聚氧化烯的聚合物组合物
CN117321151A (zh) 2021-05-12 2023-12-29 巴斯夫欧洲公司 包含片状过渡金属颗粒的组合物
WO2023072740A1 (en) 2021-10-26 2023-05-04 Basf Se A method for producing interference elements
WO2023088805A1 (en) 2021-11-18 2023-05-25 Sicpa Holding Sa Methods for producing overt security features exhibiting one or more indicia
WO2024231339A1 (en) 2023-05-11 2024-11-14 Byk-Chemie Gmbh Process for preparing block copolymer

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4972037A (en) * 1989-08-07 1990-11-20 Minnesota Mining And Manufacturing Company Polysiloxane-grafted copolymer topical binder composition with novel fluorochemical comonomer and method of coating therewith
US5744523A (en) * 1992-10-28 1998-04-28 Th. Goldschmidt Ag Use of polyacrylate esters as dispersants
US20030105201A1 (en) * 2001-05-21 2003-06-05 Clemens Auschra Pigment compositions with modified block copolymer dispersants
US20040143035A1 (en) * 2002-08-07 2004-07-22 Bernd Goebelt Use of gradient copolymers as dispersants to treat pigments and other solids

Family Cites Families (39)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2474310A1 (fr) * 1980-01-25 1981-07-31 Oreal Solution stable a l'oxydation de vitamine f et d'huile de jojoba et compositions cosmetiques la contenant
KR930000892B1 (ko) 1983-07-11 1993-02-11 커몬웰스 사이언티픽 앤드 인더스트리얼 리셔치 오가니제이숀 신규의 개시제를 사용하여 중합체 또는 공중합체를 제조하는방법
DE3906702A1 (de) * 1989-03-03 1990-09-13 Goldschmidt Ag Th Polyacrylsaeureester mit langkettigen kohlenwasserstoff- und polyoxyalkylengruppen und deren verwendung als grenzflaechenaktive substanzen
DE4308773C2 (de) 1992-07-24 1996-05-09 Goldschmidt Ag Th Umgeesterte Polyacrylsäureester mit Ammonium- und Polyoxyalkylen-Gruppen und ihre Verwendung in Trennmitteln
US5322912A (en) 1992-11-16 1994-06-21 Xerox Corporation Polymerization processes and toner compositions therefrom
FR2730240A1 (fr) 1995-02-07 1996-08-09 Atochem Elf Sa Stabilisation d'un polymere par un radical libre stable
US5763548A (en) 1995-03-31 1998-06-09 Carnegie-Mellon University (Co)polymers and a novel polymerization process based on atom (or group) transfer radical polymerization
ATE210684T1 (de) 1996-07-10 2001-12-15 Du Pont POLYMERISATION MIT ßLIVINGß KENNZEICHEN
AU4773997A (en) 1996-09-25 1998-04-17 Akzo Nobel N.V. No-compounds for pseudo-living radical polymerization
US6281311B1 (en) * 1997-03-31 2001-08-28 Pmd Holdings Corp. Controlled free radical polymerization process
FR2764892B1 (fr) 1997-06-23 2000-03-03 Rhodia Chimie Sa Procede de synthese de polymeres a blocs
AU8440798A (en) 1997-07-15 1999-02-10 Ciba Specialty Chemicals Holding Inc. Polymerizable compositions containing alkoxyamine compounds derived from nitroso- or nitrone compounds
DE69840423D1 (de) 1997-07-21 2009-02-12 Commw Scient Ind Res Org Synthese von dithioester-kettentransferagentien
BR9815179A (pt) 1997-12-18 2000-10-10 Du Pont Processo para produzir um polìmero, polìmero, composição de revestimento e agente de transferência de cadeia.
AU1883199A (en) 1997-12-31 1999-07-26 Rhodia Chimie Method for block polymer synthesis by controlled radical polymerisation from dithiocarbamate compounds
SG82601A1 (en) 1998-03-09 2001-08-21 Ciba Sc Holding Ag 1-alkoxy-polyalkyl-piperidine derivatives and their use as polymerization regulators
TWI246519B (en) 1998-06-25 2006-01-01 Ciba Sc Holding Ag Use of 2,2,6,6 tetraalkylpiperidine-N-oxyl radicals having long alkyl chains as polymerization regulators
CA2337482A1 (en) 1998-07-31 2000-02-17 Ciba Specialty Chemicals Holding Inc. Open chain alkoxyamine compounds and their use as polymerization regulators
JP2000072718A (ja) * 1998-09-01 2000-03-07 Mitsubishi Rayon Co Ltd (メタ)アクリル酸ピペリジン−1−オキシルエステル誘導体からなる(メタ)アクリル酸エステル用重合防止剤およびその製造方法
TWI225483B (en) 1998-10-16 2004-12-21 Ciba Sc Holding Ag Heterocyclic alkoxyamines as regulators in controlled radical polymerization process
US6573347B1 (en) 1998-12-21 2003-06-03 Ciba Specialty Chemicals Corporation Composition and process for controlled radical polymerization using multifunctional initiator/regulator compounds
AU753012B2 (en) * 1998-12-31 2002-10-03 Ciba Specialty Chemicals Holding Inc. Pigment composition containing ATRP polymers
FR2794463B1 (fr) 1999-06-04 2005-02-25 Rhodia Chimie Sa Procede de synthese de polymeres par polymerisation radicalaire controlee a l'aide de xanthates halogenes
JP4829447B2 (ja) 1999-07-02 2011-12-07 チバ ホールディング インコーポレーテッド 官能化されたマクロマーの製造のための1および多官能価アルコキシアミン
FR2802208B1 (fr) 1999-12-09 2003-02-14 Rhodia Chimie Sa Procede de synthese de polymeres par polymerisation radicalaire controlee a l'aide de xanthates
TW541303B (en) 2000-03-22 2003-07-11 Ciba Sc Holding Ag 2,2,6,6 diethyl-dimethyl-1-alkoxy-piperidine compounds and their corresponding 1-oxides
WO2002004805A1 (en) 2000-07-10 2002-01-17 Mitsubishi Heavy Industries, Ltd. Fuel injection device
US6395850B1 (en) 2000-09-28 2002-05-28 Symyx Technologies, Inc. Heterocycle containing control agents for living-type free radical polymerization
US6569969B2 (en) 2000-09-28 2003-05-27 Symyx Technologies, Inc. Control agents for living-type free radical polymerization, methods of polymerizing and polymers with same
DE10052646A1 (de) 2000-10-24 2002-05-16 Boettcher Henrik Verfahren zur Herstellung von Funktionspolymeren sowie Schichten aus Funktionspolymeren auf Festkörperoberflächen über "lebende"/kontrollierte radikalische Polymerisation
TWI236482B (en) * 2000-11-13 2005-07-21 Ciba Sc Holding Ag Process for the (co)polymerization of vinyl chloride in the presence of a stable free nitroxyl radical
CN1249035C (zh) 2001-06-13 2006-04-05 西巴特殊化学品控股有限公司 4-亚氨基-n-烷氧基或氧基-多烷基-哌啶化合物以及它们作为聚合调节剂的用途
EP1417171B1 (en) 2001-07-05 2007-11-21 Ciba SC Holding AG Multifunctional alkoxyamines based on polyalkylpiperidines, polyalkylpiperazinones and polyalkylmorpholinones and their use as polymerization regulators/initiators
CN1553922A (zh) * 2001-09-10 2004-12-08 �������⻯ѧƷ�ع����޹�˾ 通过阴离子或受控自由基聚合制备羟基乙烯基芳族聚合物或共聚物的方法
US7632916B2 (en) * 2002-08-02 2009-12-15 3M Innovative Properties Company Process to modify polymeric materials and resulting compositions
US7157283B2 (en) * 2002-08-02 2007-01-02 3M Innovative Properties Company Continuous process for the production of combinatorial libraries of modified materials
AU2003297182A1 (en) * 2002-12-18 2004-07-22 Crompton Corporation Styrenic polymer composites
JP2004306404A (ja) * 2003-04-07 2004-11-04 Ricoh Co Ltd 有機薄膜とその製造方法及び有機薄膜を用いた光記録媒体
JP4315762B2 (ja) 2003-07-31 2009-08-19 富士フイルム株式会社 記録テープカートリッジ

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4972037A (en) * 1989-08-07 1990-11-20 Minnesota Mining And Manufacturing Company Polysiloxane-grafted copolymer topical binder composition with novel fluorochemical comonomer and method of coating therewith
US5744523A (en) * 1992-10-28 1998-04-28 Th. Goldschmidt Ag Use of polyacrylate esters as dispersants
US20030105201A1 (en) * 2001-05-21 2003-06-05 Clemens Auschra Pigment compositions with modified block copolymer dispersants
US20040143035A1 (en) * 2002-08-07 2004-07-22 Bernd Goebelt Use of gradient copolymers as dispersants to treat pigments and other solids

Cited By (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8685417B2 (en) 2006-12-20 2014-04-01 Arkema, Inc. Polymer encapsulation and/or binding
US20100010103A1 (en) * 2006-12-20 2010-01-14 Schmidt Scott C Polymer encapsulation and/or binding
US20100116010A1 (en) * 2007-05-10 2010-05-13 Clariant International Ltd Aqueous pigment preparations
US7905955B2 (en) * 2007-05-10 2011-03-15 Clariant Finance (Bvi) Limited Aqueous pigment preparations
US8221537B2 (en) * 2007-05-10 2012-07-17 Clariant Finance (Bvi) Limited Water-based pigment preparations
US20110107803A1 (en) * 2007-08-23 2011-05-12 Clariant Finance (Bvi) Limited Aqueous Pigment Preparations Comprising Anionic Additives Based on Allyl Ether and Vinyl Ether
US20110185781A1 (en) * 2007-08-23 2011-08-04 Clariant Finance (Bvi) Limited Aqueous Pigment Preparations Having Nonionic Additives on the Basis of Alyl and Vinyl Ether
US8202361B2 (en) * 2007-08-23 2012-06-19 Clariant Finance (Bvi) Limited Aqueous pigment preparations comprising anionic additives based on allyl ether and vinyl ether
US8221538B2 (en) * 2007-08-23 2012-07-17 Clariant Finance (Bvi) Limited Aqueous pigment preparations having nonionic additives on the basis of alyl and vinyl ether
US8772371B2 (en) 2008-05-09 2014-07-08 Basf Se Pearlescent pigments coated with a metal oxide/hydroxide layer and an acrylic copolymer
US20110118384A1 (en) * 2008-05-09 2011-05-19 Basf Se Pearlescent pigments coated with a metal oxide/hydroxide layer and an acrylic copolymer
US20110144260A1 (en) * 2008-06-23 2011-06-16 Basf Se Pigment dispersants with modified copolymers
US8664324B2 (en) 2008-06-23 2014-03-04 Basf Se Pigment dispersants with modified copolymers
US8221539B2 (en) * 2008-08-16 2012-07-17 Clariant Finance (Bvi) Limited Dry pigment preparations comprising anionic additives
US20110184097A1 (en) * 2008-08-16 2011-07-28 Clariant Finance (Bvi) Limited Dry Pigment Preparations Comprising Anionic Additives
US9707524B2 (en) 2008-10-28 2017-07-18 Arkema Inc. Water flux polymer membranes
US8674006B2 (en) * 2009-01-19 2014-03-18 BASF SE Ludwigshafen Black pigment dispersion
US20120172498A1 (en) * 2009-01-19 2012-07-05 Basf Se Black pigment dispersion
US9309391B2 (en) 2010-06-29 2016-04-12 Basf Se Process for improving the flow of properties of polymer melts
US20140298591A1 (en) * 2011-10-25 2014-10-09 Basf Se Use of comb or block copolymers as soil antiredeposition agents and soil release agents in laundry processes
JP2014532770A (ja) * 2011-10-25 2014-12-08 ビーエーエスエフ ソシエタス・ヨーロピアBasf Se 洗濯プロセスにおける汚れ再付着防止剤および汚れ剥離剤としての櫛型コポリマーまたはブロックコポリマーの使用
US20150280195A1 (en) * 2011-12-08 2015-10-01 Treofan Germany Gmbh & Co.Kg Highly-porous separator film with a coating
US20150017511A1 (en) * 2011-12-20 2015-01-15 Treofan Germany Gmbh & Co. Kg Highly porous separator film having a coating and a disconnecting function
US9164407B2 (en) 2013-05-14 2015-10-20 Konica Minolta, Inc. Electrostatic latent image developer
US20230192962A1 (en) * 2020-04-14 2023-06-22 Basf Se An amine-modified polymer, a controlled free radical polymerization for preparing the same and implementations thereof

Also Published As

Publication number Publication date
KR101322668B1 (ko) 2013-10-30
CN100577692C (zh) 2010-01-06
RU2401281C2 (ru) 2010-10-10
EP1861429A1 (en) 2007-12-05
US20110224375A1 (en) 2011-09-15
JP5225689B2 (ja) 2013-07-03
RU2007130535A (ru) 2009-02-20
JP2008527130A (ja) 2008-07-24
US8658741B2 (en) 2014-02-25
KR20070099646A (ko) 2007-10-09
CN101103049A (zh) 2008-01-09
US20130059964A1 (en) 2013-03-07
WO2006074969A1 (en) 2006-07-20
EP1861429B1 (en) 2013-03-13
BRPI0606305A2 (pt) 2009-06-16

Similar Documents

Publication Publication Date Title
US8658741B2 (en) Process for the post-modification of homo and copolymers prepared by controlled free radical polymerization processes
EP1611197B1 (en) Light stabilising polymer dispersants in pigment dispersions
EP1155060B1 (en) Pigment composition containing atrp polymers
US6849679B2 (en) Pigment compositions with modified block copolymer dispersants
EP1465935B1 (en) Pigment compositions with modified atrp copolymer dispersants
EP2115023B1 (en) Polyamine-polyacrylate dispersant
JP5290485B2 (ja) Atrpマクロモノマーからのクシ型ポリマー
US8900779B2 (en) Color filter composition
KR20020033840A (ko) Abc-블록 중합체 분산제 함유 안료 분산물
US7678850B2 (en) Pigment dispersions containing aminated acrylic macromonomer dispersant
EP4314155B1 (en) Polymer composition comprising polyacrylic block copolymer and aromatic based polyalkyleneoxide as dispersant
US20240336779A1 (en) Dispersant polymer and composition comprising the same

Legal Events

Date Code Title Description
AS Assignment

Owner name: CIBA SPECIALTY CHEMICALS CORP., NEW YORK

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:KNISCHKA, RALF;ECKSTEIN, ERNST;AUSCHRA, CLEMENS;AND OTHERS;REEL/FRAME:022769/0048;SIGNING DATES FROM 20070515 TO 20070529

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION