EP0645429A1 - Water-in-oil thickening dispersions, process for their preparation and their use in textile printing - Google Patents

Water-in-oil thickening dispersions, process for their preparation and their use in textile printing Download PDF

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Publication number
EP0645429A1
EP0645429A1 EP94402088A EP94402088A EP0645429A1 EP 0645429 A1 EP0645429 A1 EP 0645429A1 EP 94402088 A EP94402088 A EP 94402088A EP 94402088 A EP94402088 A EP 94402088A EP 0645429 A1 EP0645429 A1 EP 0645429A1
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Prior art keywords
water
oil
polymer
weight
designated
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EP94402088A
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German (de)
French (fr)
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EP0645429B1 (en
Inventor
Paul Mallo
Isabelle Fietier
Ulrich Karsunky
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Clariant Finance BVI Ltd
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Francaise Hoechst Ste
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Classifications

    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06PDYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
    • D06P1/00General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed
    • D06P1/44General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed using insoluble pigments or auxiliary substances, e.g. binders
    • D06P1/46General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed using insoluble pigments or auxiliary substances, e.g. binders using compositions containing natural macromolecular substances or derivatives thereof
    • D06P1/48Derivatives of carbohydrates
    • D06P1/50Derivatives of cellulose
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06PDYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
    • D06P1/00General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed
    • D06P1/44General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed using insoluble pigments or auxiliary substances, e.g. binders
    • D06P1/52General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed using insoluble pigments or auxiliary substances, e.g. binders using compositions containing synthetic macromolecular substances
    • D06P1/5207Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds
    • D06P1/525Polymers of unsaturated carboxylic acids or functional derivatives thereof
    • D06P1/5257(Meth)acrylic acid

Definitions

  • the present application relates to water-in-oil thickening dispersions, their preparation process and their application in textile printing.
  • compositions which can be used in the printing of textiles with reactive solvents, stable, miscible with water and leading to good quality prints with good color rendering, a pleasant touch and very satisfying unison.
  • compositions according to the invention are water-in-oil dispersions, stable, self-reversible, water-miscible, consisting of an oil phase, an aqueous phase and at least two emulsifying agents, at least one of which is of the water in oil type, and at least one is of the oil in water type, characterized in that they contain from 20 to 50% by weight of a mixture consisting of a polymer anionic, water-soluble, belonging to the group of carboxymethylcelluloses, designated C, and by a synthetic anionic polymer, crosslinked, insoluble in water but swellable with water, designated P, based on acrylic acid, designated AA, partially salified with an alkali metal, designated M, optionally copolymerized with 2-acrylamide-2-methyl-propanesulfonate M, designated AMPSM, crosslinked with a diethylenic carboxylic acid and in which the molar ratio of the salified acid functions to all of the functions free or salified acids is between approximately 0.6 and approximately 0.9, the
  • alkali metal M denotes sodium or potassium. Thereafter, acrylic acid is designated AA, its alkali metal salt AAM, its sodium salt AANa, and its potassium salt AAK, 2-acrylamido-2-methylpropanesulfonic acid is designated AMPS, its metal salt alkaline AMPSM, its sodium salt AMPSNa and its potassium salt AMPSK.
  • diethylenic carboxylic acid designates a crosslinking monomer, designated R, polymerizable with acrylic acid and having a carboxyl function and two ethylenic functions such as bisacrylamidoacetic acid. designated ABAA, diallyloxyacetic acid, designated DALLA.
  • water-in-oil type emulsifier is meant emulsifiers having an HLB value (hydrophilic-lipophilic balance, Kirk-Othmer, Encyclopedia of Chemical Technology, 3rd edition, volume 8, page 910) sufficiently low to provide water in oil emulsions such as sorbitan esters such as sorbitan sesquioleates, sorbitan monooleate.
  • HLB value hydrophilic-lipophilic balance
  • oil-in-water type emulsifier emulsifiers having an HLB value high enough to provide oil-in-water emulsions such as ethoxylated nonylphenols, sorbitan esters ethoxylated like sorbitan hexaoleate ethoxylated with 50 moles of ethylene oxide.
  • crosslinked polymer is meant a non-linear polymer in the state of a three-dimensional network insoluble in water but swellable in water.
  • TYLOSE® C 1000 designates a sodium carboxymethylcellulose having, under the conditions defined above, an average viscosity of 1000 mPa.s.
  • a carboxymethylcellulose is used in the form of a fine powder.
  • compositions as defined above characterized in that they contain from 20 to 50% by weight of a mixture of anionic polymers consisting of 10 to 50% by weight of a carboxymethylcellulose , C, and with 90 to 50% by weight of a crosslinked polymer, P, AA-AAM-AMPSM containing in molar proportions from 0 to 30% of AMPSM and from 100 to 70% of a mixture AA and AAM containing in molar proportions of 20 to 40% of AA and of 80 to 60% of AAM, crosslinked with from 0.01 to 0.06% in molar proportions relative to the monomers used, of a selected diethylenic carboxylic acid in the group made up of ABAA and DALLA.
  • the subject of the invention is in particular the compositions as defined above in which the polymer P is crosslinked by ABAA.
  • compositions of the invention contain from 10 to 20% by weight of a sodium carboxymethylcellulose and from 20 to 30% by weight of a polymer P, as defined above.
  • compositions according to the invention generally contain from 2 to 10% by weight of a mixture of emulsifying agents, and advantageously from 3 to 8% by weight relative to the total weight of the composition, of which 40 to 60% are constituted by one several emulsifying agents of the water in oil type and 60 to 40% are constituted by one several emulsifying agents of the oil in water type.
  • the oil phase of the compositions represents from 15 to 35% by weight, and advantageously from 20 to 25% by weight relative to the total weight of the composition.
  • This oil phase consists of a commercial mineral oil containing saturated hydrocarbons of the paraffinic, isoparaffinic, naphthenic or cycloparaffinic type, having a density at 15 ° C. of about 0.7 to about 0.9 and a boiling point greater than 180 ° C, such as white oils marketed by the company SHELL or ISOPAR®, marketed by the company EXXON.
  • compositions according to the invention contain from 25 to 60% of water in which the mixture of polymer P is partially soluble.
  • the compositions according to the invention can also contain various additives such as chelating agents, transfer agents.
  • the compositions according to the invention contain from 0.01 to 0.10% by weight of a chelating agent, and advantageously from 0.02 to 0.5% by weight relative to the total weight of the composition of sodium diethylenetriaminepentaacetate, designated DTPANa.
  • the invention also relates to a process for the preparation of the compositions defined above.
  • compositions defined above can be prepared by a process characterized in that a radical polymerization reaction is carried out in water-in-oil emulsion, starting from an aqueous solution containing the monomers constituting the polymer P , and optionally a chelating agent, which is emulsified in an oil phase in the presence of one or more emulsifying agents of the water in oil type, the polymerization reaction being initiated by the introduction into the starting emulsion of a generating product.
  • a radical polymerization reaction is carried out in water-in-oil emulsion, starting from an aqueous solution containing the monomers constituting the polymer P , and optionally a chelating agent, which is emulsified in an oil phase in the presence of one or more emulsifying agents of the water in oil type, the polymerization reaction being initiated by the introduction into the starting emulsion of a generating product.
  • azo derivatives such as azobisisobutyronitrile, designated AIBN
  • a Redox couple such as the cumene hydroperoxide couple - sodium disulfite
  • the polymerization reaction is carried out with stirring, in an inert atmosphere, from a perfectly deoxygenated reaction medium.
  • compositions according to the invention have interesting rheological properties which are demonstrated by determining, with a rheometer of the BOHLIN VOR type, the complex module, G *, the conservation module (storage modulus) G ', the angle of loss (loss angle), ⁇ , of aqueous media containing them.
  • printing pastes containing reactive dyes.
  • the following tables mention the various rheological characteristics as well as the properties of the fabrics printed with printing pastes obtained from the compositions according to the invention.
  • These printing pastes are obtained by mixing 40 g of red RB 25 REMAZOL® sold by the applicant, 10 g of sodium hydrogencarbonate, 50 g of urea, the necessary amount of a dispersion according to the invention to provide 10 , 6 g of mixture of anionic polymers and the necessary amount of water to obtain 500 g of printing paste (the printing paste consequently contains 2.12% by weight of mixture of anionic polymers).
  • the reference printing paste is prepared by mixing 40 g of RB 25 REMAZOL® red, 10 g of sodium hydrogen carbonate, 50 g of urea, 15 g of sodium alginate and the necessary amount of water. to obtain 500 g of printing paste.
  • This aqueous solution is homogenized in an oil phase containing 250 g of SHELL S 8515 oil and 25 g of sorbitan sesquioleate for 20 minutes with a SILVERSON mixer so as to obtain a water-in-oil emulsion having a Brookfield viscosity of 3,500 mPa. s. determined at 10 ° C (axis 2, speed 20 rpm, LVT model).
  • the emulsion thus obtained is transferred to a polymerizer, then it is deoxygenated by a bubbling of nitrogen and its temperature is adjusted to approximately 8 ° C.
  • the polymerization is started with stirring by the introduction over 2 minutes of 0.009 g (0.0473 mmol) of 80% cumene hydroperoxide (ie 20 molar ppm relative to the monomers) dissolved in 8 g of oil S 8515, then after 4 minutes, by the introduction in 40 minutes of 0.0136 g (0.0715 mmol) of sodium disulfite dissolved in 20 g of water, ie 30 ppm molar with respect to the monomers.
  • the polymerization starts at the temperature of the reaction medium rises to 55 ° C, a temperature which is then maintained for 1 hour.
  • reaction medium is then gradually cooled.
  • 20 g of ethoxylated nonylphenol with 10 moles of ethylene oxide are introduced (at this stage, the dispersion obtained is designated D21), then at 20 ° C., 117.6 g of carboxymethylcellulose (TYLOSE) are introduced ® C 1000 - HOECHST).
  • An aqueous solution is prepared containing 220 g (3.053 mole) of acrylic acid, 0.9 g of an aqueous solution containing 0.36 g (0.715 mmol) of sodium diethylenetriaminepentaacetate, 0.109 g (0.55 mmol) of bisacrylamidoacetic acid, 85.5 g (2.137 mole) sodium hydroxide and 393.5 g water.
  • This aqueous solution is homogenized in an oil phase containing 250 g of SHELL S 8515 oil and 25 g of sorbitan sesquioleate as in Example 1, then the emulsion obtained is polymerized as in Example 1, using one part 0.0348 g (0.183 mmol) of 80% cumene hydroperoxide dissolved in 8 g of oil S 8515, i.e. 60 molar ppm relative to the monomers and 0.029 g (0.153 mmol) of sodium disulfite dissolved in 20 g of water, ie 50 molar ppm relative to the monomers.
  • d '' a stable, self-reversible, water-miscible, water-in-oil dispersion containing 22.62% oil, 3.94% surfactants, 39.7% water and 33.73% of a mixture of anionic polymers containing by weight 30.57% of carboxymethylcellulose and 69.43% of an AA-AANa copolymer, 30 - 70 in molar proportions, crosslinked with 180 molar ppm of ABAA.
  • This dispersion is designated D2 and its rheological and applicative characteristics are mentioned in the following tables.
  • TYLOSE® C 1000 is replaced by TYLOSE® C 300, the dispersion designated D32 is obtained.
  • An aqueous solution is prepared containing 165.25 g (2.2932 moles) of acrylic acid, 52.79 g (0.2547 moles) of 2-acrylamido-2-methylpropanesulfonic acid, 104.25 (1.858 moles) d potassium hydroxide, 0.9 g of an aqueous solution containing 0.36 g (0.751 mmol) of sodium diethylenetriaminepentaacetate, 0.151 g (0.7619 mmol) of bisacrylamidoacetic acid and 386.7 g of water.
  • Example 2 is reproduced, starting from an aqueous solution containing 220 g (3.053 mole) of acrylic acid, 0.9 g of an aqueous solution containing 0.36 g (0.715 mole) of sodium diethylenetriaminepentaacetate, 0.109 g (0.550 mmol) bisacrylamidoacetic acid, 73.27 g (1.832 mole) sodium hydroxide and 405.7 g water.
  • 1140.6 g of a stable, self-reversible dispersion, miscible with water, water in oil, containing 22.62% of oil, 3.94% of surfactants, 40.31% of water are thus obtained.
  • Example 1 is reproduced, using on the one hand 0.012 g (0.565 mmol) of ABAA (240 molar ppm relative to the monomers), and on the other hand an aqueous phase containing a total of 424 g of water instead of 432 g.
  • Example 2 is reproduced, using on the one hand, 0.145 g (0.7316 mmol) of ABAA (240 ppm molar relative to the monomers) and on the other hand an oil phase containing 225 g of oil S 8515 and 22.5 g of sorbitan sesquioleate. Is thus obtained after addition of 114.5 g of TYLOSE® C 1000, 1110 g of a dispersion designated D6, the intermediate dispersion before the introduction of the carboxymethylcellulose is designated D26. In another test, 229 g of TYLOSE® C 1000 are introduced into the dispersion D26 and 1224.5 g of a dispersion designated D46 is obtained. The rheological and application characteristics of these dispersions are mentioned in the following tables.
  • Table III shows that the printing pastes produced with the compositions of the invention have application properties greater than or equal to those obtained by the use of printing pastes prepared either conventionally with sodium alginate, or only with synthetic polymers based on acrylic acid.
  • TABLE III Rheology Print specifications No. G * (Pa) ⁇ (°) To Re A Ref 7 85 3 3 3 From 56 10 3 3 3 From 12 37 3 4 3 From 16 28 3 3 3 From 7 44 3 5 3 From 6 50 From From From 8 37 3 4 3 From 16 29 3 4 3 From 6 73 3 3 3 3 3 From 4 70 3 5 3 From 86 12 From 12 38 3 4 3 From 13 40 3 4 3 From 10 42 3 3 3 From 7 52 3 4 3 From 5 56 3 5 3

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Abstract

Stable, autoreversible, water-miscible water-in-oil dispersions consisting of an oil phase, an aqueous phase and at least two emulsifying agents at least one of which is of water-in-oil type and at least one is of oil-in-water type, which contain from 20 to 50 % by weight of a mixture consisting of a water-soluble anionic polymer belonging to the group of carboxymethyl celluloses (C) and of a crosslinked synthetic anionic polymer which is insoluble in water but swellable with water (P), based on acrylic acid (AA) partially converted into salt with an alkali metal (M), optionally copolymerised with 2-acrylamido-2-methylpropanesulphonate of alkali metal M (AMPSM), crosslinked with a diethylenic carboxylic acid, and in which the molar ratio of the acidic functional groups converted into salt to the total of the acidic function groups which are free or converted into salt is between approximately 0.6 and approximately 0.9, the weight ratio C/P+C being between 0.01 and 0.4, process for their preparation and use for obtaining a printing paste.

Description

La présente demande concerne des dispersions eau dans huile épaississantes, leur procédé de préparation et leur application en impression textile.The present application relates to water-in-oil thickening dispersions, their preparation process and their application in textile printing.

Dans l'industrie textile, les tissus imprimés connaissent actuellement un développement important. Ils sont généralement obtenus par des techniques d'impression utilisant notamment des pâtes d'impression contenant soit des pigments, soit des colorants réactifs et présentant des propriétés rhéologiques bien définies en fonction de l'article souhaité et du type de colorant utilisé. Ces propriétés rhéologiques sont obtenues par l'emploi d'agents épaississants. Si dans l'impression pigmentaire, il est connu depuis quelques années d'utiliser des épaississants polymériques synthétiques à base d'acide acrylique (demandes de brevet européen N° 161 038, 169 674, 186 361, 197 635, 325 065 et 343 840) l'impression par colorant réactif plus délicate à mettre en oeuvre, réalisée dans des milieux très alcalins en présence d'une forte concentration en électrolyte, exige l'emploi d'épaississants particuliers issus de produits naturels tels que l'alginate de sodium ou des gommes de guar avec tous les inconvénients inhérents à ce type de produits naturels : fluctuation des cours, difficultés d'approvisionnement, variations des qualités.In the textile industry, printed fabrics are currently experiencing significant development. They are generally obtained by printing techniques using in particular printing pastes containing either pigments or reactive dyes and having well-defined rheological properties according to the article desired and the type of dye used. These rheological properties are obtained by the use of thickening agents. If in pigment printing, it has been known for a few years to use synthetic polymeric thickeners based on acrylic acid (European patent applications No. 161 038, 169 674, 186 361, 197 635, 325 065 and 343 840 ) printing by reactive dye, which is more difficult to implement, carried out in very alkaline media in the presence of a high concentration of electrolyte, requires the use of special thickeners derived from natural products such as sodium alginate or guar gums with all the drawbacks inherent in this type of natural product: price fluctuations, supply difficulties, variations in quality.

Afin d'obvier à ces inconvénients, la demanderesse a découvert des compositions épaississantes, utilisables dans l'impression des textiles avec des solvants réactifs, stables, miscibles à l'eau et conduisant à des impressions de bonne qualité avec un bon rendu coloristique, un toucher agréable et un unisson très satisfaisant.In order to overcome these drawbacks, the applicant has discovered thickening compositions which can be used in the printing of textiles with reactive solvents, stable, miscible with water and leading to good quality prints with good color rendering, a pleasant touch and very satisfying unison.

Les compositions selon l'invention sont des dispersions eau dans huile, stables, autoréversibles, miscibles à l'eau, constituées par une phase huile, une phase aqueuse et au moins deux agents émulsifiants dont au moins un est de type eau dans huile, et au moins un est du type huile dans eau, caractérisées par le fait qu'elles contiennent de 20 à 50 % en poids d'un mélange constitué par un polymère anionique, hydrosoluble, appartenant au groupe des carboxyméthylcelluloses, désigné C, et par un polymère anionique synthétique, réticulé, insoluble dans l'eau mais gonflable à l'eau, désigné P, à base d'acide acrylique, désigné AA, partiellement salifié avec un métal alcalin, désigné M, éventuellement copolymérisé avec de l'acrylamido-2 méthyl-2 propanesulfonate de métal alcalin M, désigné AMPSM, réticulé avec un acide carboxylique diéthylénique et dans lequel le rapport molaire des fonctions acides salifiées sur l'ensemble des fonctions acides libres ou salifiées est compris entre environ 0,6 et environ 0,9, le rapport pondéral C/P+C étant compris entre 0,01 et 0,4.The compositions according to the invention are water-in-oil dispersions, stable, self-reversible, water-miscible, consisting of an oil phase, an aqueous phase and at least two emulsifying agents, at least one of which is of the water in oil type, and at least one is of the oil in water type, characterized in that they contain from 20 to 50% by weight of a mixture consisting of a polymer anionic, water-soluble, belonging to the group of carboxymethylcelluloses, designated C, and by a synthetic anionic polymer, crosslinked, insoluble in water but swellable with water, designated P, based on acrylic acid, designated AA, partially salified with an alkali metal, designated M, optionally copolymerized with 2-acrylamide-2-methyl-propanesulfonate M, designated AMPSM, crosslinked with a diethylenic carboxylic acid and in which the molar ratio of the salified acid functions to all of the functions free or salified acids is between approximately 0.6 and approximately 0.9, the C / P + C weight ratio being between 0.01 and 0.4.

L'expression "métal alcalin M" désigne le sodium ou le potassium. Par la suite, l'acide acrylique est désigné AA, son sel de métal alcalin AAM, son sel de sodium AANa, et son sel de potassium AAK, l'acide acrylamido-2 méthyl-2 propanesulfonique est désigné AMPS, son sel de métal alcalin AMPSM, son sel de sodium AMPSNa et son sel de potassium AMPSK.The expression "alkali metal M" denotes sodium or potassium. Thereafter, acrylic acid is designated AA, its alkali metal salt AAM, its sodium salt AANa, and its potassium salt AAK, 2-acrylamido-2-methylpropanesulfonic acid is designated AMPS, its metal salt alkaline AMPSM, its sodium salt AMPSNa and its potassium salt AMPSK.

L'expression "acide carboxylique diéthylénique" désigne un monomère de réticulation, désigné R, polymérisable avec l'acide acrylique et possédant une fonction carboxyle et deux fonctions éthyléniques tel que l'acide bisacrylamidoacétique,. désigné ABAA, l'acide diallyloxyacétique, désigné DALLA.The expression “diethylenic carboxylic acid” designates a crosslinking monomer, designated R, polymerizable with acrylic acid and having a carboxyl function and two ethylenic functions such as bisacrylamidoacetic acid. designated ABAA, diallyloxyacetic acid, designated DALLA.

Par "agent émulsifiant du type eau dans huile", on désigne des agents émulsifiants possédant une valeur HLB (hydrophile-lipophile balance, Kirk-Othmer, Encyclopedia of Chemical Technology, 3 ème édition, volume 8, page 910) suffisamment faible pour fournir des émulsions eau dans huile tels que les esters de sorbitan comme les sesquioléates de sorbitan, le monooléate de sorbitan.By "water-in-oil type emulsifier" is meant emulsifiers having an HLB value (hydrophilic-lipophilic balance, Kirk-Othmer, Encyclopedia of Chemical Technology, 3rd edition, volume 8, page 910) sufficiently low to provide water in oil emulsions such as sorbitan esters such as sorbitan sesquioleates, sorbitan monooleate.

Par "agent émulsifiant du type huile dans eau", on désigne des agents émulsifiants possédant une valeur HLB suffisamment élevée pour fournir des émulsions huile dans eau tels que les nonylphénols éthoxylés, les esters de sorbitan éthoxylés comme l'hexaoléate de sorbitan éthoxylé avec 50 moles d'oxyde d'éthylène.By "oil-in-water type emulsifier" is meant emulsifiers having an HLB value high enough to provide oil-in-water emulsions such as ethoxylated nonylphenols, sorbitan esters ethoxylated like sorbitan hexaoleate ethoxylated with 50 moles of ethylene oxide.

Par "polymère réticulé", on désigne un polymère non linéaire se présentant à l'état d'un réseau à trois dimensions insoluble dans l'eau mais gonflable à l'eau.By "crosslinked polymer" is meant a non-linear polymer in the state of a three-dimensional network insoluble in water but swellable in water.

L'expression "groupe des carboxyméthylcellulose" désigne les produits issus de la réaction de Williamson avec le chloroacétate de sodium sur une alcali-cellulose (cf Ullmann's Encyclopedia of Industrial Chemistry, 5 ème édition, volume A5, pages 477-488) tels que les produits commercialisés par la demanderesse sous la désignation de TYLOSE® C. Ces produits présentent une plage de viscosité de 100 à 4000 mPa.s. déterminée avec un viscomètre à chute de bille, HÖPPLER, à une température de 20°C, en solution à 2 % en poids dans l'eau. Ainsi la TYLOSE® C 1 000 désigne une carboxyméthylcellulose sodique présentant dans les conditions définies ci-dessus une viscosité moyenne de 1000 mPa.s.. Préférentiellement, on utilise une carboxyméthylcellulose à l'état de poudre fine.The expression “carboxymethylcellulose group” designates the products resulting from the reaction of Williamson with sodium chloroacetate on an alkali-cellulose (cf. Ullmann's Encyclopedia of Industrial Chemistry, 5th edition, volume A5, pages 477-488) such as products marketed by the applicant under the designation of TYLOSE® C. These products have a viscosity range from 100 to 4000 mPa.s. determined with a HÖPPLER drop ball viscometer, at a temperature of 20 ° C., in a 2% by weight solution in water. Thus TYLOSE® C 1000 designates a sodium carboxymethylcellulose having, under the conditions defined above, an average viscosity of 1000 mPa.s. Preferably, a carboxymethylcellulose is used in the form of a fine powder.

L'invention a plus particulièrement pour objet les compositions telles que définies ci-dessus caractérisées par le fait qu'elles contiennent de 20 à 50 % en poids d'un mélange de polymères anioniques constitués par 10 à 50 % en poids d'une carboxyméthylcellulose, C, et par 90 à 50 % en poids d'un polymère réticulé, P, AA-AAM-AMPSM contenant en proportions molaires de 0 à 30 % d'AMPSM et de 100 à 70 % d'un mélange AA et AAM contenant en proportions molaires de 20 à 40 % d'AA et de 80 à 60 % d'AAM, réticulé avec de 0,01 à 0,06 % en proportions molaires par rapport aux monomères mis en oeuvre, d'un acide carboxylique diéthylénique choisi dans le groupe constitué par l'ABAA et le DALLA.A more particular subject of the invention is the compositions as defined above, characterized in that they contain from 20 to 50% by weight of a mixture of anionic polymers consisting of 10 to 50% by weight of a carboxymethylcellulose , C, and with 90 to 50% by weight of a crosslinked polymer, P, AA-AAM-AMPSM containing in molar proportions from 0 to 30% of AMPSM and from 100 to 70% of a mixture AA and AAM containing in molar proportions of 20 to 40% of AA and of 80 to 60% of AAM, crosslinked with from 0.01 to 0.06% in molar proportions relative to the monomers used, of a selected diethylenic carboxylic acid in the group made up of ABAA and DALLA.

Parmi ces dernières compositions, l'invention a notamment pour objet les compositions telles que définies ci-dessus dans lesquelles le polymère P est réticulé par l'ABAA.Among these latter compositions, the subject of the invention is in particular the compositions as defined above in which the polymer P is crosslinked by ABAA.

Parmi ces dernières compositions, on peut citer plus particulièrement les compositions telles que définies ci-dessus dans lesquelles le polymère P est choisi parmi les polymères réticulés suivants :

  • AA-AAM-AMPSM, contenant en proportions molaires de 10 à 30 % d'AMPSM et de 90 à 70 % d'acide acrylique dont 60 à 80 % sont sous la forme d'un acrylate de métal alcalin.
  • AA-AAM, contenant en proportions molaires de 30 à 40 % en poids d'AA et de 70 à 60 % d'AAM.
Among these latter compositions, there may be mentioned more particularly the compositions as defined above in which the polymer P is chosen from the following crosslinked polymers:
  • AA-AAM-AMPSM, containing in molar proportions from 10 to 30% of AMPSM and from 90 to 70% of acrylic acid of which 60 to 80% are in the form of an alkali metal acrylate.
  • AA-AAM, containing in molar proportions 30 to 40% by weight of AA and 70 to 60% of AAM.

Préférentiellement, les compositions de l'invention contiennent de 10 à 20 % en poids d'une carboxyméthylcellulose sodique et de 20 à 30 % en poids d'un polymère P, tel que défini précédemment.Preferably, the compositions of the invention contain from 10 to 20% by weight of a sodium carboxymethylcellulose and from 20 to 30% by weight of a polymer P, as defined above.

Les compositions selon l'invention contiennent généralement de 2 à 10 % en poids d'un mélange d'agents émulsifiants, et avantageusement de 3 à 8 % en poids par rapport au poids total de la composition, dont 40 à 60 % sont constitués par un plusieurs agents émulsifiants du type eau dans huile et 60 à 40 % sont constitués par un plusieurs agents émulsifiants du type huile dans eau.The compositions according to the invention generally contain from 2 to 10% by weight of a mixture of emulsifying agents, and advantageously from 3 to 8% by weight relative to the total weight of the composition, of which 40 to 60% are constituted by one several emulsifying agents of the water in oil type and 60 to 40% are constituted by one several emulsifying agents of the oil in water type.

La phase huile des compositions représente de 15 à 35 % en poids, et avantageusement de 20 à 25 % en poids par rapport au poids total de la composition. Cette phase huile est constitué par une huile minérale commerciale contenant des hydrocarbures saturés du type paraffinique, isoparaffinique, naphténique ou cycloparaffinique, présentant une densité à 15°C d'environ 0,7 à environ 0,9 et un point d'ébullition supérieur à 180°C, telle que les huiles blanches commercialisées par la Société SHELL ou l'ISOPAR®, commercialisée par la Société EXXON.The oil phase of the compositions represents from 15 to 35% by weight, and advantageously from 20 to 25% by weight relative to the total weight of the composition. This oil phase consists of a commercial mineral oil containing saturated hydrocarbons of the paraffinic, isoparaffinic, naphthenic or cycloparaffinic type, having a density at 15 ° C. of about 0.7 to about 0.9 and a boiling point greater than 180 ° C, such as white oils marketed by the company SHELL or ISOPAR®, marketed by the company EXXON.

Les compositions selon l'invention contiennent de 25 à 60 % d'eau dans laquelle le mélange de polymère P est partiellement soluble. Les compositions selon l'invention peuvent contenir également divers additifs tels que des agents chélatants, des agents de transfert. Avantageusement, les compositions selon l'invention contiennent de 0,01 à 0,10 % en poids d'un agent chélatant, et avantageusement de 0,02 à 0,5 % en poids par rapport au poids total de la composition de diéthylènetriaminepentaacétate de sodium, désigné DTPANa.The compositions according to the invention contain from 25 to 60% of water in which the mixture of polymer P is partially soluble. The compositions according to the invention can also contain various additives such as chelating agents, transfer agents. Advantageously, the compositions according to the invention contain from 0.01 to 0.10% by weight of a chelating agent, and advantageously from 0.02 to 0.5% by weight relative to the total weight of the composition of sodium diethylenetriaminepentaacetate, designated DTPANa.

L'invention a également pour objet un procédé de préparation des compositions définies ci-dessus.The invention also relates to a process for the preparation of the compositions defined above.

Selon l'invention, les compositions définies ci-dessus peuvent être préparées par un procédé caractérisé en ce que l'on effectue une réaction de polymérisation radicalaire en émulsion eau dans huile, à partir d'une solution aqueuse contenant les monomères constitutifs du polymère P, et éventuellement un agent chélatant, qui est émulsionnée dans une phase huile en présence d'un ou plusieurs agents émulsifiants du type eau dans huile, la réaction de polymérisation étant amorcée par l'introduction dans l'émulsion de départ d'un produit générant des radicaux libres tel que les dérivés azoïques comme l'azobisisobutyronitrile, désigné AIBN, ou d'un couple Redox comme le couple hydroperoxyde de cumène - disulfite de sodium, puis, lorsque la réaction de polymérisation est terminée, que l'on introduit dans la dispersion obtenue, à une température inférieure à 30°C, un ou plusieurs agents émulsifiants du type huile dans eau et la quantité désirée de polymère anionique C.According to the invention, the compositions defined above can be prepared by a process characterized in that a radical polymerization reaction is carried out in water-in-oil emulsion, starting from an aqueous solution containing the monomers constituting the polymer P , and optionally a chelating agent, which is emulsified in an oil phase in the presence of one or more emulsifying agents of the water in oil type, the polymerization reaction being initiated by the introduction into the starting emulsion of a generating product. free radicals such as azo derivatives such as azobisisobutyronitrile, designated AIBN, or a Redox couple such as the cumene hydroperoxide couple - sodium disulfite, then, when the polymerization reaction is complete, which are introduced into the dispersion obtained, at a temperature below 30 ° C, one or more emulsifying agents of the oil in water type and the desired amount of anionic polymer C.

De manière classique, la réaction de polymérisation est.effectuée sous agitation, en atmosphère inerte, à partir d'un milieu réactionnel parfaitement désoxygéné.Conventionally, the polymerization reaction is carried out with stirring, in an inert atmosphere, from a perfectly deoxygenated reaction medium.

Dans des conditions préférentielles de mise en oeuvre de l'invention, le procédé ci-dessus décrit est réalisé de la manière suivante :

  • la polymérisation est amorcée par un couple Redox, à une température inférieure ou égale à 10°C, puis elle est conduite de manière quasi adiabatique jusqu'à une température supérieure ou égale à 60°C,
  • le couple Redox utilisé est le couple hydroperoxyde de cumène - disulfite de sodium, à la dose de 10 à 100 ppm molaire par rapport aux monomères d'hydroperoxyde de cumène et de 20 à 100 ppm molaire par rapport aux monomères de disulfite de sodium.
Under preferential conditions for implementing the invention, the process described above is carried out as follows:
  • the polymerization is initiated by a Redox couple, at a temperature less than or equal to 10 ° C., then it is carried out in an almost adiabatic manner up to a temperature greater than or equal to 60 ° C.,
  • the Redox couple used is the cumene hydroperoxide - sodium disulfite couple, at a dose of 10 to 100 ppm molar with respect to the cumene hydroperoxide monomers and from 20 to 100 ppm molar with respect to the sodium disulfite monomers.

Les compositions selon l'invention présentent d'intéressantes propriétés rhéologiques qui sont mises en évidence en déterminant, avec un rhéomètre du type BOHLIN VOR, le module complexe, G*, le module de conservation (storage modulus) G', l'angle de perte (loss angle), δ, de milieux aqueux les contenant.The compositions according to the invention have interesting rheological properties which are demonstrated by determining, with a rheometer of the BOHLIN VOR type, the complex module, G *, the conservation module (storage modulus) G ', the angle of loss (loss angle), δ, of aqueous media containing them.

Ces intéressantes propriétés justifient leur application dans l'industrie textile pour la préparation de pâtes d'impression contenant des colorants réactifs. Dans les tableaux suivants on mentionne les diverses caractéristiques rhéologiques ainsi que les propriétés des tissus imprimés avec des pâtes d'impression obtenues à partir des compositions selon l'invention. Ces pâtes d'impression sont obtenues en mélangeant 40 g de rouge RB 25 REMAZOL® commercialisé par la demanderesse, 10 g d'hydrogènocarbonate de sodium, 50 g d'urée, la quantité nécessaire d'une dispersion selon l'invention pour apporter 10,6 g de mélange de polymères anioniques et la quantité nécessaire d'eau pour obtenir 500 g de pâte d'impression (la pâte d'impression contient en conséquence 2,12 % en poids de mélange de polymères anioniques). La pâte d'impression de référence est préparée en mélangeant 40 g de rouge RB 25 REMAZOL®, 10 g d'hydrogèno-carbonate de sodium, 50 g d'urée, 15 g d'alginate de sodium et la quantité nécessaire d'eau pour obtenir 500 g de pâte d'impression.These interesting properties justify their application in the textile industry for the preparation of printing pastes containing reactive dyes. The following tables mention the various rheological characteristics as well as the properties of the fabrics printed with printing pastes obtained from the compositions according to the invention. These printing pastes are obtained by mixing 40 g of red RB 25 REMAZOL® sold by the applicant, 10 g of sodium hydrogencarbonate, 50 g of urea, the necessary amount of a dispersion according to the invention to provide 10 , 6 g of mixture of anionic polymers and the necessary amount of water to obtain 500 g of printing paste (the printing paste consequently contains 2.12% by weight of mixture of anionic polymers). The reference printing paste is prepared by mixing 40 g of RB 25 REMAZOL® red, 10 g of sodium hydrogen carbonate, 50 g of urea, 15 g of sodium alginate and the necessary amount of water. to obtain 500 g of printing paste.

Avec des pâtes d'impression, on imprime des tissus 100 % coton, puis on détermine visuellement sur les tissus imprimés, le toucher, désigné To, l'unisson, désigné Un, et le rendement coloristique, désigné Re. On détermine également les caractéristiques rhéologiques de ces pâtes avec un rhéomètre BOHLIN VOR à la température ambiante, sur une prise d'essai de 7,5 g, avec un cylindre coaxial C 25HS, dans les conditions suivantes :

  • (i) Flow oscillation (précisaillement à 1 000 s⁻¹ pendant 5 minutes, suivi d'une analyse dynamique pendant 0,5 s à 20 Hz) conditionnement de la pâte suivie d'une reprise de structure instantanée,
  • (ii) oscillation (analyse dynamique à 1Hz pendant 1 000 s), reprise de structure jusqu'à l'équilibre,
  • (iii) strain sweep test (analyse dynamique à 1Hz par balayage en déformation), détermination du domaine linéaire de viscoélasticité.
With printing pastes, we print 100% cotton fabrics, then we determine visually on the printed fabrics, the touch, designated To, the unison, designated Un, and the color yield, designated Re. We also determine the characteristics rheological of these pastes with a BOHLIN VOR rheometer at room temperature, on a 7.5 g test portion, with a coaxial cylinder C 25HS, under the following conditions:
  • (i) Flow oscillation (precision at 1000 s⁻¹ for 5 minutes, followed by dynamic analysis for 0.5 s at 20 Hz) conditioning of the dough followed by an immediate resumption of structure,
  • (ii) oscillation (dynamic analysis at 1Hz for 1000 s), resumption of structure until equilibrium,
  • (iii) strain sweep test (dynamic analysis at 1Hz by strain sweep), determination of the linear range of viscoelasticity.

Les exemples suivants illustrent l'invention sans toutefois la limiter.The following examples illustrate the invention without, however, limiting it.

EXEMPLE 1EXAMPLE 1

On prépare une solution aqueuse contenant :

  • 146 g (2,026 moles) d'acide acrylique,
  • 74,2 g (0,358 mole) d'acide acrylamido-2 méthyl-2 propanesulfonique,
  • 286,9 g d'une solution aqueuse contenant 96,6 g (1,776 mole) d'hydroxyde de potassium,
  • 0,9 g d'une solution aqueuse contenant 0,36 g (0,751 mmole) de diéthylènetriaminepentaacétate de sodium,
  • 0,142 g (0,715 mmole) d'acide bisacrylamidoacétique et
  • 191,8 g d'eau.
An aqueous solution is prepared containing:
  • 146 g (2.026 moles) of acrylic acid,
  • 74.2 g (0.358 mol) 2-acrylamido-2-methylpropanesulfonic acid,
  • 286.9 g of an aqueous solution containing 96.6 g (1.776 mole) of potassium hydroxide,
  • 0.9 g of an aqueous solution containing 0.36 g (0.751 mmol) of sodium diethylenetriaminepentaacetate,
  • 0.142 g (0.715 mmol) of bisacrylamidoacetic acid and
  • 191.8 g of water.

Cette solution aqueuse est homogénéisée dans une phase huile contant 250 g d'huile SHELL S 8515 et 25 g de sesquioléate de sorbitane pendant 20 minutes avec un mixer SILVERSON de manière à obtenir une émulsion eau dans huile présentant une viscosité Brookfield de 3 500 mPa.s. déterminée à 10°C (axe 2, vitesse 20 tr/mn, modèle LVT).This aqueous solution is homogenized in an oil phase containing 250 g of SHELL S 8515 oil and 25 g of sorbitan sesquioleate for 20 minutes with a SILVERSON mixer so as to obtain a water-in-oil emulsion having a Brookfield viscosity of 3,500 mPa. s. determined at 10 ° C (axis 2, speed 20 rpm, LVT model).

L'émulsion ainsi obtenue est transférée dans un polymériseur, puis elle est désoxygénée par un barbotage d'azote et sa température est ajustée à environ 8°C. La polymérisation est amorcée sous agitation par l'introduction en 2 minutes de 0,009 g (0,0473 mmole) d'hydroperoxyde de cumène à 80 % (soit 20 ppm molaire par rapport aux monomères) dissous dans 8 g d'huile S 8515, puis après 4 minutes, par l'introduction en 40 minutes de 0,0136 g (0,0715 mmole) de disulfite de sodium dissous dans 20 g d'eau, soit 30 ppm molaire par rapport au monomères. La polymérisation démarre à la température du milieu réactionnel s'élève jusqu'à 55°C, température que l'on maintient ensuite pendant 1 heure.The emulsion thus obtained is transferred to a polymerizer, then it is deoxygenated by a bubbling of nitrogen and its temperature is adjusted to approximately 8 ° C. The polymerization is started with stirring by the introduction over 2 minutes of 0.009 g (0.0473 mmol) of 80% cumene hydroperoxide (ie 20 molar ppm relative to the monomers) dissolved in 8 g of oil S 8515, then after 4 minutes, by the introduction in 40 minutes of 0.0136 g (0.0715 mmol) of sodium disulfite dissolved in 20 g of water, ie 30 ppm molar with respect to the monomers. The polymerization starts at the temperature of the reaction medium rises to 55 ° C, a temperature which is then maintained for 1 hour.

Le milieu réactionnel est ensuite refroidi progressivement. A 30°C, on introduit 20 g de nonylphénol éthoxylé avec 10 moles d'oxyde d'éthylène (à ce stade, la dispersion obtenue est désignée D₂₁), puis à 20°C, on introduit 117,6 g de carboxyméthylcellulose (TYLOSE® C 1 000 - HOECHST). On obtient ainsi 1 140,6 g d'une dispersion stable, autoréversible, miscible à l'eau, eau dans huile contenant pondéralement 37,9 % d'eau, 22,6 % d'huile, 3,95 % de tensioactifs et 35,6 % d'un mélange de polymères anioniques contenant pondéralement 29 % de carboxyméthylcellulose et 71 % d'un copolymère AA-AAK-AMPSK, 25,5 - 59,5 - 15 en proportions molaires, réticulé avec 300 ppm molaire d'ABAA. Cette dispersion est désignée D₁ et ses caractéristiques rhéologiques et applicatives sont mentionnées dans les tableaux suivants.The reaction medium is then gradually cooled. At 30 ° C., 20 g of ethoxylated nonylphenol with 10 moles of ethylene oxide are introduced (at this stage, the dispersion obtained is designated D₂₁), then at 20 ° C., 117.6 g of carboxymethylcellulose (TYLOSE) are introduced ® C 1000 - HOECHST). 1140.6 g of a stable, self-reversible, water-miscible, water-in-oil dispersion containing 37.9% water, 22.6% oil, 3.95% surfactants and 35.6% of a mixture of anionic polymers containing by weight 29% of carboxymethylcellulose and 71% of an AA-AAK-AMPSK copolymer, 25.5 - 59.5 - 15 in molar proportions, crosslinked with 300 ppm molar of ABAA. This dispersion is designated D₁ and its rheological and applicative characteristics are mentioned in the following tables.

EXEMPLE 2EXAMPLE 2

On prépare une solution aqueuse contenant 220 g (3,053 mole) d'acide acrylique, 0,9 g d'une solution aqueuse contenant 0,36 g (0,715 mmole) de diéthylènetriaminepentaacétate de sodium, 0,109 g (0,55 mmole) d'acide bisacrylamidoacétique, 85,5 g (2,137 mole) d'hydroxyde de sodium et 393,5 g d'eau.An aqueous solution is prepared containing 220 g (3.053 mole) of acrylic acid, 0.9 g of an aqueous solution containing 0.36 g (0.715 mmol) of sodium diethylenetriaminepentaacetate, 0.109 g (0.55 mmol) of bisacrylamidoacetic acid, 85.5 g (2.137 mole) sodium hydroxide and 393.5 g water.

Cette solution aqueuse est homogénéisée dans une phase huile contenant 250 g d'huile SHELL S 8515 et 25 g de sesquioléate de sorbitan comme dans l'exemple 1, puis l'émulsion obtenue est polymérisée comme dans l'exemple 1, en utilisant d'une part 0,0348 g (0,183 mmole) d'hydroperoxyde de cumène à 80 % dissous dans 8 g d'huile S 8515, soit 60 ppm molaire par rapport aux monomères et 0,029 g (0,153 mmole) de disulfite de sodium dissous dans 20 g d'eau, soit 50 ppm molaire par rapport aux monomères. En fin de réaction de polymérisation, dans le milieu réactionnel refroidi à 30°C, on introduit sous agitation 20 g de nonylphénol éthoxylé avec 10 moles d'oxyde d'éthylène. On obtient ainsi une dispersion désignée D₂₂, dans laquelle on introduit à la température ambiante, sous agitation comme dans l'exemple 1, 117,6 g de carboxyméthylcellulose (TYLOSE® C 1 000 - HOECHST).On obtient ainsi 1140,6 g d'une dispersion stable, autoréversible, miscible à l'eau, eau dans huile contenant pondéralement 22,62 % d'huile, 3,94 % de tensioactifs, 39,7 % d'eau et 33,73 % d'un mélange de polymères anioniques contenant pondéralement 30,57 % de carboxyméthylcellulose et 69,43 % d'un copolymère AA-AANa, 30 - 70 en proportions molaires, réticulé avec 180 ppm molaire d'ABAA. Cette dispersion est désignée D₂ et ses caractéristiques rhéologiques et applicatives sont mentionnées dans les tableaux suivants. Dans un autre essai, on remplace la TYLOSE® C 1 000 par de la TYLOSE® C 300, on obtient la dispersion désignée D₃₂.This aqueous solution is homogenized in an oil phase containing 250 g of SHELL S 8515 oil and 25 g of sorbitan sesquioleate as in Example 1, then the emulsion obtained is polymerized as in Example 1, using one part 0.0348 g (0.183 mmol) of 80% cumene hydroperoxide dissolved in 8 g of oil S 8515, i.e. 60 molar ppm relative to the monomers and 0.029 g (0.153 mmol) of sodium disulfite dissolved in 20 g of water, ie 50 molar ppm relative to the monomers. At the end of the polymerization reaction, in the reaction medium cooled to 30 ° C, 20 g of ethoxylated nonylphenol with 10 moles of ethylene oxide are introduced with stirring. A dispersion designated D désign is thus obtained in which 117.6 g of carboxymethylcellulose (TYLOSE® C 1000 - HOECHST) are introduced at room temperature, with stirring as in Example 1. 1140.6 g of d '' a stable, self-reversible, water-miscible, water-in-oil dispersion containing 22.62% oil, 3.94% surfactants, 39.7% water and 33.73% of a mixture of anionic polymers containing by weight 30.57% of carboxymethylcellulose and 69.43% of an AA-AANa copolymer, 30 - 70 in molar proportions, crosslinked with 180 molar ppm of ABAA. This dispersion is designated D₂ and its rheological and applicative characteristics are mentioned in the following tables. In another test, TYLOSE® C 1000 is replaced by TYLOSE® C 300, the dispersion designated D₃₂ is obtained.

EXEMPLE 3EXAMPLE 3

On prépare une solution aqueuse contenant 165,25 g (2,2932 moles) d'acide acrylique, 52,79 g (0,2547 mole) d'acide acrylamido-2 méthyl-2 propanesulfonique, 104,25 (1,858 mole) d'hydroxyde de potassium, 0,9 g d'une solution aqueuse contenant 0,36 g (0,751 mmole) de diéthylènetriaminepentaacétate de sodium, 0,151 g (0,7619 mmole) d'acide bisacrylamidoacétique et 386,7 g d'eau. Cette phase aqueuse d'un poids total de 710 g est homogénéisée dans une phase huile constituée par 240 g d'huile ISOPAR® M (d = 0,79, Eb = 206-250°C) et 24 g de sesquioléate de sorbitan comme dans l'exemple 1, puis l'émulsion obtenue est polymérisée comme dans l'exemple 1, en utilisant d'une part, 0,01 g (0,0525 mmole) d'hydroperoxyde de cumène à 80 % dissous dans 8 g d'huile ISOPAR® M, soit 20 ppm molaires par rapport aux monomères, et 0,0145 g (0,0763 mmole) de disulfite de sodium dissous dans 20 g d'eau, soit 30 ppm molaire par rapport aux monomères. En fin de réaction de polymérisation, dans le milieu réactionnel refroidi à 30°C, on introduit sous agitation 20 g de nonylphénol éthoxylé avec 10 moles d'oxyde d'éthylène. On obtient ainsi une dispersion désignée D₂₃, dans laquelle on introduit à la température ambiante, sous agitation, 117,5 g de TYLOSE® C 1 000. On obtient ainsi 1 139,5 g d'une dispersion stable, autoréversible, miscible à l'eau, eau dans huile, contenant pondéralement 21,76 % d'huile, 3,86 % de tensioactifs, 38,72 % d'eau et 35,66 % d'un mélange de polymères anioniques contenant pondéralement 28,9 % de carboxyméthylcellulose et 71,1 % d'un polymère AA-AAK-AMPSK, 27 - 63 - 10 en proportions molaires, réticulé avec 300 ppm molaire par rapport aux monomères d'ABAA. Cette dispersion est désignée D₃ et ses caractéristiques rhéologiques et applicatives sont mentionnées dans les tableaux suivants. Dans un autre essai, on remplace la TYLOSE® C 1 000 par de la TYLOSE® C 300, on obtient ainsi une dispersion désignée D₃₃.An aqueous solution is prepared containing 165.25 g (2.2932 moles) of acrylic acid, 52.79 g (0.2547 moles) of 2-acrylamido-2-methylpropanesulfonic acid, 104.25 (1.858 moles) d potassium hydroxide, 0.9 g of an aqueous solution containing 0.36 g (0.751 mmol) of sodium diethylenetriaminepentaacetate, 0.151 g (0.7619 mmol) of bisacrylamidoacetic acid and 386.7 g of water. This aqueous phase with a total weight of 710 g is homogenized in an oil phase consisting of 240 g of ISOPAR® M oil (d = 0.79, Eb = 206-250 ° C) and 24 g of sorbitan sesquioleate as in Example 1, then the emulsion obtained is polymerized as in Example 1, using on the one hand, 0.01 g (0.0525 mmol) of 80% cumene hydroperoxide dissolved in 8 g d ISOPAR® M oil, 20 ppm molar with respect to the monomers, and 0.0145 g (0.0763 mmol) of sodium disulfite dissolved in 20 g of water, or 30 ppm molar with respect to the monomers. At the end of the polymerization reaction, into the reaction medium cooled to 30 ° C., the following are introduced under stirring 20 g of ethoxylated nonylphenol with 10 moles of ethylene oxide. A dispersion designated D₂₃ is thus obtained, into which 117.5 g of TYLOSE® C 1000 are introduced at ambient temperature, with stirring. 1139.5 g of a stable, self-reversible dispersion miscible with water are thus obtained. , water in oil, containing 21.76% by weight of oil, 3.86% of surfactants, 38.72% of water and 35.66% of a mixture of anionic polymers containing 28.9% by weight of carboxymethylcellulose and 71.1% of a polymer AA-AAK-AMPSK, 27 - 63 - 10 in molar proportions, crosslinked with 300 ppm molar with respect to the ABAA monomers. This dispersion is designated D₃ and its rheological and applicative characteristics are mentioned in the following tables. In another test, TYLOSE® C 1000 is replaced by TYLOSE® C 300, a dispersion designated D₃₃ is thus obtained.

EXEMPLE 4EXAMPLE 4

On reproduit l'exemple 2, au départ d'une solution aqueuse contenant 220 g (3,053 mole) d'acide acrylique, 0,9 g d'une solution aqueuse contenant 0,36 g (0,715 mole) de diéthylènetriaminepentaacétate de sodium, 0,109 g (0,550 mmole) d'acide bisacrylamidoacétique, 73,27 g (1,832 mole) d'hydroxyde de sodium et 405,7 g d'eau. On obtient ainsi 1 140,6 g d'une dispersion stable, autoréversible, miscible à l'eau, eau dans huile, contenant pondéralement 22,62 % d'huile, 3,94 % de tensioactifs, 40,31 % d'eau et 33,13 % d'un mélange de polymères anioniques contenant pondéralement 31,12 % de carboxyméthylcellulose et 68,88 % d'un copolymère AA-AANa, 40 - 60 en proportions molaires, réticulé avec 240 ppm molaire par rapport aux monomères d'ABAA. Cette dispersion est désignée D₄ ; la dispersion intermédiaire obtenue avant l'introduction de la carboxyméthylcellulose est désignée D₂₄. Les caractéristiques rhéologiques et applicatives de ces dispersions sont mentionnées dans les tableaux suivants.Example 2 is reproduced, starting from an aqueous solution containing 220 g (3.053 mole) of acrylic acid, 0.9 g of an aqueous solution containing 0.36 g (0.715 mole) of sodium diethylenetriaminepentaacetate, 0.109 g (0.550 mmol) bisacrylamidoacetic acid, 73.27 g (1.832 mole) sodium hydroxide and 405.7 g water. 1140.6 g of a stable, self-reversible dispersion, miscible with water, water in oil, containing 22.62% of oil, 3.94% of surfactants, 40.31% of water are thus obtained. and 33.13% of a mixture of anionic polymers containing by weight 31.12% of carboxymethylcellulose and 68.88% of a copolymer AA-AANa, 40 - 60 in molar proportions, crosslinked with 240 ppm molar with respect to the monomers d 'ABAA. This dispersion is designated D₄; the intermediate dispersion obtained before the introduction of the carboxymethylcellulose is designated D₂₄. The rheological and application characteristics of these dispersions are mentioned in the following tables.

EXEMPLE 5EXAMPLE 5

On reproduit l'exemple 1, en utilisant d'une part 0,012 g (0,565 mmole) d'ABAA (240 ppm molaire par rapport aux monomères), et d'autre part une phase aqueuse contenant au total 424 g d'eau au lieu de 432 g. On obtient ainsi, après addition de 116,7 g de TYLOSE® C 1 000, 1 131,7 g d'une dispersion désignée D₅, contenant pondéralement 4 % de tensioactifs, 22,8 % d'huile, 37,5 % d'eau et 35,8 % d'un mélange de polymères anioniques contenant pondéralement 28,8 % de carboxyméthylcellulose et 71,2 % d'un copolymère AA-AAK-AMPSK, 25,5 - 59,5 - 15 en proportions molaires, réticulé avec 240 ppm molaire d'ABAA. La dispersion intermédiaire avant l'introduction de la carboxyméthylcellulose est désignée D₂₅. Dans un autre essai, on utilise 165,4 g de TYLOSE® C 1 000 au lieu de 116,7 g. On obtient ainsi 1 189,4 g d'une dispersion, désignée D₄₅. Les caractéristiques rhéologiques et applicatives de ces dispersions sont mentionnées dans les tableaux suivants.Example 1 is reproduced, using on the one hand 0.012 g (0.565 mmol) of ABAA (240 molar ppm relative to the monomers), and on the other hand an aqueous phase containing a total of 424 g of water instead of 432 g. There is thus obtained, after addition of 116.7 g of TYLOSE® C 1000, 1131.7 g of a dispersion designated D₅, containing by weight 4% of surfactants, 22.8% of oil, 37.5% of water and 35.8% of a mixture of anionic polymers containing by weight 28.8% of carboxymethylcellulose and 71.2% of an AA-AAK-AMPSK copolymer, 25.5 - 59.5 - 15 in molar proportions, crosslinked with 240 molar ppm of ABAA. The intermediate dispersion before the introduction of the carboxymethylcellulose is designated D₂₅. In another test, 165.4 g of TYLOSE® C 1000 are used instead of 116.7 g. 1 189.4 g of a dispersion is thus obtained, designated D₄₅. The rheological and application characteristics of these dispersions are mentioned in the following tables.

EXEMPLE 6EXAMPLE 6

On reproduit l'exemple 2, en utilisant d'une part, 0,145 g (0,7316 mmoles) d'ABAA (240 ppm molaire par rapport aux monomères) et d'autre part une phase huile contenant 225 g d'huile S 8515 et 22,5 g de sesquioléate de sorbitan. On obtient ainsi après addition de 114,5 g de TYLOSE® C 1 000, 1 110 g d'une dispersion désignée D₆, la dispersion intermédiaire avant l'introduction de la carboxyméthylcellulose est désignée D₂₆. Dans un autre essai, on introduit dans la dispersion D₂₆, 229 g de TYLOSE® C 1 000 et l'on obtient 1 224,5 g d'une dispersion désignée D₄₆. Les caractéristiques rhéologiques et applicatives de ces dispersions sont mentionnées dans les tableaux suivants.Example 2 is reproduced, using on the one hand, 0.145 g (0.7316 mmol) of ABAA (240 ppm molar relative to the monomers) and on the other hand an oil phase containing 225 g of oil S 8515 and 22.5 g of sorbitan sesquioleate. Is thus obtained after addition of 114.5 g of TYLOSE® C 1000, 1110 g of a dispersion designated D₆, the intermediate dispersion before the introduction of the carboxymethylcellulose is designated D₂₆. In another test, 229 g of TYLOSE® C 1000 are introduced into the dispersion D₂₆ and 1224.5 g of a dispersion designated D₄₆ is obtained. The rheological and application characteristics of these dispersions are mentioned in the following tables.

Dans les tableaux I à III, les abréviations utilisées ont les significations suivantes :

  • Ex : exemple.
  • ABAA % ppm : indique le nombre de moles d'ABAA pour 106 moles de monomères.
  • C : polymère anionique, du type des carboxyméthylcelluloses sodiques, C 1000 indique la TYLOSE® C 1 000 et C 300 indique la TYLOSE® C 300, commercialisées par la demanderesse ; leur pourcentage en poids est calculé par rapport au poids total de la composition selon l'invention.
  • Les pourcentages pondéraux des polymères présents dans la composition de l'invention sont exprimés en sec. Ainsi, 35,6 indiqué pour la dispersion D₁, du tableau I, signifie que la composition contient 35,6 % d'un mélange de polymères anioniques, dont 10,31 % par rapport au poids total de la composition de la TYLOSE® C 1 000, et en conséquence 35,6 - 10,3 = 25,3 % d'un polymère AA-AAK-AMPSK, 25,5 - 59,5 - 15.
  • T.A : tensioactifs présents dans la composition.
  • Ref : indique une pâte d'impression préparée avec de l'alginate de sodium comme indiqué dans la présente description.
  • Les caractéristiques des impressions sont notées de 0 à 5, de mauvaise à excellente, la note 3 est la qualité obtenue avec une pâte conventionnelle préparée avec de l'alginate de sodium.
  • G* : module complexe, il est exprimé en Pascal.
  • δ : angle de perte, il est exprimé en degré et il est calculé par la relation : tan δ = G''/G' où G' représente le module de conservation (storage modulus) et G" le module de perte (loss modulus).
  • Les dispersions D₂₁, D₂₂, D₂₃, D₂₄, D₂₅ et D₂₆ sont des dispersions utilisées pour préparer les compositions de l'invention ; leurs caractéristiques sont indiquées à titre de comparaison.
In Tables I to III, the abbreviations used have the following meanings:
  • Example: example.
  • ABAA% ppm: indicates the number of moles of ABAA for 106 moles of monomers.
  • C: anionic polymer, of the sodium carboxymethylcellulose type, C 1000 indicates TYLOSE® C 1000 and C 300 indicates TYLOSE® C 300, sold by the applicant; their percentage by weight is calculated relative to the total weight of the composition according to the invention.
  • The weight percentages of the polymers present in the composition of the invention are expressed in sec. Thus, 35.6 indicated for the dispersion D₁, of Table I, signifies that the composition contains 35.6% of a mixture of anionic polymers, of which 10.31% relative to the total weight of the composition of TYLOSE® C 1,000, and therefore 35.6 - 10.3 = 25.3% of an AA-AAK-AMPSK polymer, 25.5 - 59.5 - 15.
  • TA: surfactants present in the composition.
  • Ref: indicates a printing paste prepared with sodium alginate as indicated in the present description.
  • The characteristics of the impressions are marked from 0 to 5, from poor to excellent, note 3 is the quality obtained with a conventional paste prepared with sodium alginate.
  • G *: complex module, it is expressed in Pascal.
  • δ: loss angle, it is expressed in degrees and it is calculated by the relation: tan δ = G '' / G 'where G' represents the conservation module (storage modulus) and G "the loss module (loss modulus) ).
  • The dispersions D₂₁, D₂₂, D₂₃, D₂₄, D₂₅ and D₂₆ are dispersions used to prepare the compositions of the invention; their characteristics are shown for comparison.

L'analyse du tableau III permet de constater que les pâtes d'impression réalisées avec les compositions de l'invention présentent des propriétés applicatives supérieures ou égales à celles obtenues par l'emploi de pâtes d'impression préparées soit de manière conventionnelle avec de l'alginate de sodium, soit uniquement avec des polymères synthétiques à base d'acide acrylique.

Figure imgb0001
Figure imgb0002
TABLEAU III Rhéologie Caractéristiques des impressions G*(Pa) δ (°) To Re Un Ref 7 85 3 3 3 D₂₁ 56 10 3 3 3 D₁ 12 37 3 4 3 D₂₂ 16 28 3 3 3 D₂ 7 44 3 5 3 D₃₂ 6 50 D₂₃ D₃ 8 37 3 4 3 D₃₃ 16 29 3 4 3 D₂₄ 6 73 3 3 3 D₄ 4 70 3 5 3 D₂₅ 86 12 D₅ 12 38 3 4 3 D₄₅ 13 40 3 4 3 D₂₆ 10 42 3 3 3 D₆ 7 52 3 4 3 D₄₆ 5 56 3 5 3 The analysis of Table III shows that the printing pastes produced with the compositions of the invention have application properties greater than or equal to those obtained by the use of printing pastes prepared either conventionally with sodium alginate, or only with synthetic polymers based on acrylic acid.
Figure imgb0001
Figure imgb0002
TABLE III Rheology Print specifications No. G * (Pa) δ (°) To Re A Ref 7 85 3 3 3 From 56 10 3 3 3 From 12 37 3 4 3 From 16 28 3 3 3 From 7 44 3 5 3 From 6 50 From From 8 37 3 4 3 From 16 29 3 4 3 From 6 73 3 3 3 From 4 70 3 5 3 From 86 12 From 12 38 3 4 3 From 13 40 3 4 3 From 10 42 3 3 3 From 7 52 3 4 3 From 5 56 3 5 3

Claims (10)

Dispersions eau dans huile, stables, auto-réversibles, miscibles à l'eau, constituées par une phase huile, une phase aqueuse et au moins deux agents émulsifiants dont au moins un est de type eau dans huile, et au moins un est du type huile dans eau, caractérisées par le fait qu'elles contiennent de 20 à 50 % en poids d'un mélange constitué par un polymère anionique, hydrosoluble, appartenant au groupe des carboxyméthylcelluloses, désigné C, et par un polymère anionique synthétique, réticulé, insoluble dans l'eau mais gonflable à l'eau, désigné P, à base d'acide acrylique, désigné AA, partiellement salifié avec un métal alcalin, désigné M, éventuellement copolymérisé avec de l'acrylamido-2 méthyl-2 propanesulfonate de métal alcalin M, désigné AMPSM, réticulé avec un acide carboxylique diéthylénique et dans lequel le rapport molaire des fonctions acides salifiées sur l'ensemble des fonctions acides libres ou salifiées est compris entre environ 0,6 et environ 0,9, le rapport pondéral C/P+C étant compris entre 0,01 et 0,4.Water-in-oil dispersions, stable, self-reversible, water-miscible, consisting of an oil phase, an aqueous phase and at least two emulsifying agents, at least one of which is of the water in oil type, and at least one of which is the oil in water, characterized in that they contain from 20 to 50% by weight of a mixture constituted by an anionic, water-soluble polymer, belonging to the group of carboxymethylcelluloses, designated C, and by a synthetic, cross-linked, insoluble anionic polymer in water but swellable with water, designated P, based on acrylic acid, designated AA, partially salified with an alkali metal, designated M, optionally copolymerized with 2-acrylamide 2-methyl-propanesulfonate M, designated AMPSM, crosslinked with a diethylenic carboxylic acid and in which the molar ratio of the salified acid functions to all of the free or salified acid functions is between approximately 0.6 and about 0.9, the C / P + C weight ratio being between 0.01 and 0.4. Dispersions selon la revendication 1, caractérisées par le fait qu'elles contiennent de 20 à 50 % en poids d'un mélange de polymères anioniques constitué par 10 à 50 % en poids d'une carboxyméthylcellulose, C, et par 90 à 50 % en poids d'un polymère réticulé, P, AA-AAM-AMPSM contenant en proportions molaires de 0 à 30 % d'AMPSM et de 100 à 70 % d'un mélange AA et AAM contenant en proportions molaires de 20 à 40 % d'AA et de 80 à 60 % d'AAM, réticulé avec de 0,01 à 0,06 % en proportions molaires par rapport aux monomères mis en oeuvre, d'un acide carboxylique diéthylénique choisi dans le groupe constitué par l'acide bisacrylamidoacétique et l'acide diallyloxyacétique.Dispersions according to claim 1, characterized in that they contain from 20 to 50% by weight of a mixture of anionic polymers consisting of 10 to 50% by weight of a carboxymethylcellulose, C, and 90 to 50% by weight of a crosslinked polymer, P, AA-AAM-AMPSM containing in molar proportions of 0 to 30% of AMPSM and 100 to 70% of a mixture AA and AAM containing in molar proportions of 20 to 40% of AA and from 80 to 60% of AAM, crosslinked with from 0.01 to 0.06% in molar proportions relative to the monomers used, of a diethylenic carboxylic acid chosen from the group consisting of bisacrylamidoacetic acid and diallyloxyacetic acid. Dispersions selon l'une quelconque des revendications 1 et 2, caractérisées par le fait que le polymère P est réticulé par de l'acide bisacrylamidoacétique.Dispersions according to either of Claims 1 and 2, characterized in that the polymer P is crosslinked with bisacrylamidoacetic acid. Dispersions selon l'une quelconque des revendications 1 à 3, caractérisées par le fait que le polymère P est un polymère réticulé, AA-AAM-AMPSM, contenant en proportions molaires de 10 à 30 % d'AMPSM et de 90 à 70 % d'acide acrylique dont 60 à 80 % sont sous la forme d'un acrylate de métal alcalin.Dispersions according to any one of Claims 1 to 3, characterized in that the polymer P is a crosslinked polymer, AA-AAM-AMPSM, containing in molar proportions from 10 to 30% of AMPSM and from 90 to 70% of acrylic acid of which 60 to 80 % are in the form of an alkali metal acrylate. Dispersions selon l'une quelconque des revendications 1 à 3, caractérisées par le fait que le polymère P est un polymère réticulé, AA-AAM, contenant en proportions molaires de 30 à 40 % d'AA et de 70 à 60 % d'AAM.Dispersions according to any one of Claims 1 to 3, characterized in that the polymer P is a crosslinked polymer, AA-AAM, containing in molar proportions from 30 to 40% AA and from 70 to 60% AAM . Dispersions selon l'une quelconque des revendications 1 à 5, caractérisées par le fait qu'elles contiennent pondéralement de 10 à 20 % d'une carboxyméthylcellulose sodique et de 20 à 30 % d'un polymère P.Dispersions according to any one of Claims 1 to 5, characterized in that they contain by weight from 10 to 20% of a sodium carboxymethylcellulose and from 20 to 30% of a polymer P. Procédé d'obtention d'une dispersion selon l'une des revendications 1 à 6, caractérisé en ce que l'on effectue une réaction de polymérisation radicalaire en émulsion eau dans huile, à partir d'une solution aqueuse contenant les monomères constitutifs du polymère P, et éventuellement un agent chélatant, qui est émulsionnée dans une phase huile en présence d'un ou plusieurs agents émulsifiants du type eau dans huile, la réaction de polymérisation étant amorcée par l'introduction dans l'émulsion de départ d'un produit générant des radicaux libres ou un couple Redox, puis, lorsque la réaction de polymérisation est terminée, que l'on introduit dans la dispersion obtenue, à une température inférieure à 30°C, un ou plusieurs agents émulsifiants du type huile dans eau et la quantité désirée de polymère anionique C.Process for obtaining a dispersion according to one of Claims 1 to 6, characterized in that a radical polymerization reaction in water-in-oil emulsion is carried out from an aqueous solution containing the monomers constituting the polymer P, and optionally a chelating agent, which is emulsified in an oil phase in the presence of one or more emulsifying agents of the water in oil type, the polymerization reaction being initiated by the introduction into the starting emulsion of a product generating free radicals or a Redox couple, then, when the polymerization reaction is complete, which one introduces into the dispersion obtained, at a temperature below 30 ° C., one or more emulsifying agents of the oil in water type and the desired amount of anionic polymer C. Procédé selon la revendication 7 caractérisé par le fait que la polymérisation est amorcée par un couple Redox, à une température inférieure ou égale à 10°C, puis elle est conduite de manière quasi adiabatique jusqu'à une température supérieure ou égale à 60°C.Process according to Claim 7, characterized in that the polymerization is initiated by a Redox couple, at a temperature less than or equal to 10 ° C, then it is carried out in an almost adiabatic manner up to a temperature greater than or equal to 60 ° C . Procédé selon l'une des revendications 7 et 8, caractérisé par le fait que la réaction de polymérisation est amorcée par un couple Redox hydroperoxyde de cumène - disulfite de sodium, à la dose de 10 à 100 ppm molaires par rapport aux monomères d'hydroperoxyde de cumène et de 20 à 100 ppm molaire par rapport aux monomères de disulfite de sodium.Process according to either of Claims 7 and 8, characterized in that the polymerization reaction is initiated by a Redox couple of cumene hydroperoxide - sodium disulfite, at a dose of 10 to 100 molar ppm relative to the cumene hydroperoxide monomers and from 20 to 100 molar ppm relative to the sodium disulfite monomers. Utilisation, dans l'industrie textile, d'une dispersion selon l'une quelconque des revendications 1 à 6 pour l'obtention d'une pâte d'impression contenant un ou plusieurs colorants réactifs.Use, in the textile industry, of a dispersion according to any one of claims 1 to 6 for obtaining a printing paste containing one or more reactive dyes.
EP94402088A 1993-09-29 1994-09-20 Water-in-oil thickening dispersions, process for their preparation and their use in textile printing Expired - Lifetime EP0645429B1 (en)

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US6423802B1 (en) 1999-05-21 2002-07-23 Cabot Corporation Water soluble copolymers and polymer compositions comprising same and use thereof
US6656989B1 (en) 1999-05-21 2003-12-02 Cabot Corporation Compositions comprising water soluble copolymer and cesium salt of a carboxylic acid
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