DK152512B - SULPHORIC ACID HALVESTER PREPARATIONS USED AS DISPERSIBLE IN PIGMENT PREPARATIONS FOR Aqueous FLEXOTRY COLORS AND PROCEDURES FOR ITS PREPARATION - Google Patents

SULPHORIC ACID HALVESTER PREPARATIONS USED AS DISPERSIBLE IN PIGMENT PREPARATIONS FOR Aqueous FLEXOTRY COLORS AND PROCEDURES FOR ITS PREPARATION Download PDF

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DK152512B
DK152512B DK325472A DK325472A DK152512B DK 152512 B DK152512 B DK 152512B DK 325472 A DK325472 A DK 325472A DK 325472 A DK325472 A DK 325472A DK 152512 B DK152512 B DK 152512B
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pigment
weight
preparations
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DK325472A
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DK152512C (en
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Reinhold Deubel
Max Grossmann
Volker Hemmerling
Heinz Uhrig
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Hoechst Ag
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C309/00Sulfonic acids; Halides, esters, or anhydrides thereof
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09BORGANIC DYES OR CLOSELY-RELATED COMPOUNDS FOR PRODUCING DYES, e.g. PIGMENTS; MORDANTS; LAKES
    • C09B67/00Influencing 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
    • C09B67/0071Process features in the making of dyestuff preparations; Dehydrating agents; Dispersing agents; Dustfree compositions
    • C09B67/0084Dispersions of dyes
    • C09B67/0085Non common dispersing 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
    • C09D11/00Inks
    • C09D11/02Printing inks
    • C09D11/03Printing inks characterised by features other than the chemical nature of the binder

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Materials Engineering (AREA)
  • Wood Science & Technology (AREA)
  • Inks, Pencil-Leads, Or Crayons (AREA)
  • Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Coloring (AREA)

Description

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iin

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De krav, der stilles til pigmentpræparater til anvendelse ved vandigt flexotryk, er blevet væsentlig større på grund af anvendelsen af hurtigtgående trykkemaskiner og nye udviklinger inden for bindemiddelsektoren. Til det-5 te formål kræves strømmedygtige indstillinger med høje pigmentkoncentrationer. Da faststofkoncentrationerne i det ved flexotryk anvendte bindemiddel omtrentligt ligger mellem 15 og 30 vægt%, og der ved et blandingsforhold mellem bindemiddel og pigment på ca. 2:1 i trykfarven skal overholdes et 10 bestemt viskositetsområde, bør der kun bringes en ringe andel væske ind via pigmentpræparatet. Endvidere bør pigmentdejene kun indeholde skumfattige fordelingsmidler, der også betegnes som dispergeringsmidler, for at en opskumning af den pigmenterede trykfarve kan forhindres, hvilket kun-15 ne føre til koagulering af pigmenterne og til uensartede tryk. Foruden det gunstige skumforhold kræves der en ringe egenfarve af fordelingsmidlerne, især ved lyse og brillante farvetoner. Trods høje pigmentkoncentrationer skal dejene være strømme- eller pumpedygtige, for at de kan være 20 simple at håndtere og opfylde doseringskrav i praksis. De for tiden gængse fordelingsmidler opfylder imidlertid kun det ene eller det andet af de ovennævnte krav. Med bestemte ligninsulfonater kan der f.eks. således fremstilles strømmedygtige pigmentdeje af højere koncentration, der dog 25 kun kan anvendes i begrænset omfang på grund af fordelingsmidlernes egenfarve. Fordelingsmidler på naphthaiensulfon-syre-formaldehyd-basis har i forhold hertil ganske vist en ringe egenfarvning og ringe skumtilbøjelighed, men i høje pigmentkoncentrationer kan de ikke forarbejdes til strømme-30 dygtige deje.The demands made on pigment preparations for use in aqueous flexo printing have become considerably greater due to the use of fast-moving printing machines and new developments in the binder sector. For the 5 th purpose, flowable settings with high pigment concentrations are required. Since the solids concentration in the binder used in flexo printing is approximately between 15 and 30% by weight, and at a binder-pigment blend ratio of approx. 2: 1 of the ink must be adhered to a certain viscosity range, only a small amount of liquid should be introduced via the pigment preparation. Furthermore, the pigment doughs should contain only foam-poor distribution agents, also referred to as dispersing agents, to prevent foaming of the pigmented ink, which can lead to coagulation of the pigments and to disparate pressures. In addition to the favorable foam ratio, a low intrinsic color of the dispersants is required, especially in light and brilliant tones. Despite high pigment concentrations, the dough must be fluid or pumpable in order for it to be 20 simple to handle and meet dosing requirements in practice. However, the current distribution means meet only one or the other of the above requirements. With certain lignin sulfonates, e.g. Thus, higher concentration flowable pigment doughs are produced, however, to a limited extent only because of the intrinsic color of the dispersants. Naphthalenesulfonic acid-formaldehyde-based dispersants have a poor intrinsic staining and poor foaming properties, but at high pigment concentrations they cannot be processed into flowable doughs.

Ved anvendelse af oxalkylerede alkylphenoler eller deres sulfateringsprodukter kan der ganske vist fremstilles strømmedygtige deje med højere pigmentkoncentrationer, men dejene kan dog kun anvendes i begrænset omfang i vandige 35 flexotrykfarver på grund af deres stærke skumdannelse. DeUsing oxalkylated alkyl phenols or their sulfating products, flowable doughs with higher pigment concentrations can be produced, but the doughs can only be used to a limited extent in aqueous flexo printing colors due to their strong foaming. The

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på basis af sådanne fordelingsmidler udviklede, i handelen værende vandige pigmentdeje anvendes overvejende til indfarvning af dispersionsfarver til indvendige og udvendige udstrygninger eller til pigmenttryk på tekstiler. De opfyl-5 der imidlertid ikke de høje krav, der stilles til vandige flexotrykfarver, og de er derfor ikke egnede til dette anvendelsesområde .Based on such distribution agents, commercially available aqueous pigment doughs are predominantly used for dyeing dispersion paints for interior and exterior smears or for pigment printing on textiles. However, they do not meet the high requirements of aqueous flexo inks and are therefore not suitable for this field of application.

Problemet med skumdannelse optræder ligeledes, når man anvender de olieopløselige salte med organiske aminer 10 og sulforavsyreestere af oxalkylerede enkernede alkylpheno-ler, som er kendt fra GB-patentskrift nr. 1.108.410, og når man anvender de α-sulfocarboxylsyreestere af oxalkylerede novolakker, som er kendt fra US-patentskrift nr. 3.320.212, og i hvilke der ved anvendelse af dicarboxylsyrer er bundet 15 en sulfogruppe i α-stilling til hver carboxygruppe. På grund af skumdannelsen er heller ikke de forbindelser, som er beskrevet i- de nævnte patentskrifter, egnede til anvendelse i moderne flexotrykfarver.The problem of foaming also occurs when using the oil-soluble salts with organic amines 10 and sulfuric acid esters of oxalkylated single-chain alkyl phenols known from GB-A-1,108,410, and when using the α-sulfocarboxylic acid esters of oxalkylated novolacs, which is known from US Patent No. 3,320,212 and in which, using dicarboxylic acids, a sulfo group at the α position is attached to each carboxy group. Also, because of the foaming, the compounds described in the aforementioned patents are not suitable for use in modern flexo inks.

Det har overraskende vist sig, at problemerne med de 20 kendte forbindelser kan løses ved anvendelse af det her omhandlede sulforavsyrehalvesterpræparat, som er anvendeligt som dispergeringsmiddel i pigmentpræparater til vandige fle-xotrykfarver, specielt i pigmentpræparater til anvendelse ved vandigt flexotryk i hurtiggående trykkemaskiner.Surprisingly, it has been found that the problems of the known compounds can be solved by using the present sulforic acid half-ester composition which is useful as a dispersant in pigment preparations for aqueous flexo inks, especially in pigment preparations for use in aqueous flexo printing in high-speed printing machines.

25 Opfindelsen angår derfor et sulforavsyrehalvesterpræ parat til anvendelse som dispergeringsmiddel i pigmentpræparater til vandige flexotrykfarver, og det her omhandlede præparat er ejendommeligt ved, at det består af en blanding af forbindelser med den almene formelThe invention therefore relates to a sulfuric acid half-halter composition for use as a dispersant in pigment preparations for aqueous flexo inks, and the present invention is characterized in that it consists of a mixture of compounds of the general formula

30 I B - (0 - X)n - 0 0 - (X - 0)n - A30 I B - (0 - X) n - 0 0 - (X - 0) n - A

J-Λ-J—ΛJ-J Λ Λ

R _ * RR _ * R

35 — z35 - z

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hvor A betyder en gruppe med formlen -CO-CH2-CH-COOMe el- S03Me ler -CO-CH-CHj-COOMe, B betyder et hydrogenatom og/eller S03Me 5 fortrinsvis en gruppe med betydningen af A, X betyder en ethylen- eller propylengruppe, R betyder en mættet alkyl-gruppe med 6-14 carbonatomer, Me betyder et hydrogenatom, et alkalimetalatom eller et ækvivalent jordalkalimetal-atom, n er et helt tal fra 2 til 25, fortrinsvis fra 3 til 10 15, og z er et tal fra 1 til 9.wherein A represents a group of the formula -CO-CH 2 -CH-COOMe or -SO 3 Me or -CO-CH-CH 2 -COOMe, B represents a hydrogen atom and / or SO 3 Me 5 preferably a group of the meaning of A, X means an ethylene- or propylene group, R is a saturated alkyl group of 6-14 carbon atoms, Me is a hydrogen atom, an alkali metal atom or an equivalent alkaline earth metal atom, n is an integer from 2 to 25, preferably from 3 to 10, and z is a number from 1 to 9.

Opfindelsen angår ligeledes en fremgangsmåde til fremstilling af sulforavsyrehalvesterpræparater bestående af en blanding af forbindelser med den almene formel (I), hvilken fremgangsmåde er ejendommelig ved, at man oxethy-15 lerer eller oxpropylerer flerkernede alkylphenoler med formlenThe invention also relates to a process for the preparation of sulphorboxylic acid ester preparations consisting of a mixture of compounds of the general formula (I), which is characterized by oxethylation or oxpropylation of multi-core alkylphenols of the formula

]" OH OH] "OH OH

* Ά ,Ά 2o H~i—H-. -i- (II> y : Λ*; L -i 2 hvor R og z har den ovenfor anførte betydning, omsætter de på denne måde fremkomne oxethylater eller oxpropylater med 25 maleinsyreanhydrid til maleinsyrehalvesterne og derpå sætter alkalimetal- eller jordalkalimetalsulfiter til disse.* Ά, Ά 2o H ~ i — H-. -I (II> y: Λ *; L-i 2 where R and z have the meaning given above, react the oxethylates or oxpropylates thus obtained with maleic anhydride to the maleic acid halves and then add alkali metal or alkaline earth metal sulfites thereto.

Egnede som udgangsprodukter med den almene formel (II) er flerkernede alkylphenoler (novolakker), således som de fås ved sur kondensation af monoalkylphenoler, f.eks. octyl-, 30 nonyl-, dodecylphenol eller blandinger deraf med formaldehyd i molforholdet 2:1 - 10:9. Formaldehydet kan anvendes som vandig opløsning eller som paraformaldehyd. Som katalysatorer kan der anvendes mineralsyrer, såsom svovlsyre, phos-phorsyre eller fortrinsvis saltsyre på grund af dennes lette 35 flygtighed, i en koncentration på fra 0,1 til 5 vægt%. Kon- 4Suitable starting materials of the general formula (II) are multi-core alkyl phenols (novolacs) as obtained by acidic condensation of monoalkyl phenols, e.g. octyl, nonyl, dodecylphenol or mixtures thereof with formaldehyde in the molar ratio of 2: 1 - 10: 9. The formaldehyde can be used as an aqueous solution or as paraformaldehyde. As catalysts, mineral acids such as sulfuric acid, phosphoric acid or preferably hydrochloric acid due to its light volatility can be used at a concentration of from 0.1 to 5% by weight. Con- 4

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CC

densationen gennemføres under nitrogen ved temperaturer på fra 20 til 150°C, fortrinsvis 80-130°C. Det vand, der er til stede efter kondensationen, skal afdestilleres, til sidst under formindsket tryk (< 50 mm Hg), indtil vandindholdet i 5 harpiksen er mindre end 0,3%.densification is carried out under nitrogen at temperatures of from 20 to 150 ° C, preferably 80-130 ° C. The water present after the condensation must be distilled off, finally under reduced pressure (<50 mm Hg), until the water content of the resin is less than 0.3%.

Disse novolakker er mere eller mindre sprøde, klare, i store blokke gulbruntfarvede harpikser. De består af blandinger af flerkernede, med methylenbroer forbundne alkylphe-nolkerner. Sammensætningen er fremfor alt af hasngig af forhol-10 det mellem alkylphenol og formaldehyd.These novolaks are more or less brittle, clear, in large blocks of yellow-brown colored resins. They consist of mixtures of multicore, methylene bridges linked to methylphenol cores. The composition is, above all, of the relationship between alkyl phenol and formaldehyde.

Oxalkyleringen af både de enkernede og de flerkernede alkylphenoler sker med alkylenoxider, f.eks. 1,2-propylenoxid eller fortrinsvis med ethylenoxid, ved kendte metoder, fortrinsvis med alkalimetalhydroxider eller -alkoxider som 15 katalysatorer, ved 100-200°C·, fortrinsvis ved 140-170°C.The oxalkylation of both the mono-core and the multi-core alkyl phenols occurs with alkylene oxides, e.g. 1,2-propylene oxide or preferably with ethylene oxide, by known methods, preferably with alkali metal hydroxides or alkoxides as catalysts, at 100-200 ° C, preferably at 140-170 ° C.

Mængden af alkylenoxid afpasses således, at der for hver phe-nolisk hydroxylgruppe indføres mellem 2 og 25 mol alkylenoxid.The amount of alkylene oxide is adjusted so that for each phenolic hydroxyl group, between 2 and 25 moles of alkylene oxide are introduced.

Egnede som alkalimetalhydroxider er kaliumhydroxid 20 eller fortrinsvis natriumhydroxid, som alkalimetaloxider, . natriummethylat eller -ethylat, og koncentrationen skal fortrinsvis være 0,05-1,0 vægt%, beregnet på phenolen ved oxal-kyleringens begyndelse. Oxalkyleringen kan gennemføres uden tryk eller i trykbeholdere med propylenoxid eller fortrins-25 vis ethylenoxid eller blandinger af begge to, idet alkylen-oxidet kan tilføres i gasform eller i flydende form.Suitable as alkali metal hydroxides are potassium hydroxide or preferably sodium hydroxide, such as alkali metal oxides. sodium methylate or ethylate, and the concentration should preferably be 0.05-1.0% by weight, calculated on the phenol at the beginning of oxalkylation. The oxalkylation can be carried out without pressure or in pressure vessels with propylene oxide or preferably ethylene oxide or mixtures of both, the alkylene oxide being supplied in gaseous or liquid form.

Reaktionen af de på denne måde fremstillede oxalkyla-ter med maleinsyreanhydrid til maleinsyrehalveesterne sker ved sammenblanding af komponenterne og omrøring ved 20-100°C, 30 fortrinsvis 40-80°C, i nærværelse af alkalimetalhydroxider, hvis koncentration skal andrage 0,05-1,0 vægt%, beregnet på den samlede blanding. Da maleinsyreanhydrid har tendens til sublimering, er det fordelagtigt at arbejde i trykbeholdere med et tryk på 0,2-1,0 ato nitrogen eller luft og at sørge 35 for kraftig sammenblanding, fordi det smeltede maleinsyre-The reaction of the oxalkylates thus prepared with maleic anhydride to the maleic acid esters is effected by mixing the components and stirring at 20-100 ° C, preferably 40-80 ° C, in the presence of alkali metal hydroxides whose concentration should be 0.05-1 , 0% by weight, based on the total mixture. Since maleic anhydride tends to sublimate, it is advantageous to operate in pressure vessels having a pressure of 0.2-1.0 ato nitrogen or air and to provide vigorous mixing because the molten maleic acid

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anhydrid ved reaktionens begyndelse er dårligt blandbart med oxalkylaterne. Mængden af maleinsyreanhydrid kan afpasses således, at alle oxalkylat-hydroxyl-endegrupperne eller blot en del deraf, dog mindst én, omsættes.anhydride at the beginning of the reaction is poorly miscible with the oxalkylates. The amount of maleic anhydride can be adjusted so that all the oxalkylate-hydroxyl end groups or just a portion thereof, but at least one, is reacted.

5 Omdannelsen af disse maleinsyrehalvester-forbindel- ser til de tilsvarende sulforavsyrehalvestere sker efter tilsætning af vandige opløsninger af sulfiter eller hydro-gensulfiter. For hver maleinsyrehalvestergruppe anvendes 1,0-1,5, fortrinsvis 1,05-1,1 mol, beregnet som svovlsyr-10 ling, i form af alkalimetal- eller jordalkalimetalsulfiter eller -bisulfiter eller -pyrosulfiter. Sulfiterne er særlig egnede her, fordi der herved opstår disaltene af sulfo-ravsyrehalvesterne.The conversion of these maleic acid half-ester compounds to the corresponding sulfuric acid halvesters occurs after the addition of aqueous solutions of sulfites or hydrogen sulfites. For each maleic acid half ester group, 1.0-1.5, preferably 1.05-1.1 mole, calculated as sulfuric acid, is used in the form of alkali metal or alkaline earth metal sulfites or bisulfites or pyrosulfites. The sulfites are particularly suitable here because of the disalts of the sulfuric acid halves.

Den tilsatte vandmængde kan andrage 50-85 vægt%, be-15 regnet på den samlede opløsning eller blanding, og er afhængig af sulforavsyrehalvestersaltenes opløselighed og opløsningernes viskositet. Reaktionstemperaturerne ligger på 20-100°C, fortrinsvis 40-80°C. De på denne måde fremstillede 15-50%'s vandige opløsninger kan anvendes direkte. Man 20 kan imidlertid også fjerne vandet fra disse opløsninger, f.eks. ved sprøjtetørring,, før den videre anvendelse.The amount of water added may be 50-85% by weight, based on the total solution or mixture, and is dependent on the solubility of the sulfuric acid half salts and the viscosity of the solutions. The reaction temperatures are at 20-100 ° C, preferably 40-80 ° C. The 15-50% aqueous solutions thus prepared can be used directly. However, the water can also be removed from these solutions, e.g. by spray drying ,, before further application.

På grund af deres ringe tilbøjelighed til opskum-ning og deres ringe egenfarve er de på denne måde fremstillede sulforavsyrehalvesterpræparater fremragende egnede som 25 fordelingsmidler ved fremstillingen af højpigmenterede og strømmedygtige pigmentpræparationer, der anvendes i vandigt flexotryk.Because of their low foaming propensity and poor intrinsic color, the sulfuric acid half-ester preparations thus prepared are excellent as distribution agents in the preparation of highly pigmented and flowable pigment preparations used in aqueous flexo printing.

Fremstillingen af pigmentpræparaterne sker på kendt måde ved, at man dispergerer pigmenterne, f.eks. azopigmen-30 ter, azopigmenter med lakegenskaber, triphenylmethanpigmen-ter, thioindigopigmenter, perylentetracarboxylsyrepigmenter, dioxazinpigmenter, quinacridonpigmenter eller phthalocyanin-pigmenter, med sulforavsyrehalvesterpræparaterne under tilsætning af ethylenglycol, vand og eventuelt ringe mængder af 35 andre dispergeringsmidler i et egnet dispergeringsapparat,The pigment preparations are prepared in a known manner by dispersing the pigments, e.g. azopigments, azopigments with lacquer properties, triphenylmethane pigments, thioindigopigments, perylenetetracarboxylic pigments, dioxazine pigments, quinacridone pigments or other phthalocyanine pigments,

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f.eks. en perlemølle eller et ælteapparat med dobbelttrug.eg. a mother-of-pearl or double-knit kneader.

Ved fremstillingen i ælteapparatet gås der frem på den måde, at pigmenterne indføres i den vandige opløsning af sulforav-syrehalvesterpræparatet, der i forvejen er anbragt i ælte-5 apparatet, eventuelt under tilsætning af ringe mængder af andre dispergeringsmidler, og æltes ved sej konsistens. Efter endt finfordeling fortyndes der til den ønskede farvestyrke og konsistens ved tilsætning af ethylenglycol og vand. Ved anvendelse af en perlemølle homogeniseres pigmen-10 terne ved omrøring til en dej i en blanding af det ovenfor beskrevne, vandige fordelingsmiddel, ethylenglycol og vand samt eventuelt ringe mængder af andre fordelingsmidler. Denne pumpedygtige suspension formales derpå almindeligvis i en kontinuerlig røreværkmølle med kvartsitperler med en dia-15 meter på 1-3 mm, eventuelt ad flere omgange, til den ønskede finfordeling. Derpå kan der indstilles på den ønskede farvestyrke med vand eller ethylenglycol. Forholdet mellem fordelingsmiddel og pigmentpulver kan varieres inden for vide grænser og andrager almindeligvis fra 0,1 til 0,2 vægt-20 dele fordelingsmiddel pr. 1 del tørt pigmentpulver.In the preparation of the kneader, the pigments are introduced by introducing the pigments into the aqueous solution of the sulphuric acid half-ester composition which is already placed in the kneading apparatus, optionally with the addition of small amounts of other dispersing agents, and kneading by tough consistency. After finishing, the desired color strength and consistency are diluted by the addition of ethylene glycol and water. Using a bead mill, the pigments are homogenized by stirring to a dough in a mixture of the above-described aqueous dispersant, ethylene glycol and water, and optionally small amounts of other dispersants. This pumpable suspension is then generally milled in a continuous quartz bead mill with a diameter of 1-3 mm, possibly several times, for the desired distribution. Then the desired color strength can be adjusted with water or ethylene glycol. The ratio of dispersant to pigment powder can be varied within wide limits and is generally from 0.1 to 0.2 parts by weight by weight of dispersant. 1 part dry pigment powder.

EksempelExample

Fremstilling af sulforavsyrehalvesterpræparater af oxalkyle-rede flerkernede alkylphenoler.Preparation of Sulphoric Acid Half -ester Preparations of Oxalkylated Multi-Core Alkyl Phenols.

25 a) Novolakfremstilling z + 1 mol alkylphenol og Z mol formaldehyd blandes ved stuetemperatur og omrøres i 4 timer ved 95-l06°C under tilbagesvaling efter tilsætning af 0,55 vægt% koncentreret HC1 (vf. 1,18), beregnet på alkylphenol. Derpå afde-30 stilleres vandet, til sidst under formindsket tryk ved ca. 20-2 mm Hg.A) Novolak preparation z + 1 mole of alkylphenol and Z mole of formaldehyde are mixed at room temperature and stirred for 4 hours at 95 -106 ° C under reflux after addition of 0.55% by weight of concentrated HCl (wf. 1.18), calculated on alkylphenol. . The water is then distilled off, finally under reduced pressure, at approx. 20-2 mm Hg.

b) Oxalkylering og sulforavsyrehalvesterpræparatfremstilling 1 mol novolak oxalkyleres med 0,2 vægt% NaOH, beregnet på 35 novolak, ved 140-170°C med n(z + 1) mol ethylenoxid ogb) Oxalkylation and sulphoric acid half ester preparation Preparation 1 mol of novolac is oxalkylated with 0.2% by weight NaOH, calculated on 35 novolac, at 140-170 ° C with n (z + 1) mol of ethylene oxide and

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7 forestres ved 50-80°C under omrøring med z + 1 eller færre mol maleinsyreanhydrid. Efter fortynding med vand indrøres ved 40-80°C og i løbet af 15-120 minutter 1,05-1,1 mol natriumsulfit som vandig opløsning, og der efterom-5 røres i 1 time, efter at blandingen er blevet klart vand opløselig. Mængden af det tilsatte vand kan andrage mellem 50 og 85 vægt% af slutopløsningen.7 is esterified at 50-80 ° C with stirring with z + 1 or fewer moles of maleic anhydride. After dilution with water, stir at 40-80 ° C and for 15-120 minutes 1.05-1.1 moles of sodium sulfite as aqueous solution and stir for 1 hour after the mixture has become clear water soluble. . The amount of water added can be between 50 and 85% by weight of the final solution.

Ved denne fremgangsmåde fremstilles substanserne i nedenstående tabel.In this process, the substances are prepared in the table below.

10 15 20 25 30 3510 15 20 25 30 35

g DK 152512 Bg DK 152512 B

nn

0 O0 O

ti) tMH N fO Ol cm M 0 ** * *- *· cd r* g ot ro 01 2ti) tMH N fO Ol cm M 0 ** * * - * · cd r * g ot ro 01 2

β Iβ I

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0) >1 £ +J vorirli—10)> £ 1 + J vorirli — 1

51 » S (ί (TiririO51 »S {ί (TiririO

[>) il tJ tH i—I H[>) il tJ tH i — I H

ω __J____-___-·ω __J ____-___- ·

£ 00 CM ri H£ 00 CM ri H

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DK 152512BDK 152512B

I nedenstående eksempler beskrives fremstillingen af pigmentpræparater til vandige flexotrykfarver på basis af sulforavsyrehalvesterpræparater som fordelingsmidler.In the examples below, the preparation of pigment preparations for aqueous flexo printing inks based on sulphuric acid halves preparations is described as distribution agents.

5 Eksempel 1 125 vægtdele af det ved kobling af diazoteret 3,3'--dichlorbenzidin på aceteddikeanilid fremstillede azofar-vestof (Pigment Gul 12, Colour Index Nr. 21090) æltes sejt i ca. 1 time med 54 vægtdele af en 35 vægt%-holdig vandig 10 opløsning af sulforavsyrehalvesterpræparat nr. 2 i tabellen i et ælteapparat med dobbelttrug. Efter endt finfordeling fortyndes der ved tilsætning af 60 vægtdele ethylenglycol og 11 vægtdele vand. Det 55 vægt%-holdige tyndtflydende pigmentpræparat kan i hvert forhold indstilles med vandige 15 flexotrykfernisser, f.eks. forsæbede shellakker, forsæbede polyvinylacetater, og ved simpel omrøring til en flexotryk-farve.EXAMPLE 1 125 parts by weight of the azofar vest fabric prepared by coupling diazotized 3,3 '- dichlorobenzidine on acetacetic anilide (Pigment Yellow 12, Color Index No. 21090) was kneaded hard for approx. 1 hour with 54 parts by weight of a 35 wt.% Aqueous solution of sulfuric acid half ester preparation # 2 in the table in a double trough kneading apparatus. After finishing the distribution, dilute 60 parts by weight of ethylene glycol and 11 parts by weight of water. The 55% by weight thin liquid pigment composition can be adjusted in each ratio with aqueous 15 flexo printing variants, e.g. saponified shellacs, saponified polyvinyl acetates, and by simple stirring to a flexo color.

Eksempel 2 20 200 vægtdele af et Cu-phthalocyaninpigment (PigmentExample 2 20 200 parts by weight of a Cu-phthalocyanine pigment (Pigment

Blå 15, Colour Index Nr. 74160) æltes sejt i ca. 3 timer med 100 vægtdele af en 30 vægt%-holdig vandig opløsning af sulforavsyrehalvesterpræparat nr. 1 i tabellen i et ælteapparat med dobbelttrug under tilsætning af 10 vægtdele di-25 -naphthoylmethan-disulfonat. Ved påfølgende fortynding med 80 vægtdele ethylenglycol og 10 vægtdele vand fås en strømmedygtig dej med 50 vægt% pigment.Blue 15, Color Index no. 74160) knead cool for approx. 3 hours with 100 parts by weight of a 30% by weight aqueous solution of sulphuric acid half ester preparation in the table in a double-trough kneader with the addition of 10 parts by weight of di-25-naphthoylmethane disulfonate. By subsequent dilution with 80 parts by weight of ethylene glycol and 10 parts by weight of water, a flowable dough with 50% by weight pigment is obtained.

Eksempel 3 30 57 vægtdele af et azopigment med lakegenskaber (Pig ment Rød 53, Colour Index Nr. 15585 Lake) formales i 27 vægt-dele af en 35%'s vandig opløsning af sulforavsyrehalvesterpræparat nr. 2, 20 vægtdele ethylenglycol og 38,5 vægtdele vand i 2 timer i en 1 liters laboratorieperlemølle under 35 tilsætning af ca. 600 vægtdele sili-kvartsit-perler (2-3 mmEXAMPLE 3 57 57 parts by weight of an azo pigment with lacquer properties (Pigment Red 53, Color Index No. 15585 Lake) are milled in 27 parts by weight of a 35% aqueous solution of sulphuric acid halide preparation # 2, 20 parts by weight of ethylene glycol and 38.5 parts by weight of water for 2 hours in a 1 liter laboratory bead mill during the addition of approx. 600 parts by weight of silica-quartzite beads (2-3 mm

DK 152512BDK 152512B

10 o i diameter) som formalingslegemer. Efter endt formaling fra-suges formalingslegemerne over en sigte, og der fås en hældbar pigmentdispersion med et pigmentindhold på 40 vægt%.10 o in diameter) as grinding bodies. Upon completion of grinding, the grinding bodies are extracted over a sieve and a pourable pigment dispersion having a pigment content of 40% by weight is obtained.

5 Eksempel 4 Når man dispergerer 312 vægtdele af Pigment Rød 14 (Colour Index Nr. 12380) med 102 vægtdele af en 40 vægt%-hol-dig vandig opløsning af sulforavsyrehalvesterpræparat nr. 3 under tilsætning af 6 vægtdele dinaphthoylmethan-disulfonat 10 som angivet i eksempel 1 og derpå fortynder med 120 vægtdele ethylenglycol og 60 vægtdele vand til et pigmentindhold på 52 vægt%, fremkommer der et strømmedygtigt, skumfattigt pigmentpræparat, der er egnet til fremstilling af flexotryk-farver.Example 4 When dispersing 312 parts by weight of Pigment Red 14 (Color Index No. 12380) with 102 parts by weight of a 40% by weight aqueous solution of sulphuric acid half ester preparation # 3 with the addition of 6 parts by weight of dinaphthoylmethane disulfonate 10 as set forth in Example 1 and then diluting with 120 parts by weight of ethylene glycol and 60 parts by weight of water to a pigment content of 52% by weight, a flowable, foam-poor pigment composition suitable for the production of flexo inks is obtained.

1515

Eksempel 5 75 vægtdele af det pigment, der er fremkommet ved blandingskobling af diazoteret 3,3'-dichlorbenzidin på acet-eddike-anilid og aceteddike-p-anisidid i forholdet 9:1, æl-20 tes sejt med 40,5 vægtdele af en 35 vægt%-holdig vandig opløsning af sulforavsyrehalvesterpræparat nr. 4 i tabellen i ca. 2 timer i et ælteapparat med dobbelttrug. Efter endt finfordeling fortyndes der ved tilsætning af 30 vægtdele ethylenglycol og 4,5 vægtdele vand, og der fås en strømme-25 dygtig dej, der indeholder 50 vægt% pigment.Example 5 75 parts by weight of the pigment obtained by mixing coupling of diazotized 3,3'-dichlorobenzidine to acetate-acetic anilide and acetate-acetic acid p-anisidide in a ratio of 9: 1, was eluted with 40.5 parts by weight of a 35% by weight aqueous solution of sulfuric acid half ester preparation # 4 in the table for about 1 hour. 2 hours in a double trough kneading machine. After finishing finely, 30 parts by weight of ethylene glycol and 4.5 parts by weight of water are diluted and a flowable dough containing 50% by weight pigment is obtained.

30 3530 35

Claims (3)

1. Sulforavsyrehalvesterpræparat til anvendelse som dispergeringsmiddel i pigmentpræparater til vandige flexo-5 trykfarver, kendetegnet ved, at det består af en blanding af forbindelser med den almene formel ~B - (0 - X) - 0 Ί 0 - (X - 0) - A . J_V-r-iS yj ve R J z R 15 hvor A betyder en gruppe med formlen -CO-CH^-CH-COOMe eller S03Me -CO-CH-CI^-COOMe, B betyder et hydrogenatom og/eller fortrins-S03Me vis en gruppe med betydningen af A, X betyder en ethylen- el-20 ler propylengruppe, R betyder en mættet alkylgruppe med 6-14 carbonatomer, Me betyder et hydrogenatom, et alkalimetalatom eller et ækvivalent jordalkalimetalatom, n er et tal fra 2 til 25, og z er et tal fra 1 til 9.1. Sulfuric acid half ester composition for use as a dispersant in pigment preparations for aqueous flexo printing inks, characterized in that it consists of a mixture of compounds of the general formula ~ B - (0 - X) - 0 Ί 0 - (X - 0) - A. J is a group of the formula -CO-CH 2 -CH-COOMe or SO 3 Me -CO-CH-Cl 2 -COOMe, B represents a hydrogen atom and / or preferably-SO 3 Me a group having the meaning of A, X means an ethylene or 20 propylene group, R means a saturated alkyl group having 6-14 carbon atoms, Me means a hydrogen atom, an alkali metal atom or an equivalent alkaline earth metal atom, n is a number from 2 to 25, and z is a number from 1 to 9. 2. Fremgangsmåde til fremstilling af et sulforavsyre halvesterpræparat ifølge krav 1, og bestående af en blanding af forbindelser med den almene formel "B - (O - X)n - 0 0 - (X - 0)n - A 30 1 1 H-J----jiV-CH2----fj-^j (I) W vr R _ z R 35 O DK 152512 B hvor A betyder en gruppe med formlen -CO-C^-CH-COOMe eller S03Me -CO-CH-C^-COOMe, B betyder et hydrogenatom og/eller for sone 5 trinsvis en gruppe med betydningen A, X betyder en ethylen-eller propylengruppe, R betyder en mættet alkylgruppe med 6-14 carbonatomer, Me betyder et hydrogenatom, et alkalimetalatom eller et ækvivalent jordalkalimetalatom, n er et tal fra 2 til 25, og z er et tal fra 1 til 9, kende-10 tegnet ved, at man oxethylerer eller oxpropylerer fler-kernede alkylphenoler med formlen OH Ί OH Ar ÅA process for preparing a sulfuric acid half-ester composition according to claim 1, and comprising a mixture of compounds of the general formula "B - (O - X) n - 0 0 - (X - 0) n - A 30 1 1 HJ- --- jiV-CH2 ---- fj- ^ j (I) W vr R _ z R 35 O DK 152512 B where A means a group of the formula -CO-C ^ -CH-COOMe or SO3Me -CO-CH -C 2 -COOMe, B means a hydrogen atom and / or for zone 5, preferably a group with the meaning of A, X means an ethylene or propylene group, R means a saturated alkyl group of 6-14 carbon atoms, Me means a hydrogen atom, an alkali metal atom or an equivalent alkaline earth metal atom, n is a number from 2 to 25, and z is a number from 1 to 9, characterized by oxethylating or oxpropylating multi-core alkyl phenols of the formula OH Ί OH Ar Å 15 H--fr 4—«2--frj (II) / Αχν*\ R _ z R hvor R og z har den ovenfor anførte betydning, omsætter de 20 på denne måde fremkomne oxethylater eller oxpropylater med maleinsyreanhydrid til maleinsyrehalvesterne og sætter alkalimetal- eller jordalkalimetalsulfiter til disse. 25 30 35H - fr 4 - «2 - fr (II) / Αχν * \ R _ z R where R and z have the meaning given above, the 20 thus obtained oxethylates or oxpropylates with maleic anhydride react to the maleic halves and add the alkali metal - or alkaline earth metal sulphites for these. 25 30 35
DK325472A 1971-06-30 1972-06-29 SULPHORIC ACID HALVESTER PREPARATIONS USED AS DISPERSIBLE IN PIGMENT PREPARATIONS FOR Aqueous FLEXOTRY COLORS AND PROCEDURES FOR ITS PREPARATION DK152512C (en)

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DE19712132404 DE2132404B2 (en) 1971-06-30 1971-06-30 Use of sulfosuccinic acid half-esters in pigment preparations for aqueous flexographic printing inks
DE2132404 1971-06-30

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2901461A1 (en) 1979-01-16 1980-07-24 Hoechst Ag USE OF OXALKYLATED NOVOLAC RESIN AS A PREPARATION AGENT FOR DISPERSION DYES AND PREPARATIONS THEREFORE
DE2901462A1 (en) * 1979-01-16 1980-07-31 Hoechst Ag PIGMENT DISPERSIONS AND THEIR USE
DE102012018544A1 (en) * 2012-09-19 2014-03-20 Clariant International Ltd. Derivatives of sulfosuccinic acid as a dispersant in binder-free pigment preparations

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3320212A (en) * 1962-05-03 1967-05-16 Petrolite Corp alpha-sulfocarboxylic esters of oxyalkylated polyphenols
GB1108410A (en) * 1966-10-19 1968-04-03 Witco Chemical Corp Production of oil-soluble salts of sulfopolycarboxylic acid esters of alkylene oxide adducts

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3320212A (en) * 1962-05-03 1967-05-16 Petrolite Corp alpha-sulfocarboxylic esters of oxyalkylated polyphenols
GB1108410A (en) * 1966-10-19 1968-04-03 Witco Chemical Corp Production of oil-soluble salts of sulfopolycarboxylic acid esters of alkylene oxide adducts

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FR2144414A5 (en) 1973-02-09
DE2132404C3 (en) 1975-12-18
GB1395781A (en) 1975-05-29
BE785705A (en) 1973-01-02
AU464488B2 (en) 1975-08-28
DE2132404B2 (en) 1975-04-10
DE2132404A1 (en) 1973-02-15
CA1007806A (en) 1977-04-05
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BR7204253D0 (en) 1973-06-28
CH572902A5 (en) 1976-02-27
AU4397972A (en) 1974-01-03

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