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    • 专利摘要:
    The present invention relates to a process for the preparation of a polymer having a mass Mw of less than 300 000 g / mol (in particular between 1000 and 300 000 g / mol), comprising a step (E) of controlled free-radical polymerization which is brought into contact in a aqueous medium in which micelles of surfactants are dispersed: hydrophilic ethylenically unsaturated monomers present mainly in the aqueous medium; partially hydrosoluble hydrophobic monomers, ethylenically unsaturated, distinct from the preceding ones, present at least in part within the micelles of surfactants, and having a solubility in the aqueous medium at least equal to that of hexyl acrylate; at least one radical polymerization initiator; and at least one radical polymerization control agent.
    公开号:FR3018814A1
    申请号:FR1400709
    申请日:2014-03-24
    公开日:2015-09-25
    发明作者:Simon Harrisson；James Wilson
    申请人:Rhodia Operations SAS；
    IPC主号:
    专利说明:

    [0001] The present invention relates to the field of amphiphilic polymers useful in particular as modifiers for surface or interface properties. Various polymers of this type have been described, among which mention may be made of amphiphilic copolymers of the diblock type, which comprise two blocks of radically opposite natures, namely a first substantially hydrophobic block bound to a clearly hydrophilic block. Due to the presence of two very distinct blocks, these copolymers are particularly active at a surface / interface. In return, however, because of the very different nature of the two blocks, these copolymers tend to self-assemble, typically to form micelles or other objects, where the polymers are no longer available to provide surface modification. /interface. In aqueous medium for example, these polymers have a clear tendency to see their hydrophobic blocks interact strongly in the self-assembly structure which is somehow 'frozen' kinetically (the blocks are typically associated in a relatively irreversible way to the heart micelles). On the other hand, it has been described, in particular in Polymer Chemistry 2014, 5, 819, amphiphilic polymers of statistical type, less clearly polarized. These are generally polymer chains predominantly containing hydrophilic units, in which are strongly dispersed strongly hydrophobic units present in small numbers. With this type of amphiphilic polymer, the risk of self-association is lower and it is possible, in absolute terms, to modulate the overall physicochemical properties taking into account the combined presence of hydrophobic and hydrophilic units. Nevertheless, because of the statistical nature of these copolymers, it is often difficult to finely control these properties and this in particular for high mass polymers. In addition, as a general rule, statistical polymers are not anchored optimally on the surfaces or interfaces, which can notably result in a loss of performance over time, or even an insufficient efficiency for certain applications. An object of the present invention is to provide a new type of polymer that both limits the risk of self-assembly while optimizing polymer reactivity to ensure effective surface or interface modification.
    [0002] For this purpose, the present invention provides access to typically low molecular weight polymers which can be obtained according to a controlled radical polymerization process conducted under specific conditions. More specifically, according to a first aspect, the subject of the present invention is a process for the preparation of a polymer which preferably has a molecular weight in weight Mw of less than 300 000 g / mol, in particular of between 1000 and 300 000 g / mol. (This mass is, for example, greater than 100,000 g / mol, and, independently, it is advantageously less than 300,000 g / mol), comprising a polymerization step (E) in which an aqueous medium is brought into contact (M). in which micelles of surfactants are dispersed: ethylenically unsaturated M1 monomers predominantly present in the aqueous medium, hereinafter referred to as "hydrophilic monomers"; ethylenically unsaturated monomers M2 which are distinct from the hydrophilic monomers, present at least in part within the micelles of surfactants, and which have a solubility in the aqueous medium (M) at the temperature of implementation of step (E) at least equal to that of hexyl acrylate, hereinafter referred to as "partially water-soluble hydrophobic monomers"; at least one radical polymerization initiator, preferably water-soluble or water-dispersible; and at least one radical polymerization control agent. According to another aspect, the invention relates to the polymers of the type obtained according to the aforementioned method, the mass of which can be finely controlled by means of the preparation method of the invention, as well as different uses of these polymers, described in more detail. hereinafter, in particular as surface modifiers, surfactants, dispersants or associative thickeners. The polymers as obtained according to the above-mentioned step (E) have a very specific structure which combines the advantages of a block structure and of a statistical structure: due to the use of surfactant micelles and a control agent, step (E) allows a controlled orientation of the distribution of the monomers, with a structure of the "multiblock" type, namely with alternating alternating hydrophobic and hydrophilic zones, with a direct effect on the polymer efficiency (surface / interface modification, surface / interface anchoring). This "multiblock" type structure is superior to a statistical structure, wherein the partially water-soluble hydrophobic monomer units are separated by long segments of hydrophilic monomers. On the contrary, according to the invention, the effect of partially water-soluble hydrophobic monomer units is optimized, which is reflected in particular in terms of improving the anchoring strength of the polymers; in view of the use of partially water-soluble monomers M2, step (E) also leads to a dispersion of hydrophobic units in the hydrophilic zones, with an associated modulation effect which is close to that authorized with statistical polymerization control of this modulation is further improved by the use of the control agent. It has also been demonstrated in the context of the present invention that the conditions of step (E) make it possible to obtain the polymers of controlled mass, which can in particular be chosen low, with typically a lower mass (Mw). at 300 000 g / mol or even 250 000 g / mol. For the purposes of the present description, the term "molecular weight", or "molar mass", denoted by Mw, means the average mass of a population of polymers defined by the average of the molecular weights of the polymer chains weighted by the mass of the each length. In practice, the Mw of a polymer population can typically be measured by chromatography, typically by GPC or HPLC. Interesting conditions of implementation of step (E) are described in more detail below. Monomers M2 These are ethylenically unsaturated monomers having a solubility in water sufficient for M2 monomers to be present in a significant way in the aqueous medium (M) of step (E), but nevertheless sufficiently low for that a non-negligible part (and in general clearly majority) of these monomers M2 is present within the micelles. For this purpose, the monomers M2 have a solubility in the aqueous medium (M) of at least or equal to that of a hexyl acrylate, preferably greater than or equal to 100 ppm, that is to say at least 0.01 g / 100 g in water at the temperature of implementation of step (E), this solubility in the aqueous medium (M) preferably being greater than or equal to 500 ppm (0.05 g / 100g in water at the application temperature). On the other hand, it is preferable that the solubility of the monomers M2 the aqueous medium (M) remains below 20,000 ppm. As a general rule, it is possible to use monomers M2 whose solubility in water is between the aforementioned values (typically between 100 ppm and 20,000 ppm), but it is understood that monomers having a solubility in water of Outside this range may be employed: depending on the exact nature of the aqueous medium of step (E); possible presence of additives or solvents in particular), the solubility in the aqueous medium (M) may differ significantly with respect to the solubility in water. Advantageously, the monomers M2 have a log P less than or equal to 3.3 and this LogP advantageously remains in general greater than or equal to 1.2. As used herein, LogP is the base logarithm of the ratio of the concentrations of the test substance in octanol and water. By way of nonlimiting example of monomer M2 that can be used according to the invention, mention may be made in particular of: vinylaromatic monomers such as styrene, alpha-methylstyrene, parachloromethylstyrene, vinyltoluene, 2-methylstyrene, 4-methylstyrene, 2- (n-butyl) styrene, p-styrene carboxylic acid (p-styrene carboxylic acid is particularly useful); esters of mono-, dicarboxylic acid a, 13 ethylenically unsaturated with C 2 -C 12 -alkanols, for example, methyl ethacrylate, ethyl (meth) acrylate, ethyl ethacrylate, meth) n-propyl acrylate, isopropyl (meth) acrylate, n-butyl (meth) acrylate, sec-butyl (meth) acrylate, tert-butyl (meth) acrylate, ethacrylate of tert-butyl, hexyl (meth) acrylate, n-heptyl (meth) acrylate, n-octyl (meth) acrylate, 1,1,3,3-tetramethylbutyl (meth) acrylate, (meth) ethylhexyl acrylate, n-nonyl (meth) acrylate, n-decyl (meth) acrylate, n-decyl (meth) acrylate, tridecyl (meth) acrylate, (meth) myristyl acrylate, pentadecyl (meth) acrylate, palmityl (meth) acrylate, heptadecyl (meth) acrylate, nonadecyl (meth) acrylate, arachinyl (meth) acrylate, (meth) acrylate behenyl, lignoceryl (meth) acrylate, cerotinyl (meth) acrylate, (meth) acrylate, melissinyl, palmitoleoyl (meth) acrylate, oleyl (meth) acrylate, linolyl (meth) acrylate, linolenyl (meth) acrylate, stearyl (meth) acrylate, lauryl (meth) acrylate and their mixtures; esters of vinyl or allyl alcohol with C 1 -C 12 monocarboxylic acids, for example, vinyl formate, vinyl acetate, vinyl butyrate, vinyl laurate, vinyl propionate, vinyl versatate and mixtures thereof; ethylenically unsaturated nitriles, such as acrylonitrile, methacrylonitrile and mixtures thereof; α, β-ethylenically unsaturated mono- and di-carboxylic acid esters with C 4 -C 12 alkanediols, for example, 3-hydroxybutyl acrylate, 3-hydroxybutyl methacrylate, 4-hydroxybutyl acrylate, 4-hydroxybutyl methacrylate, 6-hydroxyhexyl acrylate, 6-hydroxyhexyl methacrylate, 3-hydroxy-2-ethylhexyl acrylate and 3-hydroxy-2-ethylhexyl methacrylate; primary amides of α, β-ethylenically unsaturated mono- and di-carboxylic acids and N-alkyl and N, N-dialkyl derivatives, such as N-propyl (meth) acrylamide, N- (n-butyl); (meth) acrylamide, N- (tert-butyl) (meth) acrylamide, N- (n-octyl) (meth) acrylamide, N- (1,1,3,3-tetramethylbutyl) (meth) acrylamide , N-ethylhexyl (meth) acrylamide, N- (n-nonyl) (meth) acrylamide, N- (n-decyl) (meth) acrylamide, N- (n-undecyl) (meth) acrylamide, N-vinyllactams and its derivatives such as N-vinyl-5-ethyl-2-pyrrolidone, Nvinyl-6-methyl-2-piperidone, N-vinyl-6-ethyl-2-piperidone, N-vinyl 7-methyl-2-caprolactam and N-vinyl-7-ethyl-2-caprolactam; esters of α, β-ethylenically unsaturated mono- and di-carboxylic acids with amino alcohols, for example, N, N-dimethylaminocyclohexyl (meth) acrylate; α, β-ethylenically unsaturated mono- and di-carboxylic acid amides with diamines comprising at least one primary or secondary amino group, for example, N [2- (diethylamino) ethylacrylamide, N- [4- (dimethylamino) cyclohexyl] acrylamide, N- [4- (dimethylamino) cyclohexyl] methacrylamide; and C 2 -C 8 monoolefins such as ethylene, propylene, isobutylene and nonaromatic hydrocarbons comprising at least two conjugated double bonds, for example, isoprene or butadiene. According to a preferred embodiment, the monomers M2 used according to the invention are chosen from: unsaturated alpha-beta esters of C1-C8 alkyl, preferably of C2-6 alkyl, in particular acrylates and alkyl methacrylate, such as acrylates and methyl methacrylate, ethyl, butyl, hexyl; alpha-beta unsaturated C1-C8alkyl alkyl, preferably C2-C6alkyl, especially alkyl acrylamide and methacrylamide, such as methyl, ethyl, butyl, hexyl; vinyl or allyl alcohol esters of saturated carboxylic acids such as acetate, propionate, versatate, vinyl or allyl; alpha-beta unsaturated nitriles containing from 3 to 6 carbon atoms, such as acrylonitrile; p-styrene carboxylic acid; alpha olefins and conjugated dienes; mixtures and combination of two or more of the aforementioned monomers. Preferably, the partially water-soluble hydrophobic monomers of step (E) are chosen from ethyl (meth) acrylate, ethyl ethacrylate, n-propyl (meth) acrylate, (meth) acrylate and isopropyl, n-butyl (meth) acrylate, sec-butyl (meth) acrylate, tert-butyl (meth) acrylate, tert-butyl ethacrylate or n-hexyl acrylate ,. The surfactant micelles The surfactant micelles containing the M2 monomers employed in step (E) can be based on any suitable surfactant. By way of nonlimiting example, it is possible, for example, to use one or more surfactants chosen from the following list: The anionic surfactants may be chosen from: alkyl ester sulfonates, for example of formula R-CH (SO 3 M) - CH 2 000 R ', or alkyl ester sulphates, for example of formula R-CH (OSO 3 M) -CH 2 COOR', where R represents an alkyl radical at 8 -020, preferably at 0-10-016, R 'a C 1 -C 6 alkyl radical, preferably C1-C3 and M an alkaline earth cation, for example sodium, or the ammonium cation. Mention may in particular be made of methyl ester sulfonates whose radical R is 014-016; alkylbenzenesulfonates, more particularly C9-C20, primary or secondary alkylsulfonates, especially at 08-022, alkylglycerol sulfonates; alkyl sulphates, for example of formula ROSO 3 M, where R represents an alkyl or hydroxyalkyl radical at 0-10-024, preferably at 0-12-020; M a cation of the same definition as above; alkyl ether sulfates, for example of formula R0 (OA) SO 3 M, where R represents an alkyl or hydroxyalkyl radical at 0-10-024, preferably at C12-C20; OA representing an ethoxylated and / or propoxylated group; M representing a cation of the same definition as above, n generally ranging from 1 to 4, such as, for example, lauryl ether sulfate with n = 2; alkylamide sulphates, for example of formula RCONHR'OSO3M where R represents an alkyl radical at 02-022, preferably at 06-020, R 'at an alkyl radical at 02-03, M representing a cation of the same definition as above as well as their polyalkoxylated derivatives (ethoxylated and / or propoxylated) (alkylamidoether sulphates; saturated or unsaturated fatty acid salts, for example as those in 08-024, preferably in 014-020 and an alkaline earth cation , N-acyl N-alkyltaurates, alkylisethionates, alkylsuccinamates and alkylsulfosuccinates, alkyl glutamates, monoesters or diesters of sulfosuccinates, N-acyl sarcosinates, polyethoxycarboxylates, mono and di phosphate esters, for example of the following formula: (R) x-P (= O) (OH) x or R represents an alkyl, alkylaryl, arylalkyl or aryl radical, optionally polyalkoxylated, x and x 'being equal to 1 or 2, with the proviso that the sum of x and x 'is equal to 3, M representing an alk cation The nonionic surfactants may be chosen from: alkoxylated fatty alcohols; for example, laureth-2, laureth-4, laureth-7, oleth20, alkoxylated triglycerides, alkoxylated fatty acids, alkoxylated sorbitan esters, alkoxylated fatty amines, alkoxylated di (phenyl-ethyl) phenols, and the like. alkoxylated alkyl phenols, the products resulting from the condensation of ethylene oxide with a hydrophobic compound resulting from the condensation of propylene oxide with propylene glycol, such as marketed Pluronic by BASF; the products resulting from the condensation of ethylene oxide the compound resulting from the condensation of propylene oxide with ethylenediamine, such as Tetronic marketed by BASF; alkylpolyglycosides such as those described in US 4565647 or alkylglucosides; fatty acid amides, for example C8-C20 fatty acids, in particular monoalkanolamides of fatty acids, for example cocamide MEA or cocamide MIPA; The amphoteric surfactants (true amphoteric compounds comprising an ionic group and a potentially ionic group of opposite charge, or zwitterionic compounds comprising simultaneously two opposite charges) may be: betaines in general, in particular carboxybetaines, for example lauryl betaine (Mirataine BB of the company) Rhodia) or octylbetaine or cocobetaine (Mirataine BB-FLA from Rhodia); amidoalkyl betaines, such as cocamidopropyl betaine (CAPB) (Mirataine BDJ from Rhodia or Mirataine BET C-30 from Rhodia); sulfo-betaines or sultaines such as cocamidopropyl hydroxy sultaine (Mirataine CBS from Rhodia); alkylamphoacetates and alkylamphodiacetates, such as for example comprising a coconut chain, lauryl (Miranol C2M Conc NP, C32, L32 in particular, from Rhodia); alkylamphopropionates or alkylamphodipropionates (Miranol C2M SF); alkyl amphohydroxypropyl sultaines (Miranol CS), the oxide of alkyl amines, for example lauramine oxide (INCI); The cationic surfactants may be the salts of primary, secondary or tertiary fatty amines, optionally polyethoxylated, quaternary ammonium salts such as chlorides or bromides tetraalkylammonium, alkylamidoalkylammonium, trialkylbenzylannmonium, trialkylhydroxyalkylammonium, or alkylpyridinium , imidazoline derivatives, cationic amine oxides. An example of a cationic surfactant is cetrimonium chloride or bromide. The surfactants used according to the present invention may be block copolymers containing at least one hydrophilic block and at least one hydrophobic block distinct from the hydrophilic block, advantageously obtained according to a polymerization process in which: (a0) at least one hydrophilic monomer (hydrophobic monomer), at least one source of free radicals and at least one radical polymerization control agent of the type S (C = S) are brought together in an aqueous phase; -; (a1) contacting the polymer obtained at the end of step (a0) with at least one hydrophobic monomer (respectively hydrophilic) distinct from the monomer employed in step (a0) and at least one source of free radicals ; whereby a diblock copolymer is obtained.
    [0003] Polymers of the triblock type, or more comprising blocks, may optionally be obtained by carrying out, after step (a1), a step (a2) in which the polymer obtained is contacted at the end of the step (a1) with at least one monomer separate from the monomer employed in step (a1) and at least one source of free radicals; and more generally, by implementing (n + 1) steps of the type of the above steps (a1) and (a2) and n is an integer ranging typically from 1 to 3, where in each step (an), with nkl: the polymer obtained at the end of step (a1) is brought into contact with at least one monomer distinct from the monomer employed in step (an4 and at least one source of free radicals. The copolymers of the type described in WO003068827, WO003068848 and WO2005 / 021612 are disclosed according to one embodiment, the monomers M2 are within surfactant micelles formed in step (E) where this surfactant is introduced at a higher concentration. In a particular embodiment, the monomers M2 may be monomers which, in themselves, have the property of forming micelles without the need to add additional surfactants (monomers known as "auto-micelle" monomers). -micellizable "in the su According to this particular embodiment, the surfactant employed may be the self-micellable hydrophobic monomer itself, employed without any other surfactant, although the presence of such an additional surfactant is not excluded. Thus, for the purposes of the present description, when reference is made to monomers present within surfactant micelles, this concept also encompasses (i) hydrophobic monomers present in surfactant micelles distinct from these monomers than (ii) ) "automicellisable" monomers forming by themselves micelles in an aqueous medium. The two modes (i) and (ii) above are compatible and can coexist (hydrophobic monomers within micelles formed by another self-micellizable monomer for example, or else micelles comprising a combination of surfactants and automicellisable monomers). The aqueous medium (M) The aqueous medium (M) used in step (E) is a medium comprising water, preferably at least 50% by weight, or even at least 80%, for example at least 90%, or at least 95%. This aqueous medium may optionally comprise other solvents than water, for example a water-miscible alcohol. Thus, the medium (M) may be, for example, a hydroalcoholic mixture. According to one possible variant, the medium (M) may comprise other solvents, preferably at a concentration where said solvent is miscible with water, which may in particular make it possible to reduce the amount of stabilizing surfactants employed. Thus, for example, the medium (M) may comprise pentanol, or any other additive for modulating the aggregation number of the surfactants. In general, it is preferable for the medium (M) to be a continuous phase of water and consisting of one or more solvents and / or additives that are miscible with each other and in water at the concentrations in which they are used. The radical polymerization control agent For the purposes of the present description, the term "radical polymerization control agent" is intended to mean a compound capable of extending the life time of the growing polymer chains in a polymerization reaction and of conferring the polymerization a living or controlled character. This control agent is typically a reversible transfer agent as used in the controlled radical polymerizations designated under the terminology RAFT or MADIX, which typically implement a reversible addition-fragmentation transfer method, such as those described for example in WO96 / 30421, WO 98/01478, WO 99/35178, WO 98/58974, WO 00/75207, WO 01/42312, WO 99/35177, WO 99/31144, FR2794464 or WO 02/26836.
    [0004] According to an interesting embodiment, the radical polymerization control agent employed in step (E) is a compound which comprises a thiocarbonylthio group -S (C = S) -. Thus, for example, it may be a compound which comprises at least one xanthate group (carrying -SC = S-O-), for example one or two xanthates. According to one embodiment, the compound comprises several xanthates. Other types of control agent can be envisaged (for example of the type used in ATRP or NMP). According to one particular embodiment, the control agent employed in step (E) may be a polymer chain resulting from a controlled radical polymerization and carrying a group capable of controlling a radical polymerization (so-called "living" polymer chain ", Of a type well known in itself). Thus, for example, the control agent can be a polymer chain (preferably hydrophilic or hydrodispersible) functionalized at the end of the chain by a xanthate group or more generally comprising a group - SC = S-, for example obtained according to MADIX technology. .
    [0005] Alternatively, the control agent used in step (E) is a non-polymeric compound bearing a group that controls the radical polymerization, in particular a thiocarbonylthio -S (C = S) - group. According to a particular variant, the radical polymerization control agent employed in step (E) is a polymer, advantageously an oligomer, of water-soluble or water-dispersible nature and carrying a thiocarbonylthio -S (C = S) - group, for example, a xanthate group -SC = S-O-). This polymer, capable of acting both as a control agent for the polymerization and as a monomer in step (E), is also referred to as "prepolymer" in the following description. Typically, this prepolymer is obtained by radical polymerization of hydrophilic monomers in the presence of a control agent bearing a thiocarbonylthio -S (C = S) - group, for example a xanthate. Thus, for example, according to an interesting embodiment which is illustrated at the end of the present description, the control agent used in step (E) may advantageously be a prepolymer carrying a thiocarbonylthio-S group. (C = S) -, for example a xanthate group -SC = S-O-, obtained at the end of a controlled radical polymerization step (E °) prior to step (E). In this step (E °), one can typically contact hydrophilic monomers (MO), preferably identical to those used in step (E); a radical polymerization initiator; and a control agent carrying a thiocarbonylthio group -S (C = S) -, for example a xanthate.
    [0006] According to one embodiment, the radical polymerization control agent is a water-soluble or water-dispersible oligomer carrying a thiocarbonylthio -S (C = S) - group, for example a xanthate -SC = S-O group. which is soluble (or dispersible) in the aqueous medium (M) employed in step (E); and / or - is not adapted to penetrate the micelles of the micellar solution. According to one particular embodiment, the control agent is both soluble (or dispersible) in the aqueous medium (M), and able to penetrate in part into the micelles of the micellar solution. The implementation of step (E °) previously mentioned in step (E) allows, schematically, to hydrophilize a large number of control agents carrying thiocarbonylthio functions (for example xanthate, which are rather hydrophobic in nature), by converting them soluble or dispersible polymers in the medium (M) of step (E). Preferably, a pre-polymer synthesized in step (E °) has a short polymer chain, for example comprising a sequence of less than 50, or even less than 25 monomer units, for example between 2 and 15. According to one embodiment, In a preferred embodiment, the monomers (MO) are (meth) acrylic acid monomers (whereby the control agent is a poly (meth) acrylic acid carrier of at least one xanthate group and the polymer having the specific structure obtained. according to step (E), furthermore having a poly (meth) acrylic acid block bound to one of its ends, the control agent used in step (E) or, where appropriate, in the Step (E °) of the process of the invention is advantageously a compound bearing a thiocarbonylthio group -S (C = S) .- Most often, the control agent carries a single thiocarbonylthio group. particular embodiment, the control agent may carry more than one group For example, this control agent may correspond to formula (A) below: ## STR2 ## in which: Z represents: a hydrogen atom, a chlorine atom, . an optionally substituted alkyl radical, optionally substituted aryl, an optionally substituted heterocycle, an optionally substituted alkylthio radical, an optionally substituted arylthio radical, an optionally substituted alkoxy radical, an optionally substituted aryloxy radical, an optionally substituted amino radical, an optionally substituted hydrazine radical, an optionally substituted alkoxycarbonyl radical, an optionally substituted aryloxycarbonyl radical, an optionally substituted carboxy, acyloxy radical, an optionally substituted aroyloxy radical, an optionally substituted carbamoyl radical, a cyano radical, a dialkyl- or diaryl-phosphonato radical, a dialkyl phosphinato or diaryl phosphinato radical, or a polymer chain, and R1 represents: an optionally substituted alkyl, acyl, aryl, aralkyl, alkene or alkyne group, a carbon ring or heterocycle, saturated or unsaturated, optionally substituted aromatic, or. a polymer chain, preferably hydrophilic or hydrodispersible when the agent is used in step (E).
    [0007] The groups R1 or Z, when substituted, may be substituted with optionally substituted phenyl groups, optionally substituted aromatic groups, saturated or unsaturated carbon rings, saturated or unsaturated heterocycles, or alkoxycarbonyl or aryloxycarbonyl groups ( -COOR), carboxy (-COOH), acyloxy (-O2CR), carbamoyl (-CONR2), cyano (-CN), alkylcarbonyl, alkylarylcarbonyl, arylcarbonyl, arylalkylcarbonyl, phthalimido, maleimido, succinimido, amidino, guanidimo, hydroxy ( OH), amino (-NR2), halogen, perfluoroalkyl CnF2ni-1, allyl, epoxy, alkoxy (-OR), S-alkyl, S-aryl, groups having a hydrophilic or ionic character, such as the alkaline salts of carboxylic acids, alkali metal salts of sulfonic acid, polyalkylene oxide chains (PEO, POP), cationic substituents (quaternary ammonium salts), R representing an alkyl or aryl group, or a polymer chain.
    [0008] For the control agents of formula (A) used in step (E), it is generally preferred that the group R 1 is hydrophilic in nature. Advantageously, it is a water-soluble or water-dispersible polymer chain. The group R1 may alternatively be amphiphilic, namely present both a hydrophilic and lipophilic character. It is preferable that R1 is not hydrophobic.
    [0009] Regarding the control agents of formula (A) used in step (E °), R1 may typically be a substituted or unsubstituted alkyl group, preferably substituted. A control agent of formula (A) used in step (E °) may nevertheless comprise other types of groups R 1, in particular a ring or a polymer chain. Alkyl, acyl, aryl, aralkyl or optionally alkyne groups substituted compounds generally have 1 to 20 carbon atoms, preferably 1 to 12, and more preferably 1 to 9 carbon atoms. They can be linear or branched. They may also be substituted by oxygen atoms, in particular esters, sulfur or nitrogen atoms. Among the alkyl radicals, mention may especially be made of the methyl, ethyl, propyl, butyl, pentyl, isopropyl, tert-butyl, pentyl, hexyl, octyl, decyl or dodecyl radical. The alkyne groups are radicals generally of 2 to 10 carbon atoms, they have at least one acetylenic unsaturation, such as the acetylenyl radical. The acyl group is a radical generally having from 1 to 20 carbon atoms with a carbonyl group. Among the aryl radicals, there may be mentioned the phenyl radical, optionally substituted in particular by a nitro or hydroxyl function.
    [0010] Among the aralkyl radicals, mention may especially be made of the benzyl or phenethyl radical, optionally substituted in particular by a nitro or hydroxyl function. When R1 or Z is a polymer chain, this polymer chain may be derived from a radical or ionic polymerization or from a polycondensation.
    [0011] Advantageously, as control agent for step (E), as well as for step (E °), if appropriate, compounds carrying a xanthate function -S (C = S) O-, trithiocarbonate, dithiocarbamate, or dithiocarbazate, for example compounds bearing an O-ethyl xanthate function of formula -S (C = S) OCH 2 CH 3.
    [0012] When step (E °) is conducted, it is particularly advantageous to use as control agents in this step a compound selected from xanthates, trithiocarbonates, dithiocarbamates, or dithiocarbazates. Xanthates are particularly interesting, particularly those carrying a 0-ethyl xanthate -S (C = S) OCH2CH3 function, such as O-ethyl-S- (1-methoxycarbonylethyl) xanthate (CH3CH (CO2CH3)) S (C = S) 0ET. Another possible control agent in step (E °) is dibenzyltrithiocarbonate of formula PhCH2S (C = S) SCH2Ph (where Ph = phenyl). The living prepolymers obtained in step (E °) using the aforementioned control agents are particularly interesting for the conduct of step (E). M1 Monomers Typically, M1 monomers employed in the process of the invention may comprise monomers chosen from: ethylenically unsaturated carboxylic acids, sulfonic acids and phosphonic acids, and / or its derivatives such as acrylic acid (AA ), methacrylic acid, ethacrylic acid, α-chloroacrylic acid, crotonic acid, maleic acid, maleic anhydride, itaconic acid, citraconic acid, mesaconic acid , glutaconic acid, aconitic acid, fumaric acid, monoethylenically unsaturated dicarboxylic acid monoesters having 1 to 3, preferably 1 to 2, carbon atoms, for example, monomethyl maleate, acid vinylsulfonic acid, (meth) allylsulfonic acid, sulfoethyl acrylate, sulfoethyl methacrylate, sulfopropyl acrylate, sulfopropyl methacrylate, 2-hydroxy-3-acryloyloxypropylsulfonic acid, 2-hydroxy-acid 3- methacrylate alkyloxypropylsulfonic acid, styrenesulfonic acids, 2-acrylamido-2-methylpropanesulfonic acid, vinylphosphonic acid, α-methyl vinylphosphonic acid and allylphosphonic acid; α, β-ethylenically unsaturated mono- and di-carboxylic acid esters with C2-C3-alkanediols, for example, 2-hydroxyethyl acrylate, 2-hydroxyethyl methacrylate, 2-hydroxyethyl ethacrylate, 2-hydroxypropyl acrylate, 2-hydroxypropyl methacrylate, 3-hydroxypropyl acrylate, 3-hydroxypropyl methacrylate and polyalkylene glycol (meth) acrylates; α, β-ethylenically unsaturated monocarboxylic acid amides and their N-alkyl and N, N-dialkyl derivatives such as acrylamide, methacrylamide, N-methyl (meth) acrylamide, N-ethyl (meth) acrylamide, N-propyl (meth) acrylamide, N, N-dimethyl (meth) acrylamide, N, N-diethyl (nneth) acrylamide, morpholinyl (meth) acrylamide, and metholyl acrylamide (acrylamide and N, N-dimethyl (meth) acrylamide is particularly interesting); N-vinyllactams and its derivatives, for example, N-vinylpyrrolidone, N-vinylpiperidone; open-chain N-vinylamide compounds, for example Nvinylformamide, N-vinyl-N-methylformamide, N-vinylacetamide, N-vinylN-methylacetamide, N-vinyl-N-ethylacetamide, N-vinylpropionamide, Nvinyl-N-methylpropionamide and N-vinylbutyramide; esters of α-ethylenically unsaturated mono- and di-carboxylic acids with amino alcohols, for example, N, N-dimethylaminomethyl (meth) acrylate, N, N-dimethylaminoethyl (meth) acrylate, N acrylate, N-diethylaminoethyl, and N, N-dimethylaminopropyl (meth) acrylate, their acid addition salts and quaternization products, the alkyl employed herein being preferably C1-C3-alkyl or benzyl; α, β-ethylenically unsaturated mono- and di-carboxylic acid amides with diamines comprising at least one primary or secondary amino group, such as N- [2- (dimethylamino) ethyl] acrylamide, N [2- (dimethylamino) ethyl] methacrylamide, N- [3- (dimethylamino) propyl] acrylamide, N43- (dimethylamino) propyl] methacrylamidates N-diallylamines, N, N-diallyl-Nalkylamines, their addition salts acid and their quaternization products, the alkyl employed herein being preferably C1-C3-alkyl or benzyl; the compounds of N, N-diallyl amine and N, N-diallyl-N, N-dimethylammonium, for example chlorides and bromides; substituted vinyl and allyl nitrogen heterocycles, for example, Nvinylimidazole, N-vinyl-2-methylimidazole, substituted heteroaromatic compounds of vinyl and allyl, for example, 2- and 4-vinylpyridine, 2 and 4-allylpyridine, and their salts; - sulfobetaines; and mixtures and combination of two or more of the aforementioned monomers. According to a particular embodiment, these monomers may in particular comprise acrylic acid (AA). According to one possible embodiment, the monomers are all acrylic acids, but it is also conceivable to use as monomers a mixture comprising, inter alia, acrylic acid, in admixture with other hydrophilic monomers. According to an interesting embodiment, the monomers M1 of step (E) comprise (meth) acrylic acid monomers and / or (meth) acrylamido monomers. As used herein, the term "(meth) acrylic acid" includes methacrylic acid, acrylic acid and mixtures thereof. In the same way, for the purposes of the present description, the term "(meth) acrylate" includes methacrylate, acrylate and mixtures thereof.
    [0013] In the same way, for the purposes of the present description, the term "(meth) acrylamide / (meth) acrylamido", includes methacrylamide / methacrylamido, acrylamide / acrylamido and mixtures thereof. Monomers containing acid groups may be used for the polymerization in the form of the free acid or in the partially or completely neutralized form. For the neutralization, it is possible to use, for example, KOH, NaOH, ammonia or other base. According to a particular embodiment, the M1 monomers employed in the process of the invention are acrylic acid and / or methacrylic acid monomers, optionally wholly or partly in the form of salts. According to another embodiment, the monomers used in step (E) comprise (and typically consist of) (meth) acrylamide monomers, or more generally (meth) acrylamido monomers, including: acrylamido monomers, namely, acrylamide, its derivative sulfonate (AMPS), quaternary ammonium (APTAC) and sulfopropyl dimethylammonium propyl acrylamide. (AMPS, 2-acryloylamino-2-methylpropane-1-sulphonic acid, is particularly interesting); methacrylamido monomers, such as, sulfopropyl dimethylammonium propyl methacrylamide (SPP), sulfohydroxypropyl dimethyl ammonium propyl methacrylamido. Regardless of their exact nature, the monomers of step (E) can be carried out at relatively high concentrations, typically at concentrations that would be sufficient to provide gel formation if step (E) was driving in the absence of a screening officer. Typically, the initial concentration of monomers in the reaction medium of step (E) may be up to 40% by weight, or even up to 50% by weight, this concentration generally remaining below 35% by mass relative to to the total mass of the reaction medium. Moreover, this concentration is preferably at least 0.1% by weight, and typically at least 0.3% by weight. For example, the initial concentration of monomers in the reaction medium of step (E) is between 0.5% and 30%, especially between 1 and 20% by weight relative to the total mass of the reaction medium. According to a specific embodiment, the monomers M1 employed in step (E) are thermosensitive macromonomers, insoluble in water beyond a certain temperature (ie having a cloud point or cloud point). English), but soluble at a lower temperature, the step (E) being conducted at a temperature below the cloud point temperature. Macromonomers of this type typically have a polymerizable function of the (meth) acrylamido or (meth) acrylate type and a side chain composed of ethylene oxide or propylene oxide (random or block) chains, or based on N-isopropylacrylamide, or N-vinylcaprolactam. This embodiment gives particular access to the preparation of polymers having thermo-thickening properties, used for example in the oil industry. Preferably, in step (E), all the monomers M1 are dissolved and / or dispersed. Priming and Conducting Radical Polymerizations of Steps (E) and (E) When it is used in step (E), the initiator of the radical polymerization is preferably water-soluble or water-dispersible. Apart from this preferential condition, it is possible to use, in step (E) and step (E °) of the process of the invention, any radical polymerization initiator (source of free radicals) known per se and adapted to the conditions chosen for these conditions. steps. Thus, the radical polymerization initiator (initiator) employed according to the invention may for example be chosen from the initiators conventionally used in radical polymerization. It may be, for example, one of the following initiators: hydrogen peroxides such as: tertiary butyl hydroperoxide, cumene hydroperoxide, t-butyl peroxyacetate, t-butylperoxybenzoate, tbutylperoxyoctoate, t-butylperoxynéodécanoate, t-butylperoxyisobutarate, lauroyl peroxide, t-amylperoxypivalte, t-butylperoxypivalate, dicumyl peroxide, benzoyl peroxide, potassium persulfate, ammonium persulfate, azo compounds such as: 2-2'-azobis (isobutyronitrile), 2,2'-azobis (2-butanenitrile), 4,4'-azobis (4-pentanoic acid), 1,1'- azobis (cyclohexanecarbonitrile), 2- (t-butylazo) -2-cyanopropane, 2,2'-azobis [2-methyl-N- (1,1) -bis (hydroxymethyl) -2-hydroxyethyl] propionamide, 2,2'-azobis (2-methyl-N-hydroxyethyl) propionamide, 2,2'-azobis (N, N'-dimethyleneisobutyramidine) dichloride, 2,2'-azobis (2-amidinopropane) dichloride, 2,2'-azobis (N, N'-dimethyleneisobutyra) mide), 2,2'-azobis (2-methyl-N- [1,1-bis (hydroxymethyl) -2-hydroxyethyl] propionamide), 2,2'-azobis (2-methyl-N- [1] , 1-bis (hydroxymethyl) ethyl] propionamide), 2,2'-azobis [2-methyl-N- (2-hydroxyethyl) propionamide], 2,2'-azobis (isobutyramide) dihydrate, - redox systems comprising combinations such as: - mixtures of hydrogen peroxide, alkyl, peresters, percarbonates and the like and any of the iron salts, titanium salts, zinc formaldehyde sulfoxylate or sodium formaldehyde sulfoxylate, and reducing sugars, - persulfates, perborate or perchlorate of alkali metals or ammonium in combination with an alkali metal bisulfite, such as sodium metabisulphite, and reducing sugars, and - the alkali metal persulfates in combination with a arylphosphinic acid, such as benzene phosphonic acid and the like, and reducing sugars.
    [0014] Typically, the amount of initiator to be used is preferably determined so that the amount of radicals generated is at most 50 mole%, preferably at most 1 mole%, based on the amount of the initiator. control or transfer agent.
    [0015] Particularly in step (E), it is generally advantageous to use a radical initiator of the redox type, which has, among others, the advantage of not requiring heating of the reaction medium (no thermal initiation and which the inventors have furthermore now discovered to be suitable for the micellar polymerization of step (E).
    [0016] Thus, the radical polymerization initiator employed in step (E) may typically be a redox initiator, typically not requiring heating for its thermal initiation. It is typically a mixture of at least one oxidizing agent with at least one reducing agent.
    [0017] The oxidizing agent present in this redox system is preferably a water-soluble agent. This oxidizing agent may for example be chosen from peroxides, such as: hydrogen peroxide, tertiary butyl hydroperoxide, cumene hydroperoxide, t-butyl peroxyacetate, t-butylperoxybenzoate, t butylperoxyoctoate, t-butylperoxynéodécanoate, t-butylperoxyisobutarate, lauroyl peroxide, t-amylperoxypivalte, t-butylperoxypivalate, dicumyl peroxide, benzoyl peroxide; sodium persulfate, potassium persulfate, ammonium persulfate, or even potassium bromate. The reducing agent present in the redox system is also preferably a water-soluble agent. This reducing agent can typically be selected from sodium formaldehyde sulfoxylate (especially in its dihydrate form, known as Rongalit or in the form of an anhydride), ascorbic acid, erythorbic acid, sulphites, bisulphites or metasulfites (especially sulphites, bisulphites or metasulfites of alkali metals), nitrilotrispropionamides, and tertiary amines and ethanolamines (preferably water-soluble). Possible redox systems include combinations such as: - mixtures of water-soluble persulfates with water-soluble tertiary amines, - mixtures of water-soluble bromates (alkali metal bromate for example) with water-soluble sulfites (alkali metal sulfites for example), - mixtures of hydrogen peroxide, alkyl, peresters, percarbonates and the like and any of the iron salts, titanous salts, zinc formaldehyde sulfoxylate or sodium formaldehyde sulfoxylate, and reducing sugars, - persulfates alkali metal or ammonium perborate or perchlorate in combination with an alkali metal bisulfite, such as sodium metabisulphite, and reducing sugars, and - alkali metal persulfates in combination with an arylphosphinic acid, such as benzene phosphonic acid and the like, and reducing sugars.
    [0018] An interesting redox system includes (and preferably consists of) the combination of ammonium persulfate and sodium formaldehyde sulfoxylate. In general, and in particular in the case of the use of a redox system of the ammonium persulfate / sodium formaldehyde sulfoxylate type, it proves preferable that the reaction medium of step (E) is free of copper. In the case of the presence of copper, it is generally desirable to add a copper complexing agent, such as EDTA, in an amount suitable for masking its presence. Whatever the nature of the initiator employed, the radical polymerization of step (E °) may be carried out in any appropriate physical form, for example in solution in water or in a solvent for example an alcohol or THF , in emulsion in water (so-called "latex" process), by mass, if necessary by controlling the temperature and / or the pH in order to make liquid species and / or soluble or insoluble. After carrying out step (E), taking into account the specific use of a control agent, polymers are obtained functionalized by transfer groups (living polymers). This living character allows, if desired, to use these polymers in a subsequent polymerization reaction, according to a technique well known per se. Alternatively, if necessary, it is possible to deactivate or destroy the transfer groups, for example by hydrolysis, ozonolysis, or reaction with amines, for example, but without limitation, according to a transformation reaction as described in Moad , Rizzardo. Polym. Int 2011, 60, 9-25. . Thus, according to a particular embodiment, the process of the invention may comprise, after step (E), a step (E1) of hydrolysis, ozonolysis or reaction with amines, suitable for deactivating and / or or destroying all or part of the transfer groups present on the polymer prepared in step (E). According to another embodiment, the method of the invention may comprise, after step (E) (possibly before or after step (El) mentioned above if it is implemented) an additional step (E2) grafting at least one ethylenically unsaturated group on the polymer as obtained at the end of step (E) or step (E1), whereby polymers having an ethylenically functional function are obtained; unsaturated, which can therefore be employed as ethylenically unsaturated monomers in a radical polymerization reaction. These particular polymers as obtained at the end of step (E2) will be referred to as "macromonomers" in the following description.
    [0019] The step (E2) of grafting an ethylenically unsaturated group may be carried out according to any means known per se. By way of illustration, and in a nonlimiting manner, this step (E2) can in particular be carried out as follows when the agent employed is a xanthate: According to one embodiment, the thio-xanthate function present at the end of the chain is converted into a thiol function. of the polymer obtained at the end of step (E) or, where appropriate, step (E1). This conversion can typically be carried out by the method described in Biomacromolecules 8.2950 (2007). The thiol group is then reacted with a dimethacrylate (a thiol-ene addition) to make a methacrylate-type macromonomer, for example, according to the method described in Journal of Polymer Science Part A: Polymer Chemistry, 47, 15, 373.
    [0020] According to one particular embodiment, the xanthate function carries a masked amine, typically a phthalimido present at the end of the polymer chain obtained at the end of step (E) or, if appropriate, the step ( El). The synthesis of a xanthate with a phthalimido function is described in particular in Macromolecules, 39, 2006, 5307-5318. The phthalimido function is converted to the amine function by the method described in Macromolecules, 39, 2006, 5293-5306. The amine function is then reacted with the (meth) acrylic acid or anhydride to generate a (meth) acrylamido type macromonomer. Use of the Polymers of the Invention The polymers as obtained after step (E) and possible steps (E1) and / or (E2) described in the preceding paragraphs are, inter alia, useful for modifying a liquid / liquid interface, liquid / solid, liquid / gas, in particular for stabilizing an emulsion or a foam or for increasing or reducing the wettability of a solid surface. They can be used as dispersants for organic or mineral pigments.
    [0021] The polymers obtained at the end of step (E) and of the optional step (E1) described in the preceding paragraph may also be useful for the regulation of the rheology of liquid media, in particular when the mass of polymers is sufficiently high, especially aqueous media. A polymer according to the invention may for example be used to modify the rheology of a cosmetic composition, a household product, a detergent composition, or a formulation intended for the field of agriculture. More specifically, the polymers as obtained according to the invention may be of interest as a rheology control agent in the field of oil and natural gas extraction. They can in particular be used for the constitution of drilling fluids, for fracturing, for stimulation and for enhanced oil recovery.
    [0022] Moreover, the nature of the synthesizable polymers according to the present invention is extremely flexible, which allows a very important choice both on the backbone and on the presence of substituents, which can be judiciously chosen according to the applications envisaged for the polymer. According to a particular aspect, the invention relates to the use of the polymers as obtained at the end of step (E2) as monomers (macromonomers) in a radical polymerization, preferably a controlled radical polymerization. The macromonomers as obtained according to step (E2) have one or more ethylenically unsaturated groups, typically a single unsaturated group at the end of the chain. This type of macromonomer can be copolymerized with other hydrophilic monomers to generate polymers which are typically of the comb type: the copolymerization most often leads to the formation of a linear polymer chain integrating the macromonomers ("base" of the comb), each of the macromonomers carrying a "multiblock" side chain as synthesized in step (E) ("tooth" of the comb). They can alternatively be used for the synthesis of star polymers. These macromonomers have interesting associative properties and they can especially be used in solutions or emulsions (direct or inverse). Various aspects and advantages of the invention will be further illustrated by the examples, hereinafter, in which polymers have been prepared according to the process of the invention.
    [0023] EXAMPLES Raw Materials Employed M2 Monomer: AE = Ethyl Acrylate AB = Butyl Acrylate AH = Hexyl Acrylate Monomer M1: Am = Acrylamide (50% solution in water) SDS = Sodium Dodecyl Sulfate Rhodixan A1 = 5 % by weight in ethanol NaPS = Sodium persulfate (1% by weight in water) NaFS = Sodium formaldehyde sulfoxylate (1% by weight in water) Synthesis protocol For each example, the steps were carried out following: 1. introduction into a reactor: - the solution of acrylamide (Am), - a hydrophobic monomer (AE, AB or AH as appropriate), - sodium dodecyl sulphonate solution (SDS) of the solution of Rhodixan A1, of the solution of sodium persulfate (NaPS) and of water, in the proportions given in Table 1 below. 2. stirring at 240 rpm until homogenization of the reaction mixture. 3. Degassing the medium by introducing nitrogen at a moderate rate for 10 minutes while maintaining agitation (closed system). 4. adding the NaFS solution. 5. Degassing of the medium by introducing nitrogen at a moderate rate for 10 minutes while maintaining agitation (closed system). 6. reacting the medium obtained for 15h at room temperature (20 ° C).
    [0024] Table 1: Proportions of the reagents employed in the examples Example monomer monomer Water SDS (g) Rhodixan Al NaFS NaPS MI (g) M2 (g) added (g) (g) (g) (g) 1 21.32 AB 4.81 23.33 12.23 4.29 5.12 5.33 2 21.32 AB 4.81 20 20 0.43 5.12 2.33 3 14.22 AB 8.33 34 12 0.43 3.41 3.55 4 14.22 AB 8.33 23 20 4.28 3.41 3.55 11.37 AE 11.61 42 13.8 4.8 1.42 1.14 6 11.37 AE 11.61 40 21 0.48 1.42 1.14 7 14.22 AH 3.91 The resulting polymers were analyzed by HPLC with the results reported in Table 2 below: Table 2: Properties of the polymers obtained in the examples monomeric polymer MI (% mol) monomer M2 (% mol) monomer NI1 (% mo /) monomer M2 (% mol) 1 99% 95% 79 19 2 99% 96% 80 20 3 99% 93% 58 39 4 99% 97% 60 40 5 99% 99% 40 60 6 90% 82% 38 58 7 96% 80% 77 17 8 98% 95% 79 2010
    权利要求:
    Claims (13)
    [0001]
    REVENDICATIONS1. Process for preparing a polymer preferably having a molecular weight in weight Mw of less than 300 000 g / mol, comprising a polymerization step (E) in which is placed in contact in an aqueous medium (M) in which micelles are dispersed surfactants: - ethylenically unsaturated monomers M1 predominantly present in the aqueous medium, hereinafter referred to as "hydrophilic monomers"; ethylenically unsaturated monomers M2 which are distinct from the hydrophilic monomers, present at least in part within the micelles of surfactants, and which have a solubility in the aqueous medium (M) at the temperature of implementation of step (E) at least equal to that of hexyl acrylate, hereinafter referred to as "partially water-soluble hydrophobic monomers"; at least one radical polymerization initiator, preferably water-soluble or water-dispersible; and at least one radical polymerization control agent.
    [0002]
    2. The process according to claim 1, wherein the radical polymerization control agent is a compound which comprises at least one thiocarbonylthio-S (C = S) - group, preferably a xanthate.
    [0003]
    3. Method according to one of the preceding claims, wherein the radical polymerization control agent is a pre-polymer bearing at least one thiocarbonylthio -S (C = S) - group, for example a xanthate group, obtained at the end of a step (E °), prior to step (E), said step (E °) bringing into contact - monomers MO having hydrophilic groups, preferably identical to the hydrophilic monomers of the step (E); a radical polymerization initiator; and a control agent carrying at least one thiocarbonylthio -S (C = S) - group, for example a xanthate.
    [0004]
    4. Method according to one of the preceding claims, wherein the radical polymerization control agent is a water-soluble or hydrodispersible oligomer with a thiocarbonylthio -S (C = S) - group, for example a xanthate group -SC = S-O-, which is soluble (or dispersible) in the aqueous medium (M) employed in step (E); and / or - is not adapted to penetrate the micelles of the micellar solution.
    [0005]
    The process according to claim 3, wherein the monomers (MO) are (meth) acrylic acid monomers (whereby the control agent is a poly (meth) acrylic acid carrier of at least one xanthate moiety and the polymer having the specific structure obtained according to step (E) with, in addition, a poly (meth) acrylic acid block bonded to one of its ends.
    [0006]
    6. Method according to one of the preceding claims, wherein the hydrophilic monomers of step (E) are (meth) acrylic acid monomers or acrylamido or methacrylamido monomers, especially (meth) acrylamides.
    [0007]
    7. Method according to one of the preceding claims, wherein the hydrophilic monomers of step (E) are 2-acryloylamino-2-nnethylpropane-1-sulfonic acid (AMPS) or acrylamide or acrylic acid.
    [0008]
    8. Method according to one of the preceding claims, wherein the partially water-soluble hydrophobic monomers of step (E) comprise acrylate monomers, especially chosen from ethyl (meth) acrylate, ethyl ethacrylate, ( meth) n-propyl acrylate, isopropyl (meth) acrylate, n-butyl (meth) acrylate, sec-butyl (meth) acrylate, tert-butyl (meth) acrylate, ethacrylate tert-butyl or n-hexyl acrylate.
    [0009]
    9. Method according to one of claims 1 to 8, which comprises, after step (E), a step (E2) for grafting an ethylenically unsaturated group. 30
    [0010]
    10. Polymer with a mass of less than 300 000 g / mol, especially ranging from 1000 to 300 000 g / mol, obtainable according to the method of one of the preceding claims.
    [0011]
    11. Polymer according to claim 10 obtainable according to the method of claim 9 which comprises an ethylenically unsaturated group.
    [0012]
    12. Use of the polymer according to claim 10, for the modification of a liquid / liquid interface, liquid / solid, liquid / gas, (especially for stabilizing an emulsion or a foam to increase or reduce the wettability of a solid surface. ); for regulating the rheology of a liquid medium, in particular aqueous medium; and / or as dispersants for organic or inorganic pigments.
    [0013]
    13. Use of the polymer according to claim 11 as ethylenically unsaturated monomers in a radical polymerization, preferably a controlled radical polymerization.
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    申请号 | 申请日 | 专利标题
    FR1400709A|FR3018814B1|2014-03-24|2014-03-24|MULTIBLOCK AMPHIPHILIC POLYMERS|FR1400709A| FR3018814B1|2014-03-24|2014-03-24|MULTIBLOCK AMPHIPHILIC POLYMERS|
    EP15709711.4A| EP3122793A1|2014-03-24|2015-03-16|Amphiphilic multiblock polymers|
    PCT/EP2015/055436| WO2015144475A1|2014-03-24|2015-03-16|Amphiphilic multiblock polymers|
    US15/128,162| US10450397B2|2014-03-24|2015-03-16|Amphiphilic multiblock polymers|
    CN201580027593.3A| CN106414528B|2014-03-24|2015-03-16|Amphiphilic multiblock polymers|
    US16/655,475| US11267923B2|2014-03-24|2019-10-17|Multiblock amphiphilic polymers|
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