Polymer latices from esters of (meth)acrylic acid and a vinyl ester of a branched chain carboxylic acid

Abstract: The invention provides polymers of esters of (meth)acrylic acid and the vinyl ester of a branched chain carboxylic acid; latices containing such polymers and their preparation; coating compositions comprising such latices; and solid polymeric products such as redispersible latex powders formed by physical drying of such latices. The present polymers provide attractive combination of properties to latices and coatings.

Description: This invention relates to polymers of esters of (meth)acrylic acid and a vinyl ester of a branched chain carboxylic acid, to latices containing such polymers, to the preparation of such polymers, to coating compositions comprising such latices and to solid polymeric products, for example redispersible latex powders formed by drying of such latices. GB-A-967,479 actually discloses a method for the preparation of a stable latex comprising copolymerising a monomer mixture containing (1) a vinyl ester of saturated aliphatic monocarboxylic acids in which the carboxyl groups are attached to tertiary and/or quaternary carbon atoms, (2) an alkyl ester of a polymerisable alpha,beta-ethylenically unsaturated carboxylic acid, and (3) from 0.5 to 5% by weight of total monomer of an alpha,beta-ethylenically unsaturated carboxylic acid, in an aqueous emulsion at a temperature between 0 °C and 90 °C and using a free radical initiator. More particularly in the examples I-IX, monomer premix compositions are used as starting materials which comprise as sole alkyl ester of alpha,beta-ethylenically unsaturated carboxylic acid component ethyl acrylate or propyl acrylate or methyl methacrylate, whereas as the vinyl ester of saturated branched aliphatic monocarboxylic acid component, inter alia mixtures of several carboxylic acids are applied, which contain from 7-19 carbon atoms. Moreover in page 3 and in claim 8 of this publication as preferred combination of starting monomers has been mentioned, that of ethyl acrylate and vinyl pivalate with methacrylic acid in proportions from 60-82 parts of ethyl acrylate, from 17-39 parts vinyl pivalate and from 1-3 parts of methacrylic acid respectively. This process has been found to provide only insufficient polymerisation yields, so that the latices obtained are still containing a substantial amount of residual monomers. The presence of free monomers in the latices is considered disadvantageous. These free monomers are substantially contributing to the odour of the latices and latex powders, cause a deleterious effect on latex stability and in the context of coating applications have shown a deleterious effect on the hardness, outdoor durability and blocking resistance of films formed by drying of the latices. Furthermore, from the point of view of toxicity it is desirable to minimise free monomers. Moreover, it was still a generally existing conception under persons skilled in the art that alkyl methacrylates and/or alkyl acrylates and vinyl esters with a large branched carbon chain were extremely difficult to copolymerise into a substantially random copolymer, due to a large difference in reactivity of the respective monomers. Therefore the copolymerisation of monomer pairs to a polymer dispersion at lower temperatures showing attractive properties of the coating films, was regarded as rather difficult or even impossible as can be derived from e.g. VeoVa Technical Manual VM 2.1, pages 7 and 8, Technical Bulletin, issued June, 1988 (VeoVa is a trade mark). Said conception also could be derived from the lectures held during FATIPEC Meeting Louvain-la-Neuve, Belgium, September 11, 1989 and during NVVT Meeting, Rotterdam, the Netherlands, May 23, 1989. In addition, the theoretically expected yield cannot be reached because some of the monomer does not polymerise and give rise to the aforementioned unattractive properties. Due to a growing need of environmentally friendly aqueous coatings having more attractive properties, and/or obtained by a more reliable and efficient copolymerisation, intensive further research effort was directed to the development of latices, containing a polymer of vinyl acetate and vinyl esters of one or more tertiary carboxylic acid(s) and having attractive physical properties in coating formulations and a relatively higher solids content and a low free monomer content. Although polymers containing latices were known in principle to give acceptable properties when used in coating applications, as is known from e.g. EP-A-315278, and US-A 3,654,209, there was a strong need to improve the mechanical properties, chemical resistance and water resistance of the finally obtained coating film after drying coating compositions, containing these polymers, due to modern industrial requirements. More particularly, it will be appreciated that there is a strong need to improve the properties of latices further in order to meet the modern requirements of glossy emulsion paints and anti-corrosion paints, characterised by a low free monomer content, good water spot resistance, low water absorption, alkali resistance and freeze-thaw stability. Moreover there is a need for an efficient, reliable, high monomer conversion process for the preparation of such latices, in order to enable the manufacture via an economically attractive way and avoiding the disadvantages (bad smell and instability during storage) of free monomers as much as possible. As a result of extensive research and experimentation there were surprisingly found such polymer compositions aimed at, showing a very attractive combination of properties such as high monomer conversion and chemical stability, alkali resistance, and light resistance of the latex film. Accordingly a group of polymers is provided characterised in that they are obtainable from a starting comonomer mixture comprising (i) methyl methacrylate; (ii) butyl acrylate; (iii) the vinyl ester of pivalic acid ("vinyl pivalate"); (iv) a stabilising monomer, selected from the group comprising acrylic acid, methacrylic acid, acrylamide, methacrylamide, diacetone acrylamide and sodium vinyl sulphonate and mixtures thereof, of which acrylic acid, methacrylic acid and methacrylamide are the most preferred, in an amount of from 0.5 to 5% by weight relative to the total weight of monomers, wherein the respective weight percentages of the components (i), (ii) and (iii) being calculated relative to the total weight of the sum of the amounts of these components, are simultaneously fulfilling the following equations, each describing compositions having equal performance contour lines in a triangle diagram: (I) CONV. = 100 x 1 + 100 x 2 + 99.3 x 3 + 0.2 x 1 .x 3 - 1 x 2 .x 3 - 4.8 x 1 .x 2 .x 3 (II) T g = 112 x 1 - 44 x 2 + 71 x 3 - 88 x 1 .x 2 - 86 x 1 .x 3 - 66 x 2 .x 3 + 36 x 1 .x 2 .x 3 (III) WA = 2 x 1 + 62 x 2 + 7 x 3 + 56.8 x 1 .x 2 + 3.6 x 1 .x 3 + 17.6 x 2 .x 3 - 11.7 x 1 .x 2 .x 3 (VI) WSR = 10 x 1 + 10 x 3 - 4 x 1 .x 2 - 12 x 2 .x 3 + 57 x 1 .x 2 .x 3 wherein CONV represents the monomer conversion and has a value of at least 99.0% (m/m) when an emulsion premix containing components (i) to (iv), an alkaryl sulphonate anionic surfactant, a non-ionic surfactant and potassium persulphate in demineralized water is added over 3 hours at 80 °C to the alkaryl sulphonate anionic surfactant and potassium persulphate in demineralized water, and the resulting mixture is digested for two hours at the same temperature, wherein the emulsion premix contains from 15.0 to 50.0 %wt of component (i), from 24.0 to 33.0 %wt of component (ii), from 20.0 to 60.0 %wt of component (iii) and from 1.0 to 2.0 %wt of component (iv), the weight percentages being based on the total of components (i) to (iv) and amounting to 100%, T g represents the glass transition temperature having a value in the range of from 0 °C to 50 °C, wherein WA represents the water absorption value being at most 45% m/m measured as specified hereinafter, wherein WSR represents the water spot value being at least 5, after 24 hours as specified hereinafter wherein x 1 represents the weight percentage of component (i), x 2 represents the weight percentage of component (ii) and wherein x 3 represents the weight percentage of component (iii), the values of x 1 , x 2 and x 3 being at least 0.5% by weight, calculated on the total weight of components (i), (ii) and (iii). It is observed that the exact values of the coefficients in equations (I) to (IV) are slightly depending on the specific types of the applied stabilising monomer and surfactant, and on the concentrations thereof. These small deviations will, however, easily be taken into account by persons skilled in the art. In this respect reference is made to EP-A-431656 and EP-A-486110, both published after the priority date of the present invention, which also describe polymers obtainable from (i) methylmethacrylate, (ii) butylacrylate, (iii) the vinyl esters of tertiary carboxylic acids and a stabilizing monomer. However, in case of EP-A-431656 the acid of component (iii) has 9 or 10 carbon atoms, whereas the acids of component (iii) according to EP-A-486110 contain 10 carbon atoms. According to a preferred embodiment of the present invention, polymers are provided, which are derivable from the components (i) - (iv), wherein the component (iv) is consisting of acrylic acid, methacrylic acid or methacrylamide in an amount of 0.5 - 2% by weight and preferably 1% by weight, wherein the respective weight percentages x 1 , x 2 and x 3 of the components (i), (ii) and (iii), being calculated relative to the total weight of the sum of the amounts of these components, are simultaneously fulfilling the equations (I) to (IV) wherein CONV, T g , WA, WSR have the same value as defined above. More preferably component (iv) is acrylic acid in concentration of 1% by weight. The starting comonomer compositions containing monomers (i), (ii) and (iii) in proportions meeting the aforementioned equations are represented by the shaded area in figure 1. It will be appreciated that vinyl pivalate, as component (iii) to be applied according to the present invention, is normally manufactured starting from a technical quality alkene and that in spite of application of modern separation techniques applied on the initially obtained vinyl ester the desired main component may contain similar homologues in minor amounts which can be used successfully for the preparation of latices according to the present invention. As component (iii), predominantly containing the vinyl pivalate, preferably VeoVa 5 is used as starting comonomer. A more preferred group of polymers of the present invention are derivable from comonomer mixtures, wherein the weight fractions of said components (i), (ii) and (iii) simultaneously fulfil the equations (I) to (IV), wherein, however, CONV has now a value of at least 99.3% (m/m), T g has now a value in the range of from 10 °C and 35 °C, the water absorption WA has now a value of at most 35%, and the water spot resistance WSR has now a value of at least 6 and wherein component (iv) is 1% by weight acrylic acid. These preferred starting comonomer compositions, containing monomers (i), (ii) and (iii) in the suitable proportions meeting the aforementioned requirements are represented by the shaded area in figure 2. It was found that the application of other stabilising monomers instead of acrylic acid in the same weight percentage did not change these shaded areas in figures 1 and 2 significantly. One of the most preferred embodiments of the polymers of the present invention is formed by those, characterised in that they are derivable from a starting comonomer mixture as set out above, comprising: from 3 to 61% by weight of methyl methacrylate; from 20 to 39% by weight of butyl acrylate; from 20 to 39% by weight of butyl acrylate; from 5 to 75% by weight of vinyl esters of tertiary carboxylic acids containing 5 carbon atoms; and 1% by weight of acrylic acid, the total amounting to 100%. It has moreover been found, that by the use of only one copolymerisable stabilising component (iv), latices could be obtained showing an acceptable low free monomer content, i.e. < 0.7% by weight, based on the solids content, and a good stability. It will be appreciated that the present invention is also relating to latices, containing as polymeric constituent 40-60% by weight of a polymer as described above and more preferably those wherein the polymeric constituent amounts from 45 to 50% by weight, to coating compositions comprising a latex and preferably at least one pigment, and to solid polymeric products formed by physical drying of such latices or coatings and to redispersible latex powders formed by physical drying of such latices and to coating compositions derived from such powders. A further aspect of the present invention relates to a process for the preparation of latices containing the aforementioned specified polymers. It was found in addition that these attractive results could be reached by effecting thermal initiation of the starting reaction mixture, being rather independent on the actual relative proportions of the components (i)-(iv) in the indicated ranges. The polymers containing latices according to the present invention may be prepared under conditions which are known in the art and generally involve a temperature of 20-100 °C. More particularly the preparation process is carried out in a temperature range of from 60-100 °C, and preferably from 75 to 85 °C. In the reaction mixture additional stabilisers, optionally to be copolymerised, one or more polymerisation initiators and optionally buffering agents are to be included, but more preferably not any buffering agent is used. Stabilisers suitably constitute 2-8% by weight, calculated relative to the total weight of the monomer constituents. Suitable stabilisers and the amount they are used in are well-known in the art and described in for instance EP-A-295,727, and in Emulsifiers and detergents, international edition, volume 1 (by Mc Cutcheon, The Manufacturing Confectioner Publishing Co., Glen Rock NY, USA 1990). Preferably an anionic and a non-ionic surface active agent are used. Especially preferred is the use of an alkylaryl sulphonate together with an ethoxylated nonylphenol (e.g., "Arkopol N230", a trademark). Likewise suitable free radical initiators, radical formation accelerators, buffering agents and their relative amounts are also well-known in the art and disclosed in the above cited Technical Manual and European patent application. According to a preferred embodiment of the process of the present invention, thermal initiation is applied and the reaction is carried out in an inert atmosphere, nitrogen suitably being used to flush out the reaction vessel prior to the start of the reaction. According to a further preferred embodiment of the process of the present invention, an emulsion premix is prepared in demineralised water from a part of one or more surface active agent, and a part of one or more initiators and comonomers (i)-(iv). The reactor is flushed with nitrogen and filled with about an equal amount of demineralised water, and the remaining amounts of the surface active agent(s) and initiator. The reactor is heated to a temperature in the specified range, e.g. 80 °C, the nitrogen stream is stopped and the emulsion premix addition is started. The addition is normally extended over a period of from 2 to 5 hours during which the originally adjusted temperature is maintained. A post polymerisation period of from 1 to 3 hours is normally used at a temperature of e.g. 80 °C. After this post polymerisation, the latex obtained is cooled and if necessary filtered. The generally obtained latices have a total solids content in the range of from 30-60% by weight of the latex and preferably from 40-50% and a weight average particle diameter in the range of from 90-170 nm depending on the surfactant repartition between the emulsion premix and the initial reactor charge. A further aspect of the present invention relates to a latex produced by the process described above, and the polymer which forms on physical drying of such a latex, for example to form a coating on a substrate or a powder intended for reconstitution as a latex or use in a concrete or other latex based end product. Latices in accordance with the invention may find application in concretes, lacquers, paints, wood coatings, anti-corrosion paints and textured coatings. They are of particular interest for composing lacquers and paints due to their good film forming properties, their excellent water resistance, their high pigment binding power, the lack of tackiness of the films, their alkali resistance and resistance to ultra violet light. Paints in accordance with the invention contain the latices of the invention, pigments, and common further constituents such as fillers, cosolvents, thickeners, dispersants, preservatives, corrosion inhibitors, and anti-foaming agents. It will be appreciated therefore that coating compositions, comprising the latices according to the present invention and solid polymer product formed thereof, also form an aspect of the present invention. The invention will now be further described with reference to the following examples. EXAMPLE I In a three litre reaction flask, provided with a central and four peripheral glass openings fitted with a reflux condenser, stirrer, thermometer, nitrogen inlet tube and emulsion premix inlet tube. An emulsion premix is prepared by mixing the following ingredients in the given amounts. Demineralised water 575.0 g Humifen SF 90 (10% in water) 95.0 Arkopal N230 (25% in water) 120.0 Potassium persulphate 4.0 Methyl methacrylate 330.0 n-Butyl acrylate 330.0 VeoVa 5 330.0 Acrylic acid 10.0 The reaction flask is swept with nitrogen and the following ingredients are added: Demineralised water 480.2 g Humifen SF 90 (10% in water) 5.0 Potassium persulphate 1.0 The ingredients in the reaction flask are heated to 80 °C. When the temperature reaches 80 °C, the nitrogen stream is stopped and the emulsion premix addition is started. The monomer pre-emulsion is added regularly over a period of 3 hours and a temperature of 80 °C is maintained. A 2-hour digestion period (at the same temperature) is applied. After the post-cooking, the latex is cooled and if necessary filtered. In general, these latices have a total solids content of about 45% and the weight average particle diameter is about 150 nm. The obtained latices were tested as to water absorption, water spot resistance of latex polymer film, whereas also monomer conversion, particle size, minimum film formation temperature, and glass transition temperature were measured. EXAMPLES II-VI In the same way as described in Example I, polymer latices were prepared from different sets of comonomers. The respective amounts of the applied constituting monomers in per cent by weight as to total starting composition and the relevant properties of the latices obtained are listed in the following table. Test methods The water absorption of latex polymer and emulsion paint films (Thick film test method) was measured as described hereinafter. A wet film of 2 mm thickness is applied on a polyethylene foil (the latex is kept on the foil by applying an automotive sealer on the edges of the foil). To avoid a too fast evaporation of water and as a result severe mud-cracking the panels are covered with some water vapour transmitting material and then stored at 20 °C above the Tg for a week. The cover is removed after clear films are formed. Three pieces of 2 x 2 cm are cut from the film after removal from the glass panel and weighed to the nearest 0.1 mg. These are stored in demineralised water at 23 °C and reweighed after 14 days (after removal of the excess of water by filter paper). The water absorption is calculated from the observed weight increase. The result of the triplicate measurements are averaged. The water spot resistance of latex polymer films was measured as described hereinafter. A wet latex film of 200 µm (micron) is applied on a glass panel and allowed to dry for a week at 20 °C above the Tg. When cooled to 23 °C a drop of water is brought on the film and the panel is placed on a dark underground. After 24 hrs the whitening effect is visually judged. A rating between 10 (film is unaffected) and 0 (film is completely white) is given. In order to avoid evaporation of the water droplet, it can be covered overnight by a watch glass.

Claims: Claims for the following Contracting States : BE, CH, DE, FR, GB, IT, LI, NL, SE Polymers obtainable by polymerisation of a starting comonomer mixture comprising (i) methyl methacrylate; (ii) butyl acrylate; (iii) the vinyl ester of pivalic acid; (iv) a stabilising monomer, selected from the group comprising acrylic acid, methacrylic acid, acrylamide, methacrylamide, diacetone acrylamide and sodium vinyl sulphonate and mixtures thereof, in an amount of from 0.5 to 5% by weight relative to the total weight of monomers, wherein the respective weight percentages of the components (i), (ii) and (iii) being calculated relative to the total weight of the sum of the amounts of these components, are simultaneously fulfilling the following equations, each describing compositions having equal performance contour lines in a triangle diagram: (I) CONV. = 100 x 1 + 100 x 2 + 99.3 x 3 + 0.2 x 1 .x 3 - 1 x 2 .x 3 - 4.8 x 1 .x 2 .x 3 (II) T g = 112 x 1 - 44 x 2 + 71 x 3 - 88 x 1 .x 2 - 86 x 1 .x 3 - 66 x 2 .x 3 + 36 x 1 .x 2 .x 3 (III) WA = 2 x 1 + 62 x 2 + 7 x 3 + 56.8 x 1 .x 2 + 3.6 x 1 .x 3 + 17.6 x 2 .x 3 - 11.7 x 1 .x 2 .x 3 (IV) WSR = 10 x 1 + 10 x 3 - 4 x 1 .x 2 - 12 x 2 .x 3 + 57 x 1 .x 2 .x 3 wherein CONV represents the monomer conversion and has a value of at least 99.0% (m/m) when an emulsion premix containing components (i) to (iv), an alkaryl sulphonate anionic surfactant, a non-ionic surfactant and potassium persulphate in demineralized water is added over 3 hours at 80 °C to the alkaryl sulphonate anionic surfactant and potassium persulphate in demineralized water, and the resulting mixture is digested for two hours at the same temperature, wherein the emulsion premix contains from 15.0 to 50.0 %wt of component (i), from 24.0 to 33.0 %wt of component (ii), from 20.0 to 60.0 %wt of component (iii) and from 1.0 to 2.0 %wt of component (iv), the weight percentages being based on the total of components (i) to (iv) and amounting to 100%, T g represents the glass transition temperature having a value in the range of from 0 °C to 50 °C, wherein WA represents the water absorption value being at most 45% m/m, wherein WSR represents the water spot resistance being at least 5, after 24 hours, wherein x 1 represents the weight percentage of component (i), x 2 represents the weight percentage of component (ii) and x 3 represents the weight percentage of component (iii), the values of x 1 , x 2 and x 3 being at least 0.5% by weight, calculated on the total weight of components (i), (ii) and (iii). Polymers according to claim 1, characterised in that they are derivable from comonomer mixtures, comprising methyl methacrylate (i), butyl acrylate (ii), vinyl esters of tertiary carboxylic acids containing 5 carbon atoms (iii), and acrylic acid (iv) the amount of acrylic acid ranging of from 0.5 to 2.0% by weight and the total amounting to 100%. Polymers according to claim 2, characterised in that the weight fractions x 1 , x 2 and x 3 of the components (i), (ii) and (iii) simultaneously fulfil the equations (I) to (IV), each describing compositions having equal performance contour lines in a triangle diagram wherein CONV has a value of at least 99.3% (m/m), T g has a value in the range from 10 to 35 °C, WA has a value of at most 35%, and WSR has a value of at least 6, after 24 hours as defined above, when applied in coating films, and wherein component (iv) is 1% acrylic acid by weight. Polymers according to any one of claims 1 to 3, characterised in that they are derivable from a starting mixture comprising: from 3 to 61% by weight of methyl methacrylate; from 20 to 39% by weight of butyl acrylate; from 5 to 75% by weight of vinyl esters of tertiary carboxylic acids containing 5 carbon atoms; and 1% by weight of acrylic acid, the total amounting to 100%. A latex containing as polymeric constituent 40-60% by weight of a polymer according to any one of the claims 1 to 4. Coating compositions comprising a latex according to claim 5 and at least one pigment. A solid polymeric product formed by physical drying of a latex according to claim 5. A process for the preparation of latices, containing the polymers according to any one of the claims 1 to 4, by polymerisation of the comonomer mixtures at a temperature in the range of from 60 to 100 °C in the presence of additional stabilisers, one or more polymerisation initiators. Process according to claim 8, in which the polymerization is conducted at a temperature in the range of from 75 to 85 °C. Claims for the following Contracting State : ES Process comprising polymerisation of a starting comonomer mixture comprising (i) methyl methacrylate; (ii) butyl acrylate; (iii) the vinyl ester of pivalic acid; (iv) a stabilising monomer, selected from the group comprising acrylic acid, methacrylic acid, acrylamide, methacrylamide, diacetone acrylamide and sodium vinyl sulphonate and mixtures thereof, in an amount of from 0.5 to 5% by weight relative to the total weight of monomers, wherein the respective weight percentages of the components (i), (ii) and (iii) being calculated relative to the total weight of the sum of the amounts of these components, are simultaneously fulfilling the following equations, each describing compositions having equal performance contour lines in a triangle diagram: (I) CONV. = 100 x 1 + 100 x 2 + 99.3 x 3 + 0.2 x 1 .x 3 - 1 x 2 .x 3 - 4.8 x 1 .x 2 .x 3 (II) T g = 112 x 1 - 44 x 2 + 71 x 3 - 88 x 1 .x 2 - 86 x 1 .x 3 - 66 x 2 .x 3 + 36 x 1 .x 2 .x 3 (III) WA = 2 x 1 + 62 x 2 + 7 x 3 + 56.8 x 1 .x 2 + 3.6 x 1 .x 3 + 17.6 x 2 .x 3 - 11.7 x 1 .x 2 .x 3 (IV) WSR = 10 x 1 + 10 x 3 - 4 x 1 .x 2 - 12 x 2 .x 3 + 57 x 1 .x 2 .x 3 wherein CONV represents the monomer conversion and has a value of at least 99.0% (m/m) when an emulsion premix containing components (i) to (iv), an alkaryl sulphonate anionic surfactant, a non-ionic surfactant and potassium persulphate in demineralized water is added over 3 hours at 80 °C to the alkaryl sulphonate anionic surfactant and potassium persulphate in demineralized water, and the resulting mixture is digested for two hours at the same temperature, wherein the emulsion premix contains from 15.0 to 50.0 %wt of component (i), from 24.0 to 33.0 %wt of component (ii), from 20.0 to 60.0 %wt of component (iii) and from 1.0 to 2.0 %wt of component (iv), the weight percentages being based on the total of components (i) to (iv) and amounting to 100%, T g represents the glass transition temperature having a value in the range of from 0 °C to 50 °C, wherein WA represents the water absorption value being at most 45% m/m, wherein WSR represents the water spot resistance being at least 5, after 24 hours, wherein x 1 represents the weight percentage of component (i), x 2 represents the weight percentage of component (ii) and x 3 represents the weight percentage of component (iii), the values of x 1 , x 2 and x 3 being at least 0.5% by weight, calculated on the total weight of components (i), (ii) and (iii). Process according to claim 1, characterised in that the comonomer mixtures comprise methyl methacrylate (i), butyl acrylate (ii), vinyl esters of tertiary carboxylic acids containing 5 carbon atoms (iii), and acrylic acid (iv) the amount of acrylic acid ranging of from 0.5 to 2.0% by weight and the total amounting to 100%. Process according to claim 2, characterised in that the weight fractions x 1 , x 2 and x 3 of the components (i), (ii) and (iii) simultaneously fulfil the equations (I) to (IV), each describing compositions having equal performance contour lines in a triangle diagram wherein CONV has a value of at least 99.3% (m/m), T g has a value in the range from 10 to 35 °C, WA has a value of at most 35%, and WSR has a value of at least 6, after 24 hours as defined above, when applied in coating films, and wherein component (iv) is 1% acrylic acid by weight. Process according to any one of claims 1 to 3, characterised in that the starting mixture comprises: from 3 to 61% by weight of methyl methacrylate; from 20 to 39% by weight of butyl acrylate; from 5 to 75% by weight of vinyl esters of tertiary carboxylic acids containing 5 carbon atoms; and 1% by weight of acrylic acid, the total amounting to 100%. A process for the preparation of latices, containing the polymers obtainable by a process according to any one of the claims 1 to 4, by polymerisation of the comonomer mixtures at a temperature in the range of from 60 to 100 °C in the presence of additional stabilisers, one or more polymerisation initiators. Process according to claim 6, in which the polymerization is conducted at a temperature in the range of from 75 to 85 °C. Process comprising physical drying of a latex according to claim 6 or 7.

Inventors: COPPIN LINDA LOUISE-MARIE GUIL, SCHOLTEN HENRICUS PAULUS HUBER, SLINCKX MARTINE MADELEINE CHRI, COPPIN, LINDA LOUISE-MARIE GUILLAUME, SCHOLTEN, HENRICUS PAULUS HUBERTUS, SLINCKX, MARTINE MADELEINE CHRISTIANE PIERRE
Applicants: SHELL INT RESEARCH, SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
Application year: 1992
Main classification: C08F220
IPC codes: C09D5, C08F220, C08F218, C09D133, C08F2, C09D131, C08F18, C08L31