Patent Application
20090326142
The present invention relates to the field of aqueous dispersions of structured polymers comprising at least one polymer with a low glass transition temperature and at least one polymer with a high glass transition temperature, which dispersions are intended to be used as binders in paint formulations.
The properties which characterize a good gloss paint formulation are good ease of application, good binding power on various types of substrates (bare walls or even walls covered with old layers of paint, wood, paper, and the like), determined by the elasticity and the adhesion of the binder, film formation at low temperature (˜5° C.), good resistance to soiling, good resistance to wet abrasion (washability), good resistance to blocking and a suitable specular gloss.
Generally, water paint compositions comprise a polymer as binder and pigments. After application to the substrate to be treated and drying of the composition, the film forms by coalescence of the particles. The quality of the film depends on good coalescence. This is generally favoured by the addition of solvents which are coalescence agents. They plasticize the particles of polymers, thus reducing the temperature of formation of the paint film. These coalescence agents make it possible to use polymers which do not normally form a film at the temperature at which the paint is applied. After drying, they are gradually removed by evaporation. The paint film thus gradually hardens and thus acquires advantageous properties: good resistance to wet abrasion, good resistance to blocking, and the like. Unfortunately, there are disadvantages to these coalescence agents. They are volatile products, in particular if their boiling point is low: they contribute to polluting the atmosphere. If, on the other hand, their boiling point is high, they are removed very gradually, which results in a very slow development of the hardness of the film. In this case, the properties, such as the resistance to blocking in the period following the application of the paint, are limited. Furthermore, these paints do not conform to the standards, such as those referred to as “Nordic Swan” or “Blue Angel”.
The use of conventional latexes based on polymers of low Tg, which thus form films at temperatures of approximately 0° C., makes it possible to solve these problems in the case of matt paints, where the level of polymers is low. On the other hand, for gloss paints, which for their part have a high level of polymers, the use of these latexes causes problems related to the inadequate hardness of the paint film.
Mention may be made, among the solutions provided to solve the problems mentioned above, for example, of JP56116759 (Daicel Chemical Ind.), which discloses polymer acrylic emulsions prepared by multistage polymerization, so that 50-97% of the polymer prepared in the first stage has a glass transition temperature (Tg)<−20° and 3-50% prepared in the final stage has a Tg>+20°. The acrylic emulsions according to this document are of use as coating materials.
EP 0522789 discloses an elastomer composition comprising a sequential latex, the Tg of the soft part of which is less than −30° C. and the level of which is more than 70%. Furthermore, the difference between the two Tg values is greater than 40° C.
EP 0728154 B1 discloses, positioning itself with respect to the abovementioned document (EP 0522789), an aqueous dispersion of structured particles of polymer comprising at least one first polymer with a Tg1 of between −25° C. and 0° C. and at least one polymer 2 with a Tg2 of between 5 and 40° C. The monomers participating in the polymers 1 and 2 are chosen so that Tg2−Tg1 is less than or equal to 40° C.
The Applicant Company has found that the solution to these problems and to many others is the use of an aqueous dispersion based on structured polymer exhibiting two distinct glass transition temperatures which is obtained by the two-stage emulsion polymerization of mixtures of well-chosen monomers.
A first subject-matter of the present invention is thus an aqueous dispersion of polymers in the form of structured particles with a mean diameter of between 70 and 300 nm comprising at least one polymer exhibiting a glass transition temperature (Tg1) of between −50° C. and 0° C., representing from 30 to 70% by weight of the total weight of the particles, and at least one second polymer having a glass transition temperature (Tg2) of between 10 and 80° C., representing from 70 to 30% by weight of the total weight of the particles. The polymers 1 and 2 are defined such that Tg2−Tg1 is greater than or equal to 40° C.
According to a preferred form of the invention, the polymers 1 and 2 are mutually incompatible.
The term “incompatibility” is understood to mean the existence at least of two separate phases of the copolymers in the same particle having a structured morphology.
The structured particles according to the invention can have any morphology of structured particles. In particular, they can be provided in the form of a core-shell morphology or in the form of a multicore structure, in the form of a multicellular nodule or in the “hazelnut” form, one polymer phase of which incompletely surrounds the second. Examples of these structures have been described by D. C. Sundberg and Y. G. Durant in “Polymer Reaction Engineering”, vol. 11, No. 3, pp. 379-432 (2003).
The incompatibility can be determined by the use, optionally in conjunction, of various techniques, such as:
DSC—differential scanning calorimetry is employed to determine the thermal transitions of the various phases in structured materials. For each phase of the polymer, the change in heat capacity observed at the Tg is proportional to the amount of this phase.
DMA—dynamic mechanical analysis provides the dynamic moduli as a function of the temperature. The mechanical transitions (Tg) of the various phases of the structured materials can be accessed by this method.
TEM—transmission electron microscopy is the most commonly used method to visualize the domains of the structured particles. Observation may be carried out either on whole particles or on sections of particles obtained by techniques such as cryofracturing.
NMR—nuclear magnetic resonance spectroscopy, in particular of solids, provides important information relating to the internal composition of the various phases and interphases of the structured particles. The technique is based on the measurement of the spin relaxation times of the protons, which depend on the glass transition temperature of the phase.
The glass transition temperatures (Tgs) can be determined by various techniques, in particular by DSC and by DMA.
Preferably, the particles of the invention display a structure of “hazelnut” type by TEM, as represented diagrammatically in the drawing below.
According to the invention, the polymers 1 and 2 are prepared from a mixture of monomers comprising at least one ethylenically unsaturated monomer chosen from (meth)acrylic acid esters and vinyl monomers, such as vinyl acetate and vinylaromatic monomers, and also the monomers which can copolymerize with them.
Mention may also be made, as nonlimiting examples of monomers which can copolymerize with vinyl acetate and/or acrylic esters and/or styrene, of ethylene and olefins, such as isobutene; vinyl esters of saturated and straight or branched monocarboxylic acids having from 1 to 12 carbon atoms, such as vinyl propionate, “vinyl versatate” (vinyl neodecanoate), vinyl pivalate or vinyl laurate; esters of unsaturated mono- or dicarboxylic acids having 3 to 6 carbon atoms with alkanols having 1 to 10 carbon atoms, such as methyl maleate, ethyl maleate, butyl maleate, ethylhexyl maleate, methyl fumarate, ethyl fumarate, butyl fumarate or ethylhexyl fumarate; vinylaromatic monomers, such as methylstyrenes or vinyltoluenes; vinyl halides, such as vinyl chloride or vinylidene chloride; diolefins, particularly butadiene; (meth)allyl esters of (meth)acrylic acid; (meth)allyl esters of the mono- and diesters of maleic acid, fumaric acid and itaconic acid; and alkene derivatives of the amides of acrylic acid and methacrylic acid, such as N-methallylmaleimide.
The monomers forming the first polymer can be identical to or different from those forming the second polymer. This is because a person skilled in the art knows to select the monomers to be polymerized and to define their proportions according to the properties which he wishes to give to the polymer being prepared. Thus, a person skilled in the art, by applying the Fox law (T. G. Fox, Bull. Am. Physic. Soc., vol. 1, No. 3, page 123, year 1956), knows to select the mixture of monomers to be polymerized in order to confer the desired Tg on the polymer being prepared.
Each polymer participating in the composition of the aqueous dispersion of the invention can additionally comprise at least one functional monomer chosen from:
According to a preferred form of the invention, the polymer 1 and the polymer 2 are prepared from a monomer mixture comprising:
More preferably still, the polymer 1 is prepared from a mixture of monomers comprising:
i. from 5 to 45% of at least one monomer (a),
ii. from 55 to 95% of at least one monomer (b), and
iii. from 0 to 5% of at least one monomer (c).
For its part, the polymer 2 is prepared from a mixture comprising:
i. from 55 to 90% of at least one monomer (a),
ii. from 10 to 45% of at least one monomer (b), and
iii. from 0 to 5% of at least one monomer (c).
As described above, the mixtures of monomers are defined so as to confer the required properties, in particular the desired Tg values, on the polymers being prepared.
Furthermore, the composition is arranged so that the difference between Tg2 and Tg1 is greater than or equal to 40 and preferably between 45 and 100° C.
The dispersion of the invention is prepared by radical emulsion polymerization according to a process in at least two stages comprising an emulsion polymerization stage, resulting in the polymer 1, and another polymerization stage, resulting in the polymer 2, characterized in that:
Generally, the mixtures of monomers to be polymerized do not comprise crosslinking monomers. However, the addition, to the first stage or to the second stage, of 0 to 5% by weight of at least one crosslinking monomer, such as 1,2-ethylene glycol dimethacrylate, 1,4-butylene glycol dimethacrylate, trimethylolpropane triacrylate, allyl methacrylate, diallyl phthalate, divinylbenzene or triallyl cyanurate, is not ruled out.
As indicated above, the mixtures of monomers can comprise up to 5% by weight of at least one functional monomer.
During one stage, the polymerization is carried out of a mixture of monomers comprising:
i. from 5 to 45% of at least one monomer (a),
ii. from 55 to 95% of at least one monomer (b), and
iii. from 0 to 5% of at least one monomer (c).
The mixture introduced during the other stage comprises:
from 55 to 90% of at least one monomer (a),
from 10 to 45% of at least one monomer (b), and
from 0 to 5% of at least one monomer (c).
The polymerization of the first stage is carried out in the presence of a surfactant and of a initiator, which are introduced all at once as initial charge into the reactor in the form of an aqueous solution.
The solutions of surfactant and of initiator can also be added simultaneously with the addition of monomers.
The surfactant which is used can be any surfactant conventionally used for emulsion polymerization processes.
The surfactants which can be used are anionic, cationic or nonionic emulsifiers. Use may be made of one surfactant alone or a mixture of several surfactants.
Use is generally made, as surfactant, of conventional anionic surfactants represented in particular by alkyl sulphates, such as sodium lauryl sulphate, alkylsulphonates, alkylaryl sulphates, alkylaryl-sulphonates, such as sodium dodecylbenzenesulphonate, aryl sulphates, arylsulphonates, alkyl ethoxylates, alkylaryl ethoxylates, sulphated or phosphated alkyl ethoxylates or alkylaryl ethoxylates or their salts, sulphosuccinates, alkali metal alkyl phosphates, salts of hydrogenated or nonhydrogenated abietic acid, or fatty acid salts, such as sodium stearate.
Use is preferably made of anionic or nonionic surfactants.
They are generally employed in a proportion of 0.01 to 5% by weight, with respect to the total weight of the monomers.
It is also possible to couple the use of one of the anionic surfactants mentioned above with a water-soluble nonionic polymer, such as, for example, poly(vinyl alcohol) or polyvinylpyrrolidone (PVP).
It is also possible to couple the use of one of the anionic surfactants mentioned above with a stabilizing system based on synthetic anionic polymers, for example poly((meth)acrylic acid), poly(meth)acrylamide, poly(vinylsulphonic acid)s and water-soluble copolymers of these, or condensates, such as sulphonated melamine/formaldehyde or sulphonated naphthalene/formaldehyde, styrene/maleic acid copolymers and vinyl ether/maleic acid copolymers.
The monomers constituting each of the phases of the dispersion can be simply introduced into the reactor in the form of a homogeneous mixture of monomers or can be emulsified using at least one surface-active agent.
The polymerization can be initiated either by the thermal decomposition of a radical initiator, such as sodium persulphate or potassium persulphate, or by a redox system composed of a pairing of an oxidizing agent and of a reducing agent. Mention may be made, as examples of redox system, of: sodium persulphate/sodium disulphite; t-butyl hydroperoxide/sodium formaldehydesulphoxylate; t-butyl perbenzoate/erythorbic acid; hydrogen peroxide/erythorbic acid; H2O2/Fe2+; ROOH/Ce4+ (where R represents an organic group, such as a C1-C6 alkyl or C5-C8 aryl group) or K2S2O8/Fe2+.
The initiators are added at a level of between 0.05 and 3% by weight, with respect to the monomers used.
Preferably, the first stage is initiated by a thermal initiator.
The polymerization of the first stage is carried out at a temperature of between 60 and 95° C.
According to the invention, the introduction of the monomers of the second stage begins when the conversion of the monomers of the first stage is greater than 95% and preferably greater than 97%.
Preferably, the main mixture of the monomers constituting the second polymer of the dispersion is emulsified using at least one surface-active agent. It is preferable to use anionic or nonionic surfactants.
Preferably, the second stage is polymerized using a redox initiator.
The oxidizing agent is chosen from the group consisting of peroxides and hydroperoxides, such as t-butyl perbenzoate and t-butyl hydroperoxide. Preferably, the oxidizing agent is introduced during the synthesis of the first stage.
Preferably, the solution of reducing agent is added simultaneously with the addition of monomers of the second stage.
The polymerization of the second stage is carried out at a temperature of between 40 and 95° C.
The amount of water used in the reaction medium is generally determined by the level of solids desired in the dispersion and generally lies between 40 and 70%, preferably between 45 and 60%.
The polymer emulsion after the second stage can be subjected to treatment by an additional redox initiation system for the purpose of reducing the level of residual monomers. It can also be purified by steam distillation of the volatile organic compounds (stripping).
The pH of the latex is adjusted to a value slightly greater than 7 using alkaline substances, for example sodium hydroxide or potassium hydroxide, for good compatibilization with the other ingredients of the paint formulation.
The dispersion of the invention is used in coatings, such as varnishes or paints, for applications on walls and ceilings, frontages, wood, tiles, and the like. It is preferably used as binder in varnish and paint formulations devoid of solvents or coalescence agents. Another of the subject-matters of the invention is a paint formulation devoid of solvent or coalescence agent comprising the dispersion of the invention.
A representative formulation is specified in Table 1 and an outline manufacturing procedure is given below.
The preparation of the paint comprising the dispersion of the invention follows the following protocol:
The invention may be better understood on reading the following examples, which illustrate the invention without limiting the scope thereof.
The Tg values targeted in the examples below are calculated as mentioned above according to the Fox equation, taking into consideration the main monomers (the groups a and b), by applying the Tg values of the homopolymers given by “Polymer Handbook; Third Edition, 1989” as follows:
Tg=100° C. for polystyrene
Tg=105° C. for poly(methyl methacrylate)
Tg=−54° C. for poly(butyl acrylate)
Tg=−50° C. for poly(2-ethylhexyl acrylate)
These procedures are based on a process which can be broken down into two separate phases, a first stage, which is the preparation of a random copolymer, and a second stage, which is the synthesis of a random copolymer following the first copolymer, in order to obtain the latex comprising structured particles.
This copolymer is synthesized in a 2 litre glass reactor of SVL type. The maximum working capacity of this type of reactor is 1.5 litres. The internal temperature of the reactor is regulated by a cryostat of Huber type. The temperature is measured using a Pt 100 probe which is immersed in the reactor and which is used for the regulation.
The stirrer is a stainless steel anchor stirrer. The rotational speed of the stirrer is of the order of 200 rev/min.
The reactor is also equipped with a reflux device (coil condenser) sufficiently efficient to allow the monomers to reflux without losses of product.
At the bottom of the vessel, 276.6 g of water, 3.53 g of a 40% solution in water of the surfactant (sodium salt of α-olefinsulphonate), 3.44 g of a 40% solution in water of Sipomer COPS-I and 3.30 g of t-butyl perbenzoate are introduced at ambient temperature and subsequently 4% by weight (13.5 g) of a pre-emulsified mixture 1 comprising:
The reaction mixture obtained is stirred under nitrogen for 30 minutes (200 rev/min). The temperature is subsequently raised to 75° C. and then a solution of 0.230 g of sodium persulphate dissolved in 2.1 g of water is introduced.
The mixture is brought to 80° C.
After 15 minutes, the addition of the remaining amount (96% by weight) of mixture 1 described above is begun.
The addition is continued for 100 minutes.
Simultaneously, for 100 minutes, a mixture 2 comprising:
0.92 g of sodium persulphate,
22.0 g of water,
is added.
After complete addition of the various ingredients, the temperature of the emulsion is brought to 90° C. over 15 minutes and the copolymer emulsion obtained is maintained at 90° C. for one hour.
A sample (˜5 g) is then withdrawn and the particle size of the latex is measured by light scattering (Malvern Zetasizer). The mean diameter obtained is equal to 95 nm.
An analysis of the sample by gravimetric measurement of the dry extract reveals that the conversion of the monomers is greater than 97%.
The starting material is the emulsified copolymer obtained above in stage 1 after having withdrawn ˜5 g of it for analysis and without having halted the heating.
A pre-emulsified mixture 3 comprising:
The addition is continued for 210 minutes.
Simultaneously, the addition is begun of a mixture 4 comprising:
1.65 g of erythorbic acid,
11.0 g of water.
The addition is continued for 240 minutes.
The system is maintained at 90° C. for an additional hour.
Subsequently, the emulsion is cooled to ˜25° C. over 1 hour.
A sample (˜5 g) is then withdrawn and the particle size of the latex is measured by light scattering (Malvern Zetasizer). The mean diameter obtained is equal to 120 nm.
An analysis of the sample by gas chromatography reveals that the conversion of the monomers is greater than 98%.
A DMA analysis (measuring conditions: 861e DMA device from Mettler/Toledo; temperature scanning test from −60 to 120° C. at 3°/min; extension geometry, with test specimens of 10.5×5×0.5 (in mm), with oscillatory stress of 2 μm in amplitude at a frequency of 1 Hz) reveals that the copolymer obtained is characterized by two glass transition temperatures, Tg1=−15° C. and Tg2=+53° C.
The pH of the latex is adjusted at ambient temperature to a value of approximately 7.5 by adding thereto a 10% aqueous sodium hydroxide solution over one hour.
At the bottom of the vessel, 276.6 g of water, 3.53 g of a 40% solution in water of the surfactant (sodium salt of α-olefinsulphonate), 3.44 g of a 40% solution in water of Sipomer COPS-I and 3.30 g of t-butyl perbenzoate are introduced at ambient temperature and subsequently 4% by weight (16.8 g) of a pre-emulsified mixture 1 comprising:
The reaction mixture obtained is stirred under nitrogen for 30 minutes (200 rev/min). The temperature is subsequently raised to 75° C. and then a solution of 0.290 g of sodium persulphate dissolved in 2.60 g of water is introduced.
The mixture is brought to 80° C.
After 15 minutes, the addition of the remaining amount (96% by weight) of mixture 1 described above is begun.
The addition is continued for 120 minutes.
Simultaneously, for 120 minutes, a mixture 2 comprising:
After complete addition of the various ingredients, the temperature of the emulsion is brought to 90° C. over 15 minutes and the copolymer emulsion obtained is maintained at 90° C. for one hour.
A sample (˜5 g) is then withdrawn and the particle size of the latex is measured by light scattering (Malvern Zetasizer). The mean diameter obtained is equal to 118 nm.
An analysis of the sample by gravimetric measurement of the dry extract reveals that the conversion of the monomers is greater than 97%.
The starting material is the emulsified copolymer obtained above in stage 1 after having withdrawn ˜5 g of it for analysis and without having halted the heating.
A pre-emulsified mixture 3 comprising:
The addition is continued for 180 minutes.
Simultaneously, the addition is begun of a mixture 4 comprising:
The addition is continued for 210 minutes.
The system is maintained at 90° C. for an additional hour.
Subsequently, the emulsion is cooled to ˜25° C. over 1 hour.
A sample (˜5 g) is then withdrawn and the particle size of the latex is measured by light scattering (Malvern Zetasizer). The mean diameter obtained is equal to 141 nm.
An analysis of the sample by gas chromatography reveals that the conversion of the monomers is greater than 98%.
The pH of the latex is adjusted at ambient temperature to a value of approximately 7.5 by adding thereto a 10% aqueous sodium hydroxide solution over one hour.
At the bottom of the vessel, 276.6 g of water, 3.53 g of a 40% solution in water of the surfactant (sodium salt of α-olefinsulphonate), 3.44 g of a 40% solution in water of Sipomer COPS-1 and 3.30 g of t-butyl perbenzoate are introduced at ambient temperature and subsequently 4% by weight (16.8 g) of a pre-emulsified mixture 1 comprising:
The reaction mixture obtained is stirred under nitrogen for 30 minutes (200 rev/min). The temperature is subsequently raised to 75° C. and then a solution of 0.290 g of sodium persulphate dissolved in 2.60 g of water is introduced.
The mixture is brought to 80° C.
After 15 minutes, the addition of the remaining amount (96% by weight) of mixture 1 described above is begun.
The addition is continued for 120 minutes.
Simultaneously, for 120 minutes, a mixture 2 comprising:
After complete addition of the various ingredients, the temperature of the emulsion is brought to 90° C. over 15 minutes and the copolymer emulsion obtained is maintained at 90° C. for one hour.
A sample (˜5 g) is then withdrawn and the particle size of the latex is measured by light scattering (Malvern Zetasizer). The mean diameter obtained is equal to 117 nm.
An analysis of the sample by gravimetric measurement of the dry extract reveals that the conversion of the monomers is greater than 97%.
The starting material is the emulsified copolymer obtained above in stage 1 after having withdrawn ˜5 g of it for analysis and without having halted the heating.
A pre-emulsified mixture 3 comprising:
The addition is continued for 180 minutes.
Simultaneously, the addition is begun of a mixture 4 comprising:
The addition is continued for 210 minutes.
The system is maintained at 90° C. for an additional hour.
Subsequently, the emulsion is cooled to ˜25° C. over one hour.
A sample (˜5 g) is then withdrawn and the particle size of the latex is measured by light scattering (Malvern Zetasizer). The mean diameter obtained is equal to 142 nm.
An analysis of the sample by gas chromatography reveals that the conversion of the monomers is greater than 98%.
The pH of the latex is adjusted at ambient temperature to a value of approximately 7.5 by adding thereto a 10% aqueous sodium hydroxide solution over one hour.
At the bottom of the vessel, 241.7 g of water, 3.21 g of a 40% solution in water of the surfactant (sodium salt of alkylsulphonic acid) and 3.13 g of a 40% solution in water of Sipomer COPS-I are introduced at ambient temperature and subsequently 14% by weight (29.9 g) of a mixture 1 comprising:
The reaction mixture obtained is stirred under nitrogen for 30 minutes (200 rev/min). The temperature is subsequently raised to 75° C. and then a solution of 0.350 g of sodium persulphate dissolved in 3.5 g of water is introduced.
The mixture is brought to 80° C.
After 15 minutes, the addition of the remaining amount (86% by weight) of mixture 1 described above is begun.
The addition is continued for 90 minutes.
Simultaneously, a mixture 2 comprising:
After complete addition of the mixtures 1 and 2, 3.00 g of t-butyl perbenzoate are added. Subsequently, the temperature of the emulsion is maintained at 80° C. for one hour.
A sample (˜5 g) is then withdrawn and the particle size of the latex is measured by light scattering (Malvern Zetasizer). The mean diameter obtained is equal to 95 nm.
A DSC analysis (the measuring conditions: Mettler 822E/200W DSC; thermal cycle: 20° C./min; temperature range: −50° C. to 120° C.; controlled atmosphere: nitrogen; aluminium pan: standard 40 μl) reveals that the copolymer obtained is characterized by a glass transition temperature Tg=−17° C.
An analysis of the sample by gravimetric measurement of the dry extract reveals that the conversion of the monomers is greater than 97%.
The starting material is the emulsified copolymer obtained above in stage 1 after having withdrawn ˜5 g of it for analysis and without having halted the heating.
A pre-emulsified mixture 3 comprising:
The addition is continued for 150 minutes.
Simultaneously, the addition is begun of a mixture 4 comprising:
The addition is continued for 180 minutes.
The system is maintained at 90° C. for an additional hour.
Subsequently, the emulsion is cooled to ˜25° C. over 1 hour.
A sample (˜5 g) is then withdrawn and the particle size of the latex is measured by light scattering (Malvern Zetasizer). The mean diameter obtained is equal to 130 nm.
An analysis of the sample by gas chromatography reveals that the conversion of the monomers is greater than 98%.
A DSC analysis (the measuring conditions: Mettler 822E/200W DSC; thermal cycle: 20° C./min; temperature range: −50° C. to 120° C.; controlled atmosphere: nitrogen; aluminium pan: standard 40 μl) reveals that the copolymer obtained is characterized by two glass transition temperatures, Tg1=−10° C. and Tg2=+37° C.
The pH of the latex is adjusted at ambient temperature to a value of approximately 7.5 by adding thereto a 10% aqueous sodium hydroxide solution over one hour.
At the bottom of the vessel, 276.6 g of water, 3.53 g of a 40% solution in water of the surfactant (sodium salt of α-olefinsulphonate), 3.44 g of a 40% solution in water of Sipomer COPS-I and 3.30 g of t-butyl perbenzoate are introduced at ambient temperature and subsequently 4% by weight (16.8 g) of a pre-emulsified mixture 1 comprising:
The reaction mixture obtained is stirred under nitrogen for 30 minutes (200 rev/min). The temperature is subsequently raised to 75° C. and then a solution of 0.290 g of sodium persulphate dissolved in 2.60 g of water is introduced.
The mixture is brought to 80° C.
After 15 minutes, the addition of the remaining amount (96% by weight) of mixture 1 described above is begun.
The addition is continued for 120 minutes.
Simultaneously, for 120 minutes, a mixture 2 comprising:
After complete addition of the various ingredients, the temperature of the emulsion is brought to 90° C. over 15 minutes and the copolymer emulsion obtained is maintained at 90° C. for one hour.
A sample (˜5 g) is then withdrawn and the particle size of the latex is measured by light scattering (Malvern Zetasizer). The mean diameter obtained is equal to 97 nm.
An analysis of the sample by gravimetric measurement of the dry extract reveals that the conversion of the monomers is greater than 97%.
The starting material is the emulsified copolymer obtained above in stage 1 after having withdrawn ˜5 g of it for analysis and without having halted the heating.
A pre-emulsified mixture 3 comprising:
The addition is continued for 180 minutes.
Simultaneously, the addition is begun of a mixture 4 comprising:
1.65 g of erythorbic acid,
11.0 g of water.
The addition is continued for 210 minutes.
The system is maintained at 90° C. for an additional hour.
Subsequently, the emulsion is cooled to ˜25° C. over one hour.
A sample (˜5 g) is then withdrawn and the particle size of the latex is measured by light scattering (Malvern Zetasizer). The mean diameter obtained is equal to 130 nm.
An analysis of the sample by gas chromatography reveals that the conversion of the monomers is greater than 98%.
The pH of the latex is adjusted at ambient temperature to a value of approximately 7.5 by adding thereto a 10% aqueous sodium hydroxide solution over one hour.
Use of the latexes synthesized in Examples 1 to 5 in gloss paint formulations. The paints were prepared according to the procedure described above.
For the paints obtained, the physical characteristics were determined as follows:
| Number | Date | Country | Kind |
|---|---|---|---|
| 05/08167 | Jul 2005 | FR | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/EP06/07165 | 7/20/2006 | WO | 00 | 8/13/2009 |
