WO1995017473A1 - Process for making a non-aqueous dispersion of a cooper phthalocyanine - Google Patents

Process for making a non-aqueous dispersion of a cooper phthalocyanine Download PDF

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Publication number
WO1995017473A1
WO1995017473A1 PCT/GB1994/002786 GB9402786W WO9517473A1 WO 1995017473 A1 WO1995017473 A1 WO 1995017473A1 GB 9402786 W GB9402786 W GB 9402786W WO 9517473 A1 WO9517473 A1 WO 9517473A1
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WO
WIPO (PCT)
Prior art keywords
acid
cupc
obtainable
salt
group
Prior art date
Application number
PCT/GB1994/002786
Other languages
English (en)
French (fr)
Inventor
Dean Thetford
John David Schofield
Original Assignee
Zeneca Limited
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 Zeneca Limited filed Critical Zeneca Limited
Priority to AU12776/95A priority Critical patent/AU680084B2/en
Priority to DK95903873T priority patent/DK0736070T3/da
Priority to BR9408366A priority patent/BR9408366A/pt
Priority to CA002179749A priority patent/CA2179749C/en
Priority to DE69416695T priority patent/DE69416695T2/de
Priority to US08/596,179 priority patent/US5753022A/en
Priority to JP7517268A priority patent/JPH09506922A/ja
Priority to EP95903873A priority patent/EP0736070B1/en
Publication of WO1995017473A1 publication Critical patent/WO1995017473A1/en

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09B—ORGANIC DYES OR CLOSELY-RELATED COMPOUNDS FOR PRODUCING DYES, e.g. PIGMENTS; MORDANTS; LAKES
    • C09B67/00—Influencing the physical, e.g. the dyeing or printing properties of dyestuffs without chemical reactions, e.g. by treating with solvents grinding or grinding assistants, coating of pigments or dyes; Process features in the making of dyestuff preparations; Dyestuff preparations of a special physical nature, e.g. tablets, films
    • C09B67/0001—Post-treatment of organic pigments or dyes
    • C09B67/0022—Wet grinding of pigments
    • C09B67/0023—Wet grinding of pigments of phthalocyanines
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09B—ORGANIC DYES OR CLOSELY-RELATED COMPOUNDS FOR PRODUCING DYES, e.g. PIGMENTS; MORDANTS; LAKES
    • C09B67/00—Influencing the physical, e.g. the dyeing or printing properties of dyestuffs without chemical reactions, e.g. by treating with solvents grinding or grinding assistants, coating of pigments or dyes; Process features in the making of dyestuff preparations; Dyestuff preparations of a special physical nature, e.g. tablets, films
    • C09B67/0001—Post-treatment of organic pigments or dyes
    • C09B67/0002—Grinding; Milling with solid grinding or milling assistants
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09B—ORGANIC DYES OR CLOSELY-RELATED COMPOUNDS FOR PRODUCING DYES, e.g. PIGMENTS; MORDANTS; LAKES
    • C09B67/00—Influencing the physical, e.g. the dyeing or printing properties of dyestuffs without chemical reactions, e.g. by treating with solvents grinding or grinding assistants, coating of pigments or dyes; Process features in the making of dyestuff preparations; Dyestuff preparations of a special physical nature, e.g. tablets, films
    • C09B67/0001—Post-treatment of organic pigments or dyes
    • C09B67/0014—Influencing the physical properties by treatment with a liquid, e.g. solvents
    • C09B67/0016—Influencing the physical properties by treatment with a liquid, e.g. solvents of phthalocyanines
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09B—ORGANIC DYES OR CLOSELY-RELATED COMPOUNDS FOR PRODUCING DYES, e.g. PIGMENTS; MORDANTS; LAKES
    • C09B67/00—Influencing the physical, e.g. the dyeing or printing properties of dyestuffs without chemical reactions, e.g. by treating with solvents grinding or grinding assistants, coating of pigments or dyes; Process features in the making of dyestuff preparations; Dyestuff preparations of a special physical nature, e.g. tablets, films
    • C09B67/0033—Blends of pigments; Mixtured crystals; Solid solutions
    • C09B67/0034—Mixtures of two or more pigments or dyes of the same type
    • C09B67/0035—Mixtures of phthalocyanines

Definitions

  • the present invention relates to a process for making a non- aqueous dispersion (NAD) of a copper phthalocyanine (CuPc) which is especially suitable for direct incorporation into a printing ink.
  • NAD non- aqueous dispersion
  • CuPc copper phthalocyanine
  • GB 1,373,660 discloses polyesteramine dispersants obtainable by reacting poly(hydroxycarboxylic acids)
  • PHCA poly(C 2 , 4 -alkyleneimine)
  • PAI poly(C 2 , 4 -alkyleneimine)
  • US 5,000,792 discloses polyesteramine dispersants obtainable by reacting 2 parts of PHCA with 1 part of a di-alkylenetriamine.
  • NAD containing high -concentrations of pigment often exhibit high viscosity and are difficult to handle and formulate into inks and paints. It has therefore been proposed to incorporate fluidising agents into such NAD's as disclosed in GB 1,508,576.
  • Offset inks and varnishes are presently made by first converting crude CuPc to pigmentary CuPc by salt milling in the presence of a water-miscible solvent such as ethylene glycol followed by washing with water to form a press paste which is either (1) dried and dispersed in an aliphatic medium or oil and formulated into an ink or (2) flushed into the aliphatic medium to make a "flush” colour which is then incorporated into the aliphatic medium to form the printing ink or varnish.
  • a water-miscible solvent such as ethylene glycol
  • a method of preparing a NAD of CuPc which ccmprises milling crude CuPc in a high boiling liquid at a temperature from 50 to 150°C in the presence of a) a polyesteramine or polyesterammonium salt obtainable by the reaction of an amine with a PHCA of formula (1)
  • A is divalent hydrocarbyl; Y is hydrogen or optionally substituted hydrocarbyl; n is from 1 to 100; and b) a CuPc fluidising agent.
  • the precise structure of the chain terminating group Y is not critical provided it is inert to the other coiponents of the composition under the normal processing conditions to which it is subjected. It is preferably free from ionic and strongly polar groups and preferably has a molecular weight of less than 300 and contains only C and H or C, H and O atoms.
  • the optionally substituted hydrocarbyl group Y is preferably alkyl or alkenyl containing up to 35 carbon atoms, especially from 7 to 25, and more especially from 7 to 20 carbon atoms such as heptyl, octyl, undecyl, lauryl, heptadecyl, heptadecenyl, heptadecadienyl, stearyl, oleyl, linoleyl or such a group substituted by a hydroxy, halo or alkoxy group, especially C- . - 4 alkoxy.
  • Y include, C 4 - 8 -cycloalkyl, such as cyclohexyl; polycycloalkyls, for example, polycyclic terpenyl groups which are derivable from naturally occu-rring acids such as abietic acid; aryl, such as phe ⁇ yl; aralkyl, such as benzyl and polyaryl, such as naphthyl, biphenyl, stilbenyl and phenylmethylphenyl.
  • groups are preferably unsubstituted or substituted by a group selected from hydroxy, halogen and Ci-.-alkoxy.
  • Particularly preferred terminal groups Y-CO- are 12-hydr ⁇ xystearyl and 12-hydroxyoleyl.
  • the divalent hydrocarbyl represented by A may be an aromatic, aliphatic or cycloaliphatic group. It is preferably an alkylene or alkenylene group, especially one containing from 4 to 25 carbon atoms with at least 4 carbon atoms between the oxygen atom and carbonyl group.
  • n has a value of at least two. When n is greater than one, the groups represented by A in the polyester chain [0 - A -C0] n may be the same or different. When the group A is an aliphatic chain containing nine or more carbon atoms it is preferred that n is from 1 to 10, and especially from 1 to 6.
  • n is from 1 to 60.
  • the groups represented by A may carry other substituents which do not confer water-solubility on the molecule, such as halogen and alkoxy.
  • Preferred examples of the group (-0-A-C0) are 12-oxystearyl, 12-oxyoleyl and 6-oxycaproyl.
  • the PHCA of formula I is conveniently derived from a mixture of (i) a saturated or unsaturated aliphatic hydroxycarboxylic acid containing from 4 to 25 carbon atoms having at least 4 carbon atoms between the hydroxy and carboxyl groups or a cyclic precursor thereof, such as a lactone and (ii) one or more aliphatic carboxylic acids of the formula Y-COOH, where Y is as hereinbefore defined.
  • suitable hydroxycarboxylic acids and precursors are 12-hydroxystearic acid,
  • 12-hydroxy-9-oleic acid ricinoleic acid
  • 6-hydroxycaproic acid 6-hydroxycaproic acid
  • e-caprolactone examples of suitable acids from which the end group -Y- CO- is derivable, by reaction with a terminal hydroxy group on the polyester chain, are lauric acid, palmitic acid, stearic acid and 9- oleic acid and mixtures containing these acids which are derivable from natural products.
  • Preferred PHCA's are poly(12-hydroxystearic acid), poly(ricinoleic acid) and poly(6-hydroxycaproic acid) , hereinafter PHS, PR and PHC respectively. PHS is especially preferred.
  • the amine which reacts with the PHCA contains at least one group which is reactable with a carboxylic acid group of the PHCA, and is preferably a hydroxy and especially an amino group which may be either primary or secondary amino.
  • the amine may contain both hydroxy and amino groups as in alkanolamines or it may contain only amino groups as in alkylenediamines or PA .
  • a first preferred dispersant is a polyesteramine of formula (2): Y-CO[O-A-CO] n -Z-R (2) wherein
  • Y, A and n are as hereinbefore defined;
  • Z is a divalent bridging group; and R is an amino or ammonium group.
  • the divalent bridging group, Z is preferably of the formula
  • Q is hydrogen or alkyl and L is an alkylene or hydroxyalkylene group, or, when (2) is of formula (3) , N, Q and L, together with the group R form a cycloheteroaliphatic group.
  • the group Q preferably contains up to 25 carbon atoms.
  • the alkylene group which is, or which is present in, the group L preferably contains from 2 to 6 carbon atoms. Examples of the group represented by Q are methyl, ethyl, n-propyl, n-butyl and octadecyl and examples of the group represented by L are -(GH 2 ) 2 -,
  • group R is an amino group, it may be a primary, secondary or tertiary amino group and is preferably of the formula (5) :
  • T 1 and T 2 are independently hydrogen, C- ⁇ -alkyl, substituted C ⁇ a -alk !, aralkyl or cycloalkyl; or
  • T 1 and T 2 together with the nitrogen atom to which they are attached form a 5- or 6- membered ring.
  • T 1 or T 2 When T 1 or T 2 is alkyl, it is preferably C ⁇ -alkyl, such as methyl. When T 1 , T 2 and the nitrogen atom form a ring it is preferably piperidinyl, morpholinyl or especially an N-alkylpiperazinyl. When T 1 or T 2 is aralkyl, it is preferably benzyl.
  • the bridging group Z together with R forms a cycloheteroaliphatic group, one of T 1 or T 2 is incorporated into the bridging group.
  • the group -Z-R may be of the formula (6) :
  • T 1 and T 2 are other than hydrogen, so that R is tertiaryamino.
  • the group R is an ammonium group, it is preferably of the fo- ⁇ ula (7) :
  • T 3 is hydrogen, C ⁇ -alkyl, substituted C- ⁇ -alkyl, aralkyl or cycloalkyl;
  • W" is a colourless anion
  • the polyesterammonium salt is conveniently formed from the polyesteramine by reaction with an acid or quaterising agent.
  • the acids used to form the polyesterammonium salt may be inorganic or organic and include hydrochloric, sulphuric, acetic, formic, methanesulphonic, benzenesulphonic and benzoic acids.
  • the anion is methanesulphonic acid.
  • Preferred quaterising agents are dialkyl sulphates where the alkyl groups contain from 1 to 4 carbon atoms. An especially preferred quaterising agent is dimethylsulphate.
  • the polyesteramine or polyesterammonium salt is obtainable by reacting at least one PHCA with an appropriate amine in a suitable solvent followed by reaction with a salt or quaterising agent.
  • a salt or quaterising agent Such co ⁇ pounds may be prepared by any of the processes described in GB Patent Nos 1,342,746, 1,373,660, EP 127,325 and EP 23387 and all such dispersants are imported herein by reference.
  • Dispersant 1 may be prepared by the method in EP 23387.
  • a second preferred dispersant is obtainable by the reaction of a PHCA of formula I with a PAI to form a PAI derivative in which at least two PHCA's are attached to each PAI chain.
  • the PHCA is as described hereinbefore.
  • the PAI may be linear or branched, but is preferably branched, with at least 20% of the nitrogen atoms present as tertiary amino groups.
  • the molecular weight of the PAI is generally greater than 500, preferably greater than 5,000 and especially greater than 10,000.
  • the molecular weight is preferably less than 200,000, more preferably less than 100,000 and especially less than 50,000.
  • a preferred PAI is polyethyleneimine (hereinafter PEI)
  • PEI polyethyleneimine
  • the second preferred dispersant is obtainable by reacting up to 50 parts, preferably up to 30 parts, more preferably up to 10 parts and especially up to 5 parts of a PHCA with one part of a PAI wherein all parts are by weight.
  • a particularly useful dispersant of this type is that obtainable by reacting 3 parts of PHS with 1 part PEI having a molecular weight of about 20,000 (hereinafter Dispersant 2) .
  • Dispersant 2 may be prepared by the method described for Agent C in GB 2,001,083 except that a PEI with MW of 20,000 is used in place of the PEI with MW of 50,000.
  • a third preferred dispersant is that obtainable by reacting a PHCA of formula I with an amine of formula (8)
  • R 1 and R 2 are each independently Cj-g-alkylene
  • R 3 is Ci- 2 -alkyl; and where 0.8 to 1.0 molar equivalents of the amino groups are reacted with the PHCA.
  • Examples of amines of formula 8 are N,N-bis(aminoethyl) - methylamine; N,N-bis(amin ⁇ propyl)methylamine; N,N-bis(aminobutyl)methylamine; N,N-bis(aminoethyl)ethylamine; N,N-bis(aminopropyl)ethylamine; N,N-bis(aminobutyl)ethylamine and N- (aminomethyl) -N- (aminoethyl) -methylamine.
  • the preferred PHCA is PHS.
  • the preparation of compounds of this type are described in GB 5,000,792 and all such dispersants are imported herein by reference.
  • the CuPc fluidising agent is preferably at least partially soluble in the high-boiling liquid and co ⁇ prises a substituted ammonium salt of a CuPc acid wherein there are from 19 to 60 carbon atoms contained in at least 3 chains attached to the nitrogen atom of the substituted ammonium ion.
  • the CuPc fluidising agent contains at least four organic chains attached to each nitrogen atom of each substituted ammonium ion and these chains preferably contain, in total, between 25 and 40 carbon atoms. It is further preferred that at least one and more preferably two of the chains are alkyl or alkenyl groups containing at least 8 and preferably at least 12 carbon atoms, especially those groups containing between 12 and 20 carbon atoms.
  • the CuPc acid may be any CuPc molecule containing -COOH groups or more especially -S0 3 H groups which is capable of forming a salt with an amine or substituted ammonium salt to form the substituted ammonium salt of the CuPc acid.
  • the CuPc acid is preferably mono- or disulphonic or more especially a mixture thereof containing on average from 1.0 to 1.6 and especially from 1.1 to 1.5 sulphonic acids for each CuPc molecule.
  • amines and substituted ammonium salts which may be used to form the CuPc fluidising agent are tertiary amines and quaternary ammonium salts such as N,N-dimethyloctadecylamine, cetyl- trimethylammonium bromide, didodecyldimethylammonium chloride and dioctadecyldimethylammoni ⁇ m chloride.
  • the amines or substituted ammonium salts may contain polyester chains such as the amine and amine salts of the dispersants as described hereinbefore.
  • the amines and substituted ammonium salts may be cyclised wherein at least two of the organic chains are linked to form a ring containing the nitrogen atom which will form the charge centre of the substituted ammonium ion.
  • the ring or rings so formed may be aliphatic rings such as piperidine or aromatic rings such as pyridine and as examples of such amines or salts there may be mentioned N- cetylpiperidine.
  • One or more of the organic chains attached to the N-atom of the amine or substituted ammonium ion may be substituted by aromatic groups such as phenyl and substituted phenyl radicals which are free from acidic groups e.g. benzyldimethyloctadecylammonium chloride.
  • aromatic groups such as phenyl and substituted phenyl radicals which are free from acidic groups e.g. benzyldimethyloctadecylammonium chloride.
  • one or more of the organic chains may contain other nonacidic substituents such as hydroxy groups e.g. octadecylbis(2- hydroxyethyl)amine, amino or substituted amino e.g.
  • the preparation of the CuPc fluidising agent is described in GB 1,508,576 and all such agents are imported herein by reference. Particularly useful effects have been obtained when the fluidising agent is the dioctadecyldimethylammonii-im salt of a sulphonated CuPc containing an average of 1.3 sulphonic acid groups (hereinafter Fluidising Agent 1) .
  • the preparation of this is described as Agent A of GB 1,508,576.
  • the high boiling liquid may be any of those commonly used in the trade for making printing inks especially offset inks and varnishes. It may be aliphatic or aromatic in character and is preferably a mixture of aliphatic and aromatic distillates where the latter is in the smaller proportion than the former.
  • the aliphatic distillate is typically a coal-tar distillate and preferably has a boiling point between 200 and 360°C. Typical specific gravities are from 0.75 to 0.85.
  • the chemical composition of such aliphatic distillates has not been precisely determined, but the MW of the components is typically between about 170 and 320.
  • Some of the aliphatic distillates contain small amounts of aromatic components and this is especially preferred in the process according to the present invention. Examples of commercially available high boiling aliphatic distillates are those available from Magie Bros Oil Company, USA (e.g. MagieSol 47 and 52) and those available from Carless Refining Ltd, UK under the Paraset trade mark (e.g. Paraset 29L) .
  • the high boiling aromatic distillate preferably has a boiling point similar to that of the aliphatic distillate and also a specific gravity which is typically between 0.7 and 1.2.
  • high boiling aromatic distillates include benzene substituted by aliphatic chains containing up to 30 carbon atoms, especially up to 20 carbon atoms. These aliphatic chains may be linear or branched.
  • Other suitable aromatic distillates are esters obtainable from phthalic acid or phthalic anhydride such as dimethylphthalate and esters obtainable from benzalmalonates such as diethylbenzalmalonate.
  • the process according to the present invention may be carried out in a high energy bead mill.
  • Any bead mill commonly used in the trade may be used provided that in operation a te ⁇ perature in excess of 50°C is obtainable. This may be achieved by external heating with a heated jacket or be exploiting the heat generated during operation of the mill.
  • a suitable bead mill is a Netzsch LM-II mill. It is preferred that milling is carried out above 75°C and especially above 90°C.
  • the diameter of the beads depends to a large extent on the type of mill used.
  • the diameter of the beads is preferably greater than 2 mm and also preferably less than 5 mm and especially less than 3 mm.
  • the diameter of the beads is preferably not greater than 2 mm, more preferably less than 1 mm and especially less than 0.5 mm, for example 0.25 mm.
  • Milling of the crude CuPc is continued until the mean particle size is below 50 microns, preferably below 20 microns and especially below 10 microns.
  • printing inks or varnishes obtained using the process of the present invention produce clear greenish blue shades which are greener and brighter than those obtained when milling is carried out at below 50°C or by milling solely in a high boiling aliphatic distillate containing no high boiling aromatic distillate.
  • the greenest and brightest shades are obtainable when milling is carried out in a high-boiling aliphatic distillate which also contains an aromatic distillate and at temperatures above 50°C. It has also been found that the amount of CuPc fluidising agent can be decreased as the milling temperature is increased.
  • the NAD also preferably contains an alkyd resin to improve the compatibility and stability of the NAD when let down into an ink or varnish.
  • the alkyd resin may be any suitable resin which is commonly used in the trade, but is preferably a "long oil" alkyd resin obtainable by reacting a long chain saturated or unsaturated fatty acid with a polyol and a di- or tri-carboxylic acid or their anhydrides.
  • the carboxylic acids are preferably aromatic in character, for example phthalic acid or trimellitic anhydride.
  • Preferred fatty acids are C 16 - 18 -aliphatic acids which may be saturated or unsaturated.
  • the NAD typically contains at least 5%, preferably at least 10%, more preferably at least 15% and especially at least 25% by weight CuPc relative to the total weight of the NAD. It is also preferred that the NAD contains less than 70%, more preferably less than 60% and especially less than 45% CuPc by weight relative to the total weight of the NAD.
  • the NAD contains at least 0.5% dispersant, more preferably at least 1% and especially at least 2% by weight of the NAD.
  • the amount of dispersant in the NAD can be the same as the amount of crude CuPc it is not generally necessary to use this amount. Consequently, it is preferred that the -amount of the dispersant is less than 25%, more preferably less than 15% and especially less than 10% by weight of the NAD.
  • the CuPc fluidising agent is preferably at least 0.1%, more preferably at least 0.3% and especially at least 0.5% by weight of the NAD. Typically, the fluidising agent is less than 10%, preferably less than 5% and especially less than 3% by weight of the NAD.
  • the high boiling liquid is preferably at least 20%, more preferably at least 30% and especially at least 40% by weight of the NAD.
  • the distillate is less than 90%, preferably less than 80%, more preferably less than 70% and especially less than 60% of the NAD.
  • the high boiling distillate may be aliphatic or aromatic in nature or preferably a mixture of both.
  • the high boiling liquid is a mixture of aliphatic and aromatic distillates in which the latter is the smaller proportion it preferably contains at least 0.1%, preferably at least 0.3% and especially at least 0.5% aromatic distillate based on the total weight of the NAD. It is also preferably less than 10%, more preferably less than 7% and especially less than 5% by weight, of the NAD.
  • the resin is typically at least 0.1%, preferably at least 0.3% and especially at least 0.5% by weight of the NAD.
  • the resin is preferably less than 10%, more preferably less than 7% and especially less than 5% by weight of the NAD.
  • the NAD prepared in accordance with the process of the present invention gives clearer and greener shades of CuPc in a high-boiling liquid than those obtained hitherto.
  • the invention therefore also provides a composition obtainable by a process according to the present invention as described hereinbefore.
  • the NAD obtainable by the process of the present invention is suitable for use in the formulation of printing inks, especially off- set inks, and varnishes to give a clear, bright greenish blue image.
  • the NAD made by the process according to the invention may be diluted with a solvent based ink or with a white ink and used directly for printing.
  • the ink may additionally contain any other adjuvants commonly used in printing, particularly off-set printing.
  • the present invention also provides a clear, bright greenish blue image by application of the NAD to a substrate.
  • a mixture of xylene (348 parts) and a commercial grade of 12-hydroxystearic acid (3350 parts; having acid and hydroxyl values of 182 mg.KOH/gm and 160 mg.KOH/gm respectively) is stirred for 22 hours at 190° to 200°C, the water formed in the reaction being separated from the xylene in the distillate which is then returned to the reaction medium. After 152 parts of water have been collected, the xylene is removed by heating at 200°C in a stream of nitrogen. The resulting pale amber coloured liquid has an acid value of 35.0 mgms/KOH/gm.
  • Dispersant 1 A mixture of polyester A (320 parts) , 3- dimethylaminopropylamine (10.2 parts) and toluene (65 parts) was stirred under reflux and under a current of nitrogen using a Dean & Stark head to remove water. The temperature was raised to 165°C and held at this temperature for 6 hours. After cooling to 20 to 25°C under nitrogen, an 87.6% solution of the adduct was obtained.
  • Dispersant 1 Preparation of Dispersant 2 Hydroxystearic acid (159 parts) was polymerised by stirring at 170-180°C in the presence of tetrabutyltitanate (1 part) as catalyst under a nitrogen atmosphere in a vessel equipped with a Dean and Stark separator until the polymer has an acid value of about 35 mg KQH/gm.
  • Polyhydroxystearic acid (159 parts) prepared as above and highly-branched polyethyleneimine (53 parts, Polymin ex BASF) were stirred at 120°C under nitrogen for about 3 hrs until the product had an acid value of 16-20 mg KOH/gm. On cooling, the product was obtained as a brown gum.
  • Example 1 The procedure of Example 1 was repeated with the exception that milling was carried out in the absence of dodecylbenzene using the Paraset aliphatic distillate alone (110 parts) and maintaining a temperature of 45°C throughout using external cooling.
  • Example 1 was repeated but maintaining a milling te ⁇ perature of 70°C throughout.
  • Example 2 was repeated except that the dodecylbenzene was replaced by the same amount of dimethylphthalate. i le Example 2 was again repeated except that the dodecylbenzene was replaced by the same amount of diethylbenzalmalonate. Sampl ?
  • the NADs of the above examples (1 part) was mixed with a white ink previously prepared from titanium dioxide pigment (18 parts, Tioxide RCR2) Dispersant 1 (0.4 parts), zinc/calcium rosinate (5.4 parts, Pexate RT3) and toluene (6.56 parts) .
  • the prepared ink was coated onto butakon coated paper with a number 2 K-bar using an automatic coater (Model KCC 202, RK Print-Coat Instruments, UK) . After drying the colour co-ordinates of the various prints were measured using a Chroma Meter CR-221 (Minolta, UK) .

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Inks, Pencil-Leads, Or Crayons (AREA)
  • Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
  • Colloid Chemistry (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Glass Compositions (AREA)
  • Iron Core Of Rotating Electric Machines (AREA)
  • Photoreceptors In Electrophotography (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Heterocyclic Carbon Compounds Containing A Hetero Ring Having Nitrogen And Oxygen As The Only Ring Hetero Atoms (AREA)
  • Cosmetics (AREA)
  • Nitrogen Condensed Heterocyclic Rings (AREA)
PCT/GB1994/002786 1993-12-23 1994-12-20 Process for making a non-aqueous dispersion of a cooper phthalocyanine WO1995017473A1 (en)

Priority Applications (8)

Application Number Priority Date Filing Date Title
AU12776/95A AU680084B2 (en) 1993-12-23 1994-12-20 Process for making a non-aqueous dispersion of a copper phthalocyanine
DK95903873T DK0736070T3 (da) 1993-12-23 1994-12-20 Fremgangsmåde til fremstilling af en ikke-vandig dispersion af en kobberphthalocyanin
BR9408366A BR9408366A (pt) 1993-12-23 1994-12-20 Processo de preparação de uma dispersão não aquosa de uma cupo e tinta de impressão contendo a mesma
CA002179749A CA2179749C (en) 1993-12-23 1994-12-20 Process for making a non-aqueous dispersion of a copper phthalocyanine
DE69416695T DE69416695T2 (de) 1993-12-23 1994-12-20 Verfahren zur herstellung von nicht wässrigen dispersionen von einem kupferphthlocyyanin
US08/596,179 US5753022A (en) 1993-12-23 1994-12-20 Process
JP7517268A JPH09506922A (ja) 1993-12-23 1994-12-20 方 法
EP95903873A EP0736070B1 (en) 1993-12-23 1994-12-20 Process for making a non-aqueous dispersion of a cooper phthalocyanine

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Application Number Priority Date Filing Date Title
GB9326374.7 1993-12-23
GB939326374A GB9326374D0 (en) 1993-12-23 1993-12-23 Process

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EP0774494A1 (en) 1995-11-16 1997-05-21 Ciba SC Holding AG Process for the production of ink concentrates
US6031030A (en) * 1997-05-15 2000-02-29 Ciba Speicialty Chemicals Corporation Production process
WO2000024503A1 (en) * 1998-10-24 2000-05-04 Avecia Limited Dispersants, compositions and use
US6458173B1 (en) 1998-12-04 2002-10-01 Infineum International Ltd. Fuel additive and fuel composition containing the same
WO2002077111A1 (en) * 2001-03-22 2002-10-03 Avecia Limited Paint compositions
EP1493782A1 (en) * 2003-06-30 2005-01-05 Toyo Ink Mfg. Co., Ltd. Pigment dispersion and use thereof
WO2007128740A1 (en) * 2006-05-03 2007-11-15 Shell Internationale Research Maatschappij B.V. Lubricating oil composition
WO2009012514A1 (en) * 2007-07-24 2009-01-29 Silverbrook Research Pty Ltd Phthalocyanine salts suitable for use in offset inks
WO2010149712A1 (en) 2009-06-25 2010-12-29 Shell Internationale Research Maatschappij B.V. Lubricating composition
US20110207640A1 (en) * 2008-07-31 2011-08-25 Jan Elsa Eugenia Carty Poly (hydroxycarboxylic acid) amide salt derivative and lubricating composition containing it
WO2012163935A2 (en) 2011-05-30 2012-12-06 Shell Internationale Research Maatschappij B.V. Liquid fuel compositions

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GB0304941D0 (en) * 2003-03-05 2003-04-09 Avecia Ltd Use of dispersions in making electronic devices
SG156674A1 (en) * 2004-10-27 2009-11-26 Lubrizol Corp Asphaltene inhibition
EP2055729A1 (en) * 2007-10-23 2009-05-06 Shell Internationale Researchmaatschappij B.V. Lubricating composition
WO2012154515A1 (en) * 2011-05-06 2012-11-15 Lubrizol Advanced Materials, Inc. Polyester quaternary salt and compositions thereof
AU2012355431A1 (en) 2011-12-21 2014-06-12 Shell Internationale Research Maatschappij B.V. Method and composition for inhibiting wax in a hydrocarbon mixture
GB2510522A (en) 2011-12-21 2014-08-06 Shell Int Research Method and composition for inhibiting asphaltene deposition in a hydrocarbon mixture
US9453173B2 (en) 2011-12-21 2016-09-27 Shell Oil Company Method and composition for inhibiting foam in a hydrocarbon mixture
WO2019124050A1 (ja) * 2017-12-22 2019-06-27 Dic株式会社 銅フタロシアニン顔料組成物及びこれを有するインキ組成物
US20220220324A1 (en) * 2019-04-18 2022-07-14 Basf Se Amine dispersants

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Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5964929A (en) * 1995-11-16 1999-10-12 Ciba Specialty Chemicals Corporation Process for the production of ink concentrates
EP0774494A1 (en) 1995-11-16 1997-05-21 Ciba SC Holding AG Process for the production of ink concentrates
US6031030A (en) * 1997-05-15 2000-02-29 Ciba Speicialty Chemicals Corporation Production process
WO2000024503A1 (en) * 1998-10-24 2000-05-04 Avecia Limited Dispersants, compositions and use
US6458173B1 (en) 1998-12-04 2002-10-01 Infineum International Ltd. Fuel additive and fuel composition containing the same
WO2002077111A1 (en) * 2001-03-22 2002-10-03 Avecia Limited Paint compositions
US7008988B2 (en) 2001-03-22 2006-03-07 The Lubrizol Corporation Paint compositions
US7381760B2 (en) 2003-06-30 2008-06-03 Toyo Ink Mfg.Co., Ltd. Pigment dispersion and use thereof
EP1493782A1 (en) * 2003-06-30 2005-01-05 Toyo Ink Mfg. Co., Ltd. Pigment dispersion and use thereof
WO2007128740A1 (en) * 2006-05-03 2007-11-15 Shell Internationale Research Maatschappij B.V. Lubricating oil composition
RU2458108C2 (ru) * 2006-05-03 2012-08-10 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Композиция смазочного масла
WO2009012514A1 (en) * 2007-07-24 2009-01-29 Silverbrook Research Pty Ltd Phthalocyanine salts suitable for use in offset inks
US7566363B2 (en) 2007-07-24 2009-07-28 Silverbrook Research Pty Ltd Alternative phthalocyanine dyes suitable for use in offset inks
AU2008280815B2 (en) * 2007-07-24 2011-04-28 Silverbrook Research Pty Ltd Phthalocyanine salts suitable for use in offset inks
US20110207640A1 (en) * 2008-07-31 2011-08-25 Jan Elsa Eugenia Carty Poly (hydroxycarboxylic acid) amide salt derivative and lubricating composition containing it
US8633142B2 (en) 2008-07-31 2014-01-21 Shell Oil Company Poly (hydroxycarboxylic acid) amide salt derivative and lubricating composition containing it
WO2010149712A1 (en) 2009-06-25 2010-12-29 Shell Internationale Research Maatschappij B.V. Lubricating composition
WO2012163935A2 (en) 2011-05-30 2012-12-06 Shell Internationale Research Maatschappij B.V. Liquid fuel compositions

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ES2128036T3 (es) 1999-05-01
IN190998B (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html) 2003-09-06
US5753022A (en) 1998-05-19
GB9326374D0 (en) 1994-02-23
KR100355219B1 (ko) 2003-01-29
EP0736070A1 (en) 1996-10-09
BR9408366A (pt) 1997-08-26
AU1277695A (en) 1995-07-10
KR970700733A (ko) 1997-02-12
ATE176918T1 (de) 1999-03-15
DE69416695T2 (de) 1999-07-08
AU680084B2 (en) 1997-07-17
CA2179749C (en) 2001-08-28
GB9424114D0 (en) 1995-01-18
GB9425636D0 (en) 1995-02-22
EP0736070B1 (en) 1999-02-24
JPH09506922A (ja) 1997-07-08
TW272224B (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html) 1996-03-11
DE69416695D1 (de) 1999-04-01
DK0736070T3 (da) 1999-08-23
CA2179749A1 (en) 1995-06-29

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