EP3877426A1 - Verfahren zur synthese von polymeren durch kontrollierte radikalische inverse emulsionspolymerisation - Google Patents

Verfahren zur synthese von polymeren durch kontrollierte radikalische inverse emulsionspolymerisation

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Publication number
EP3877426A1
EP3877426A1 EP19818209.9A EP19818209A EP3877426A1 EP 3877426 A1 EP3877426 A1 EP 3877426A1 EP 19818209 A EP19818209 A EP 19818209A EP 3877426 A1 EP3877426 A1 EP 3877426A1
Authority
EP
European Patent Office
Prior art keywords
monomer
group
water
carbon atoms
monomers
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
EP19818209.9A
Other languages
English (en)
French (fr)
Inventor
Olivier Braun
Emmanuelle READ
Thierry LEBLANC
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SNF Group
Original Assignee
SPCM SA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by SPCM SA filed Critical SPCM SA
Publication of EP3877426A1 publication Critical patent/EP3877426A1/de
Pending legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00—Processes of polymerisation
    • C08F2/32—Polymerisation in water-in-oil emulsions
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00—Processes of polymerisation
    • C08F2/38—Polymerisation using regulators, e.g. chain terminating agents, e.g. telomerisation
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/04—Acids; Metal salts or ammonium salts thereof
    • C08F220/06—Acrylic acid; Methacrylic acid; Metal salts or ammonium salts thereof
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/52—Amides or imides
    • C08F220/54—Amides, e.g. N,N-dimethylacrylamide or N-isopropylacrylamide
    • C08F220/56—Acrylamide; Methacrylamide
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F293/00—Macromolecular compounds obtained by polymerisation on to a macromolecule having groups capable of inducing the formation of new polymer chains bound exclusively at one or both ends of the starting macromolecule
    • C08F293/005—Macromolecular compounds obtained by polymerisation on to a macromolecule having groups capable of inducing the formation of new polymer chains bound exclusively at one or both ends of the starting macromolecule using free radical "living" or "controlled" polymerisation, e.g. using a complexing agent
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L33/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides or nitriles thereof; Compositions of derivatives of such polymers
    • C08L33/24—Homopolymers or copolymers of amides or imides
    • C08L33/26—Homopolymers or copolymers of acrylamide or methacrylamide
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2400/00—Characteristics for processes of polymerization
    • C08F2400/02—Control or adjustment of polymerization parameters

Definitions

  • the present invention relates to a new radical polymerization process in reverse emulsion.
  • Reversible deactivation (PRDR) radical polymerizations combine both the ease of carrying out conventional radical polymerization and the living nature of ionic polymerization.
  • PRDR brings together techniques such as iodine transfer polymerization (ITP), nitroxide-controlled polymerization, NMP (Nitroxide Mediated Polymerization), by atom transfer, ATRP (Atom Transfer Radical Polymerization), by reversible addition-fragmentation chain transfer, RAFT (Reversible Addition Fragmentation chain Transfer Polymerization), which includes MADIX technology (MAcromolecular Design by Interchange of Xanthates), various variations of polymerizations with organometallic compounds, OMRP (Organometallic Mediated Radical Polymerization), radical polymerization controlled by heteroatomic compounds (OrganoHeteroatom-mediated Radical Polymerization (OHRP).
  • This activation-deactivation process allows the chains to grow at the same rate, until the total consumption of the monomer is made, making it possible to control the molecular weights of the polymers and obtain narrow molecular weight distributions. This will also make it possible to minimize the heterogeneity of the composition.
  • Reversible deactivation of growing chains is responsible for minimizing irreversible termination reactions.
  • the vast majority of polymer chains remain in dormant form and are therefore reactivable. It is then possible to functionalize the chain ends in order to initiate other modes of polymerization or to make chain extensions. This is the key to accessing high molecular weights, compositions and controlled architectures.
  • Controlled radical polymerization therefore has the following distinctive aspects:
  • the average molecular weight is controlled by the monomer / precursor molar ratio.
  • Patent EP 991 683 describes a controlled radical polymerization in direct emulsion. This mode of polymerization requires a step of recovering the polymer, such as for example evaporation under vacuum. The polymers described in patent EP 991 683 are obtained by polymerization of lipophilic monomers. Thus, in the case of an emulsion polymerization, the emulsion is a direct emulsion and the monomers are polymerized in the dispersed phase, namely the organic phase. The technique presented leads to low molecular weight block polymers.
  • Patent application WO 2012/042167 uses the gel polymerization route. Although using water-soluble precursors, this technique does not make it possible to obtain polymers of high molecular weights.
  • the problem which the applicant proposes to solve is to obtain water-soluble polymers of high molecular weight while having a low polydispersity index, advantageously less than 2.
  • the invention relates to a process for the preparation of a polymer by reverse emulsion polymerization comprising the following steps:
  • o Z O, S or N
  • R 1 and R 2 identical or different, represent:
  • a heterocycle (iii), saturated or not, optionally substituted or aromatic, these groups and rings (i), (ii) and (iii) possibly being substituted by substituted aromatic groups or alkoxycarbonyl or aryloxycarbonyl (- COOR), carboxy (-COOH), acyloxy (-0 2 CR), carbamoyl ( -CONR2), cyano (-CN), alkylcarbonyl, alkylarylcarbonyl, arylcarbonyl, arylalkylcarbonyl, phthalimido, male ⁇ mido, succinimido, amidino, guanidimo, hydroxy (-OH), amino (-NR2), halogen, allyl, epoxy, alkoxy (-OR ), S-alkyl, S-aryl, groups having a hydrophilic or ionic character such as the alkali salts of carboxylic acids, the alkali salts of sulfonic acid, the polyalkylene oxide chains (POE
  • R representing an alkyl or aryl group
  • o A is a linear or structured polymer chain comprising n identical or different monomers
  • n is an integer between 1 and 500, advantageously between 2 and 500,
  • R 1 and R 2 are identical or different and advantageously represent a group (i) (alkyl, acyl, alkenyl or alkynyl), more advantageously a group chosen from a linear or branched alkyl group comprising from 1 to 20 carbon atoms, preferably from 1 to 10 carbon atoms; a linear or branched acyl group comprising from 2 to 20 carbon atoms, preferably from 2 to 10 carbon atoms; a linear or branched alkenyl group comprising from 2 to 20 carbon atoms, preferably from 2 to 10 carbon atoms; or a linear or branched alkynyl group comprising from 2 to 20 carbon atoms, preferably from 2 to 10 carbon atoms; these groups being optionally substituted by one or more substituted aromatic groups which may comprise 4 to 7 carbon atoms or alkoxycarbonyl or aryloxycarbonyl (-COOR), carboxy (- COOH), acyloxy (-O2CR), carbamoyl
  • R advantageously represents a linear or branched alkyl group comprising from 1 to 20 carbon atoms, preferably from 1 to 10 carbon atoms, or aryl comprising from 6 to 10 carbon atoms.
  • a carbon ring (ii) comprises from 6 to 10 carbon atoms.
  • a heterocycle (iii) advantageously comprises from 5 to 9 carbon atoms.
  • a group comprising carbon atoms is a hydrocarbon group which may optionally include heteroatoms.
  • a heterocyclic comprises 1 or more heteroatoms, advantageously N, O, S or P.
  • the term monomer also denotes the monomer in its polymerized form.
  • the two R groups can be identical or different from each other.
  • Step d) makes it possible to obtain a water-soluble polymer. It is a homopolymer or a copolymer.
  • reverse emulsion refers to both reverse emulsions and reverse microemulsions. These are water-in-oil type emulsions in which the aqueous phase is dispersed in the organic phase in the form of drops or droplets.
  • water-soluble precursor designates a water-soluble precursor, at a temperature of 25 ° C., in a proportion of at least 50 g / l. This definition also relates to the other water-soluble compounds mentioned (polymer, monomer %)
  • the polymer chain A comprises at least one nonionic monomer and / or at least one anionic monomer and / or at least one cationic monomer.
  • A comprises at least two identical monomers.
  • the following different types of monomers can be used as monomers of the aqueous phase or in the polymer chain A of the precursor.
  • the nonionic monomer or monomers which can be used within the framework of the invention can be chosen, in particular, from the group comprising vinyl monomers soluble in water.
  • Preferred monomers belonging to this class are, for example, acrylamide, methacrylamide; N-isopropylacrylamide; N, N-dimethylacrylamide; N, N diethylacrylamide; N-methylolacrylamide; N-vinylformamide; N-vinyl acetamide; N-vinylpyridine; N-vinylpyrrolidone; acryloyl morpholine (ACMO), glycidyl methacrylate, glyceryl methacrylate and diacetone acrylamide.
  • a preferred nonionic monomer is acrylamide.
  • the anionic monomer (s) are preferably chosen from acrylic acid; methacrylic acid; itaconic acid; crotonic acid; maleic acid; fumaric acid; 2-acrylamido 2-methylpropane sulfonic acid; vinyl sulfonic acid; vinylphosphonic acid; allylsulfonic acid; allylphosphonic acid; styrene sulfonic acid, said anionic monomer being unsalted, partially or fully salified, and the salts of 3-sulfopropyl methacrylate.
  • the salified form advantageously corresponds to the salts of alkali metals (Li, Na, K, etc.), of alkaline earth metals (Ca, Mg, etc.) or of ammonium, in particular quaternary ammoniums.
  • the cationic monomer or monomers which can be used within the framework of the invention can be chosen, in particular from the monomers of the acrylamide, acrylic, vinyl, allyl or maleic type having a quaternary ammonium function by salification or quaternization.
  • AD AME dimethylaminoethyl acrylate
  • MADAME dimethylaminoethyl methacrylate
  • DADMAC dimethyldiallylammonium chloride
  • ATAC acrylamide propyltrimethyl chloride ammonium
  • MATAC methacrylamido propyltrimethyl ammonium chloride
  • the cationic monomer (s) can also be chosen from associative cationic monomers as described in patent FR 2 868 783.
  • the monomer can optionally be a zwitterionic monomer of the acrylamide, acrylic, vinyl, allylic or maleic type having an amine or quaternary ammonium function and an acid function of the carboxylic, sulfonic or phosphoric type.
  • dimethylammonio dimethylamino propyl methylacrylamide derivatives such as 2 - ((3-methacrylamidopropyl) dimethylammonio) ethane-1-sulfonate, 3 - ((3-methacrylamidopropyl) dimethylammonio) propane-1-sulfonate, 4- ((3-methacrylamidopropyl) dimethylammonio) butane-1-sulfonate and [3- (methacryloyloxy) propyl)] (dimethylammonio) acetate.
  • the monomer can optionally have an LCST group or a UCST group.
  • an LCST group corresponds to a group whose solubility in water for a determined concentration is modified beyond a certain temperature and according to the salinity. It is a group having a transition temperature by heating defining its lack of affinity with the solvent medium. The lack of affinity with the solvent results in an opacification or a loss of transparency which may be due to precipitation, aggregation, gelling or viscosification of the medium.
  • the minimum transition temperature is called “LCST” (lower critical solubility temperature, from the acronym “Lower Critical Solution Temperature”).
  • LCST lower critical solubility temperature
  • the measurement of the LCST can be done visually: the temperature at which the lack of affinity with the solvent appears, that is to say the cloud point, is determined.
  • the cloud point corresponds to the clouding of the solution or loss of transparency.
  • the LCST can also be determined according to the type of phase transition, for example by DSC (differential scanning calorimetry, from the English acronym “Differential scanning calorimetry”), by a transmittance measurement or by a viscosity measurement.
  • DSC differential scanning calorimetry, from the English acronym "Differential scanning calorimetry”
  • the LCST is determined by determining the cloud point by transmittance according to the following protocol.
  • the transition temperature is measured for an LCST compound for a solution having a concentration by weight in deionized water of 1% by weight of said compound.
  • the cloud point corresponds to the temperature at which the solution has a transmittance equal to 85% of light rays having a wavelength between 400 and 800 nm.
  • the temperature at which the solution has a transmittance equal to 85% corresponds to the minimum transition temperature LCST of the compound, in this case from the macromonomer to LCST.
  • a transparent composition has a maximum light transmittance value, whatever the wavelength between 400 and 800 nm, through a sample of 1 cm thickness, of at least 85 %, preferably at least 90%. This is the reason why, the cloud point corresponds to a transmittance of 85%.
  • a group with UCST corresponds to a group whose solubility in water for a determined concentration is modified below a certain temperature and according to the salinity. It is a group having a transition temperature by cooling defining its lack of affinity with the solvent medium. The lack of affinity with the solvent results in an opacification or a loss of transparency which can be due to precipitation, aggregation, gelling or viscosification of the medium.
  • the maximum transition temperature is called “UCST” (upper critical solubility temperature, from the acronym “Upper Critical Solution Temperature”).
  • UCST upper critical solubility temperature
  • Upper Critical Solution Temperature Upper Critical Solution Temperature
  • the precursor is of formula (I) in which:
  • the precursor is of formula (I) in which:
  • o A is a linear or structured polymer chain obtained from 1 to 100 (advantageously 2 to 100) monomers comprising at least one nonionic monomer and / or at least one anionic monomer and / or at least one cationic monomer.
  • the precursor is of formula (I) in which:
  • A is a linear or structured polymer chain obtained from 1 to 100 (advantageously 2 to 100) monomers comprising at least one nonionic monomer and / or at least one anionic monomer and / or at least one associative cationic monomer.
  • the precursor is of formula (I) in which:
  • o A is a linear or structured polymer chain obtained from 1 to 100 (advantageously 2 to 100) monomers comprising at least one nonionic monomer and / or at least one anionic monomer and / or at least one monomer comprising an LCST group.
  • A consists of n identical nonionic monomers. More advantageously, A is a polyacrylamide.
  • the precursor has the following formula (II):
  • n denotes an integer between 1 and 100, preferably between 1 and 50.
  • n denotes an integer between 2 and 100, preferably between 3 and 100, more preferably between 4 and 50.
  • the amount of precursor in the emulsion can be between 5. 10 7 % and 5% relative to the weight of the emulsion, preferably between 5.10 4 and 5.10
  • the molar ratio of water-soluble monomer / precursor in the aqueous phase is advantageously between 12,500: 1 and 300,000: 1, preferably between 27,500: 1 and 250,000: 1, more preferably between 27,500: 1 and 10,000: 1.
  • the radical polymerization initiator can be chosen from the initiators conventionally used in radical polymerization. It can for example be one of the following initiators:
  • hydrogen peroxides such as those selected from the group comprising tertiary butyl hydroperoxide, cumene hydroperoxide, t-butylperoxyacetate, t-butylperoxybenzoate, t-butylperoxyoctoate, t-butylperoxyneodecanoate, t -butylperoxyisobutarate, lauroyl peroxide, t-amylperoxypivalte, t-butylperoxypivalate, dicumyl peroxide, benzoyl peroxide, potassium persulfate, and ammonium persulfate, azo compounds such as those selected from the group including 2-2'- azobis (isobutyronitrile), 2,2'-azobis (2-butanenitrile), 4,4'-azobis (4-pentanoic acid), l, l'-azobis (cyclohexane-carbonitrile), 2- (t -butyl
  • alkali metal persulfates in combination with an arylphosphinic acid, such as benzene phosphonic acid and the like, and reducing sugars.
  • the different monomers used in the aqueous phase can be chosen from the respective lists mentioned above in the description also concerning the polymer chain A of the precursor.
  • the monomer is chosen from the group comprising nonionic monomers; anionic monomers; and mixtures of nonionic monomers and anionic monomers.
  • the polymer obtained according to the invention has a molecular weight of between 1,250,000 and 30,000,000 (30 million) g / mol, and preferably between 2,750,000 and 25,000,000 g / mol. Molecular weight is understood as weight average molecular weight.
  • the polydispersity index (Ip) of the polymer obtained according to the invention is advantageously at most 2 ( ⁇ 2), preferably at most 1.5 ( ⁇ 1.5).
  • the index of polydispersity is determined according to the following formula:
  • Mw is the weight average molecular weight
  • Mn is the number average molecular weight
  • the determination of the average molecular weights in weight (Mw) and in number (Mn) is carried out in a conventional manner, advantageously by steric exclusion chromatography (CES) coupled to a multi-angle light scattering detector of the Dawn Heleos II type. , 18 angles (Wyatt technology).
  • the invention relates to the use of the polymers obtained according to the polymerization process described above in the oil and gas industry, hydraulic fracturing, paper, water treatment, construction, mining, cosmetics, textiles or detergents.
  • the polymers are used in the field of enhanced oil and gas recovery.
  • Figure 1 illustrates the reversible balance between a dormant species and an active species in a radical polymerization process by reversible deactivation.
  • FIG. 2 illustrates the nuclear magnetic resonance spectrum of the proton (3 ⁇ 4 NMR) of the water-soluble precursor of formula (I) of Example 1.
  • R 1 CH2-CH3
  • This precursor was notably characterized by its 1 H NMR spectrum (300.13 MHz) in D 2 0 (FIG. 2).
  • Preparation of the aqueous phase 400 g of acrylamide (50% by weight in water), 90 g of acrylic acid, 150 g of water and 0.0015% by weight relative to the emulsion were mixed , of the water-soluble precursor of Example 1.
  • the aqueous phase was neutralized with 90 g of sodium hydroxide (50% by weight in water).
  • the aqueous phase and the organic phase were mixed and emulsified.
  • the emulsion was then degassed for 60 minutes before polymerization was initiated by the addition of a reducing agent, sodium metabisulfite (MBS).
  • MBS sodium metabisulfite
  • the polymer obtained is recovered by precipitation in acetone.
  • Polymer P2 is synthesized as in Example 2, replacing the water-soluble precursor with sodium hypophosphite.
  • the three polymers P1, P2 and P3 were analyzed by steric exclusion chromatography (CES), the conditions of which are as follows: a Shodex SB807- G precolumn and two Shodex OHpak columns in series (SB-807 HQ and SB-805 HQ ) coupled with a refractive index detector (Optilab T-rEX, Wyatt Technology, and Dawn Heleos II 18 angles, Wyatt Technology).
  • CES steric exclusion chromatography
  • Table 1 values of the molecular weights in number and in weight and the polydispersity index of PL P 2 and P 3
  • the molecular weight in number of the polymer P3 was difficult to control because the precursor used is not soluble in water which is equivalent to a polymerization without precursor.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Polymerisation Methods In General (AREA)
EP19818209.9A 2018-11-06 2019-11-04 Verfahren zur synthese von polymeren durch kontrollierte radikalische inverse emulsionspolymerisation Pending EP3877426A1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR1860202A FR3088067B1 (fr) 2018-11-06 2018-11-06 Procede de synthese de polymeres par polymerisation radicalaire controlee en emulsion inverse
PCT/FR2019/052609 WO2020094963A1 (fr) 2018-11-06 2019-11-04 Procede de synthese de polymeres par polymerisation radicalaire controlee en emulsion inverse

Publications (1)

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EP3877426A1 true EP3877426A1 (de) 2021-09-15

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EP19818209.9A Pending EP3877426A1 (de) 2018-11-06 2019-11-04 Verfahren zur synthese von polymeren durch kontrollierte radikalische inverse emulsionspolymerisation

Country Status (10)

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US (1) US20210380729A1 (de)
EP (1) EP3877426A1 (de)
JP (1) JP2022506667A (de)
KR (1) KR20210088634A (de)
CN (1) CN112969721A (de)
AR (1) AR116985A1 (de)
AU (1) AU2019376489A1 (de)
CA (1) CA3118202A1 (de)
FR (1) FR3088067B1 (de)
WO (1) WO2020094963A1 (de)

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FR3125296A1 (fr) * 2021-07-13 2023-01-20 Rhodia Operations Préparation de polymères séquencés amphiphiles par polymérisation radicalaire micellaire inverse
CN116023683A (zh) * 2021-10-27 2023-04-28 爱森（中国）絮凝剂有限公司 凝胶聚合的水溶性聚合物
CN115073677B (zh) * 2022-07-22 2022-11-11 山东诺尔生物科技有限公司 一种助留剂的制备方法及助留剂

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FR2764892B1 (fr) * 1997-06-23 2000-03-03 Rhodia Chimie Sa Procede de synthese de polymeres a blocs
FR2868783B1 (fr) 2004-04-07 2006-06-16 Snf Sas Soc Par Actions Simpli Nouveaux polymeres amphoteres associatifs de haut poids moleculaire et leurs applications
FR2965564B1 (fr) 2010-09-30 2012-10-26 Rhodia Operations Preparation de polymeres hydrophiles de haute masse par polymerisation radicalaire controlee
CN102492092B (zh) * 2011-12-21 2014-05-07 浙江大学 反相乳液聚合制备超支化离子型酰胺类聚合物的方法
CN104693385B (zh) * 2015-02-12 2017-03-01 浙江理工大学 含定量硫酸酯乙基砜基团的三硫代酯化合物及其合成方法和应用

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WO2020094963A1 (fr) 2020-05-14
FR3088067B1 (fr) 2020-11-06
AU2019376489A8 (en) 2021-06-17
FR3088067A1 (fr) 2020-05-08
US20210380729A1 (en) 2021-12-09
AU2019376489A1 (en) 2021-05-27
CA3118202A1 (en) 2020-05-14
JP2022506667A (ja) 2022-01-17
CN112969721A (zh) 2021-06-15
KR20210088634A (ko) 2021-07-14
AR116985A1 (es) 2021-06-30

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