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    • 专利摘要:
    The invention relates to a dispersion of a hydrophilic phase into a lipophilic phase, comprising: a hydrophilic phase comprising at least one water-soluble (co) polymer, - a lipophilic phase, at least one interfacial polymer composed of at least one monomer of formula (I): in which, - R1, R2, R3 are independently a hydrogen atom, a methyl group, a carboxylate group and Z-X, - Z is chosen from the group comprising C (= O) -O; C (= O) -NH; O-C (= O); NH-C (= O) -NH; NH-C (= O) -O; and a carbon chain comprising from 1 to 20 unsaturated or unsaturated carbon atoms, substituted or unsubstituted, which may contain one or more heteroatoms chosen from nitrogen and oxygen, X is a group chosen from alkanolamides, sorbitan esters, ethoxylated sorbitan esters, glyceryl esters, and polyglycosides; and comprising a hydrocarbon chain, saturated or unsaturated, linear, branched or cyclic, optionally aromatic.
    公开号:FR3075219A1
    申请号:FR1762196
    申请日:2017-12-14
    公开日:2019-06-21
    发明作者:Olivier Braun；Lionel Lauber
    申请人:SNF SA；
    IPC主号:
    专利说明:

    The present invention relates to a composition comprising at least one water-soluble (co) polymer encapsulated in an envelope.
    Another aspect of the invention relates to a process for the preparation of said composition.
    Another aspect of the invention relates to an enhanced oil and gas recovery process using said composition.
    PRIOR STATE OF THE ART
    Most of the oil fields that are currently in use have matured, and have in fact started to decline, or are about to start declining. The recovery rate of these fields is currently around 15 to 35% on average compared to the initial quantity of oil. They therefore offer a still considerable production potential.
    In general, the recovery of crude oil contained in the deposits is carried out in several stages.
    The production results initially from the natural energy of the fluids and the rock which decompresses. At the end of this depletion phase, the amount of oil recovered from the surface represents on average some 5 to 15% of the initial reserve. It is therefore necessary, in a second step, to employ techniques aimed at increasing the recovery yield while maintaining the field pressure.
    The most frequently used method is to inject water into the deposit through dedicated injection wells. This is called secondary recovery. This second phase stops when the water / oil ratio is too high, that is to say when the quantity of water in the mixture produced by the producing wells is too high. This secondary recovery thus makes it possible to obtain an additional recovery rate of the order of 10 to 20%.
    The other techniques that can be used are grouped under the name of enhanced oil recovery (RAP or EOR, acronym for "Enhanced Oil Recovery"). Their goal is to recover between 10 and 35% of additional oil compared to the initial quantity of oil. Under the term enhanced oil recovery, various thermal techniques are known, or not, such as the so-called electric, miscible, steam, or chemical techniques for improved recovery of the oil remaining in place (see “Oil & gas science and technology” - IFP review, vol 63 (2008) n ° l, pp 9-19).
    By "petroleum" is meant any type of oil, namely light oil as heavy oil, even bituminous. An oil generally results from the natural transformation of organic matter and is composed of a mixture of hydrocarbons. In the description of the prior art or of the invention, the terms petroleum and oil are used to designate the same material, with the exception of the mention of the composition of an emulsion or of a dispersion.
    The efficiency of water injection sweeping is generally improved by the addition of water-soluble (co) polymers. The expected and proven benefits of the use of (co) polymers, through the “viscosification” of the injected water, are the improvement of the sweeping and the reduction of the viscosity contrast between the fluids to control their mobility ratio in the field, in order to recover the oil quickly and efficiently. These (co) polymers increase the viscosity of water.
    It is known to those skilled in the art that synthetic water-soluble (co) polymers, in particular acrylamide-based (co) polymers, are (co) polymers which are very advantageous for increasing the viscosity of aqueous solutions and are in fact , mainly used in assisted recovery.
    However, acrylamide polymers are sensitive to chemical, biological and mechanical degradation. Solutions have been proposed in documents WO 2010/133258 and WO 2013/108173 to improve the resistance of polymers to chemical degradation and to high temperatures. Other solutions have been proposed in documents US 2012/0292029 and US 2015/041143 to avoid mechanical degradation of the polymer by using suitable equipment.
    Document US Pat. No. 7,897,546 describes the use of microparticles of highly crosslinked expandable polymers encapsulated to modify the permeability to water in an underground reservoir. These microparticles obtained are water-swelling. Their swelling in certain areas of the formation allows the plugging of said areas by formation of a gel.
    Document US 2011/0312858 describes the use of a borosilicate glass capsule containing a chemical compound in the petroleum field for the drilling, cementing and stimulation stages. The compound can be a water-swelling polymer.
    These various encapsulated polymers are not suitable for the application of enhanced oil recovery by sweeping since they cannot propagate far in the formation and therefore provide a uniform and efficient sweeping of the reservoir. Indeed, the gel by its selective placement modifies the sweeping of the tank and does not have the function of pushing the oil. The conformance treatment is punctual and aims to modify the permeability of the reservoir in a localized manner.
    The problem which the Applicant proposes to solve is to be able to inject an aqueous composition containing polymers in the context of operation (s) of enhanced recovery of oil or gas by sweeping an underground formation while avoiding mechanical degradation and chemistry of polymers during the injection of the composition and within the underground formation.
    STATEMENT OF THE INVENTION
    The invention relates to a dispersion of a hydrophilic phase in a lipophilic phase, the dispersion comprising:
    a hydrophilic phase comprising at least one water-soluble (co) polymer,
    - a lipophilic phase, at least one interfacial polymer composed of at least one monomer of formula (I):
    RR / c = c /
    R, Z "X
    Formula (I) in which,
    - RI, R2, R3 are independently chosen from the group comprising a hydrogen atom, a methyl group, a carboxylate group and Z-X,
    - Z is chosen from the group comprising C (= 0) -0; C (= O) -NH; OC (= O); NH-C (= 0) -NH; NH-C (= 0) -0; and a carbon chain comprising from 1 to 20 unsaturated or unsaturated carbon atoms, substituted or unsubstituted, which may contain one or more heteroatoms chosen from nitrogen and oxygen,
    - X is a group chosen from alkanolamides, sorbitan esters, ethoxylated sorbitan esters, glyceryl esters, and polyglycosides; and comprising a hydrocarbon chain, saturated or unsaturated, linear, branched or cyclic, optionally aromatic.
    By "polymer composed of at least one monomer" is meant a polymer obtained from several molecules of at least one monomer. Thus, a polymer of a monomer corresponds to a polymer obtained from several repeat units of molecules of a monomer.
    Hydrophilic phase to lipophilic phase dispersion
    The composition according to the invention is a dispersion of a hydrophilic phase into a lipophilic phase. In other words, the lipophilic phase is the continuous phase and the hydrophilic phase is the dispersed phase. The interfacial polymer is placed at the interface between the hydrophilic phase and the lipophilic phase. Preferably, the hydrophilic phase is an aqueous phase and the lipophilic phase is an oily phase. Thus, the composition according to the invention is advantageously a water in oil dispersion, more advantageously a water in oil emulsion.
    The interfacial polymer obtained by polymerization of at least one monomer of formula (I) forms an envelope at the interface of the hydrophilic phase and the lipophilic phase. In general, the envelope is resistant to mechanical stresses such as shearing and more particularly shearing during the dissolution of the polymer, during its injection through valves, nozzles and other restrictions with passage speeds greater than 3 meters per second, or when sweeping an underground formation near the layer-hole connection. The envelope is also resistant to chemical stresses which may be due to the presence of oxygen, H 2 S or metals during the injection phase. Preferably, the envelope is semi-permeable.
    As already indicated, preferably, the dispersion is in the form of an inverse emulsion.
    Generally, the hydrophilic phase is in the form of dispersed micrometric droplets, advantageously emulsified, in the lipophilic phase. The average size of these droplets is advantageously between 0.01 and 30 μm, more advantageously between 0.05 and 3 μm. The interfacial polymer therefore comes to be placed at the interface between the hydrophilic phase and the lipophilic phase at the level of each droplet. The average size of the droplets is advantageously measured with a laser measuring device using conventional techniques which are part of the general knowledge of those skilled in the art. A device of the Mastersizer type from the company Malvern may be used for this purpose.
    Generally, the dispersion according to the invention contains between 10 and 65% by mass of water-soluble (co) polymer, more advantageously between 30 and 60% by mass.
    In addition, the dispersion according to the invention has a mass ratio hydrophilic phase / lipophilic phase advantageously between 0.1 and 100, more advantageously between 1 and 80, and even more advantageously between 10 and 60.
    The water-soluble (co) polymer of the hydrophilic phase
    The water-soluble (co) polymer can be a natural (co) polymer, such as, for example, xanthan gums, guar gums, schyzophillan, scleroglucan or other compounds of the polysaccharide family, or a synthetic (co) polymer or semisynthetic. Preferably, the water-soluble (co) polymer is a synthetic (co) polymer.
    When the water-soluble (co) polymer is a synthetic (co) polymer, it is preferably a (co) polymer obtained from at least one nonionic monomer and / or at least one anionic monomer and / or minus a cationic monomer and / or a zwitterionic monomer.
    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. The nonionic monomer does not include the monomers of formula (I). Preferred monomers belonging to this class are, for example, acrylamide, methacrylamide, N-isopropylacrylamide, N, Ndimethylacrylamide and N-methylolacrylamide. Likewise, Nvinylformamide, N-vinyl acetamide, N-vinylpyridine and N-vinylpyrrolidone, acryloyl morpholine (ACMO), glycidyl methacrylate, glyceryl methacrylate and diacetone acrylamide can be used. A preferred nonionic monomer is acrylamide.
    The anionic monomer (s) are preferably chosen from acrylic acid, methacrylic acid, itaconic acid, maleic acid, acrylamido tertiary butyl sulfonic acid (also called ATBS or 2-acrylamido-2methylpropane sulfonic acid), vinylsulphonic acid, vinylphosphonic acid, said anionic monomer being unsalified, partially or totally 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 ammonium.
    Above and below, the cationic monomers and the anionic monomers, such as for example MADAME and ATBS, include the non-salified, salified, partially or fully salified forms.
    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. Mention may be made, in particular and without limitation, of dimethylaminoethyl acrylate (AD AME) quatemized, dimethylaminoethyl methacrylate (MADAME) quatemized, dimethyldiallylammonium chloride (DADMAC), acrylamide propyltrimethyl ammonium chloride (APTAC) , and methacrylamido propyltrimethyl ammonium chloride (MAPTAC).
    The cationic monomer (s) can also be chosen from hydrophobic cationic monomers as described in patent FR 2 868 783.
    The zwitterionic monomer (s) can also be used in the context of the invention; they combine both anionic and cationic charges on a single monomer. They can be chosen, in particular from monomers of the betaine, sultaine, sulfobetaine, phosphobetaine, and carboxybetaine type. As examples of zwitterionic monomers, mention may be made of sulfopropyl dimethylammonium ethyl methacrylate, sulfopropyl dimethylammonium propylmethacrylamide, sulfopropyl 2-vinylpyridinium, and phosphato ethyl trimethylammonium ethyl methacrylate.
    According to a particular embodiment of the invention, the water-soluble (co) polymer is composed only of ATBS.
    The water-soluble (co) polymer is preferably an anionic (co) polymer based on acrylamide, preferably a (co) polymer of acrylamide and acrylamido tertiary butyl sulfonic acid (ATBS) optionally partially post-hydrolyzed, more preferably a ter (co) polymer of acrylamide, acrylic acid and acrylamido tertiary butyl sulfonic acid (ATBS).
    The water-soluble (co) polymer preferably contains between 10% and 50 mol% of anionic monomer (s), more preferably between 20% and 45 mol%.
    The water-soluble (co) polymer preferably contains between 50% and 90 mol% of nonionic monomer (s), more preferably between 60% and 75 mol%.
    Preferably, the water-soluble (co) polymer contains only anionic and nonionic monomer units. In other words, it is preferably obtained from at least one anionic monomer and from at least one nonionic monomer.
    According to the invention, the water-soluble (co) polymer can have a linear, branched (branched), star (star-shaped) or comb (comb-shaped) structure. These structures can be obtained by selection at the option of the initiator, of the transfer agent, of the polymerization technique such as the controlled radical polymerization known as RAFT (reversible chain transfer by addition-fragmentation). addition fragmentation chain transfer), NMP (polymerization in the presence of nitroxides, from English Nitroxide Mediated Polymerization) or ATRP (radical polymerization by atom transfer, from English Atom Transfer Radical Polymerization), from the incorporation of structural monomers , concentration ... The general knowledge of a person skilled in the art allows him to prepare a water-soluble (co) polymer having one of these types of structure.
    According to the invention, the water-soluble (co) polymer is linear or structured. By structured (co) polymer (branched, star, comb), is meant a non-linear (co) polymer which has side chains so as to obtain, when this (co) polymer is dissolved in water, a strong state of entanglement leading to very high low gradient viscosities. The water-soluble polymer according to the invention is not crosslinked.
    In the case where the (co) polymer is structured, it can be structured:
    by at least one structural agent, which can be chosen from the group comprising polyethylenically unsaturated monomers (having at least two unsaturated functions), such as for example vinyl, allyl, acrylic and epoxy functions and mention may, for example, be made of methylene bis acrylamide (MBA), triallyamine, or also by macroinitiators such as polyperoxides, polyazoics and transfer polyagents such as polymercaptant (co) polymers.
    According to a particular embodiment, the water-soluble (co) polymer can comprise at least one LCST group.
    According to the general knowledge of a person skilled in the art, 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 about 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 can 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"). For each group concentration at LCST, a transition temperature by heating is observed. It is greater than the LCST which is the minimum point of the curve. Below this temperature, the (co) polymer is soluble in water, above this temperature, the (co) polymer loses its solubility in water.
    According to a particular embodiment, the water-soluble (co) polymer can comprise at least one group with UCST.
    According to the general knowledge of a person skilled in the art, a group at 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"). For each group concentration at UCST, a transition temperature by cooling is observed. It is greater than the LCST which is the minimum point of the curve. Above this temperature, the (co) polymer is soluble in water, below this temperature, the (co) polymer loses its solubility in water.
    According to the invention, the (co) polymer has an advantageously high molecular weight. By "high molecular weight" is meant molecular weights of at least 1 million g / mol, preferably between 2 and 40 million g / mol, more preferably between 5 and 30 million g / mol. Molecular weight is understood as weight average molecular weight.
    The interfacial polymer
    As already indicated, the interfacial polymer is obtained from at least one monomer of formula (I):
    R
    Formula (I) in which,
    - Rl, R2, R3 are independently chosen from the group comprising a hydrogen atom, a methyl group, a carboxylate group and Z-X,
    - Z is chosen from the group comprising C (= 0) -0; C (= O) -NH; OC (= O); NH-C (= O) -NH; NH-C (= 0) -0; and a carbon chain comprising from 1 to 20 unsaturated or unsaturated carbon atoms, substituted or unsubstituted, which may contain one or more heteroatoms chosen from nitrogen and oxygen,
    - X is a group chosen from alkanolamides, sorbitan esters, ethoxylated sorbitan esters, glyceryl esters, and polyglycosides; and comprising a hydrocarbon chain, saturated or unsaturated, linear, branched or cyclic, optionally aromatic.
    Thus, X can in particular be one of the following groups:
    an alkanolamide, preferably of the diethanolamide monooleate formula
    (Witcamide 511), stearoyl ethanolamide (WITCAMIDE 70) monoisopropanolamide acid oleic (WITCAMIDE 61) monoisopropanolamide acid iso stearic (WITCAMIDE SPA),
    coconut monoisopropanolamide (Empilan CLS), coconut monoethanolamide, oleic acid diethanolamide (Mexanyl), oleyl monoisopropanolamide (Simaline IE 101)
    a sorbitan ester, for example and in a non-exhaustive manner a sorbitan monolaurate (Span 20), sorbitan monopalmitate (Span 40), sorbitan monostearate (Span 60), sorbitan monoisostearate (Span 70), sorbitan tristearate ( Span 65), sorbitan monooleate (Span 80), sorbitan sesquioleate (Span 83) or sorbitan trioleate (Span 85)
    - an ethoxylated sorbitan ester, preferably of the formula polyethylene glycol of sorbitan monolaurate (Tween 20), polyethylene glycol of sorbitan monopalmitate (Tween 40), polyethylene glycol of sorbitan monostearate (Tween 60), polyethylene glycol of sorbitan monooleate (Tween 80) or sorbitan trioleate polyethylene glycol (Tween 85)
    - a glyceryl ester, preferably of the polyglycerol monolaurate formula (Decaglyn IL), polyglycerol myristate (Decaglyn 1-M), polyglycerol decaoleate (Polyaldo 10-10-0), polyglycerol distearate (Polyaldo 6-2-S ), polyglycerol oleate (Polyaldo 10-1-0), polyglycerol caprate (Polyaldo ΙΟΙ CC KFG), polyglycerol stearate (Polyaldo 10-1-S)
    - a polyglucoside, preferably of the formula glucoside decyle (Triton BG-10), lauryle glucoside (Plantacare 1200UP), capryle glucoside (Plantacare 810 UP), butyl glucoside (Simulsol SL 4), heptyl glucoside (Simulsol SL 7 G ), octyl and decyle glucoside (Simulsol SL 8), decyle glucoside (Simulsol SL 10), undecyle glucoside (Simulsol SL 11 W), decyle & hexadecyle glucoside (Simulsol SL 26), octyl glucoside & hexadecyle (Simulsol SL 826).
    According to a particular embodiment, the monomer of formula (I) has an HLB value advantageously less than 4.5, and advantageously at least 1.
    The HLB value ("hydrophilic - lipophilie balance" or hydrophilic / lipophilic balance) is used to calculate the balance between the hydrophilic and the lipophilic part of a molecule. This value is determined by calculating the values of the different parts of the molecule, as described by Griffin in 1949 (Griffin WC, Classification of Surface-Active Agents by HLB, Journal of the Society of Cosmetic Chemists 1 (1949): 311).
    In the present invention, the Griffin method, used conventionally, is based on the calculation of the values of the chemical groups of the molecule. Griffin assigned a value between 0 and 20 thus giving information on the solubility in a hydrophilic medium and in a lipophilic medium of the molecule. Thus the substances having an HLB of 10 are distributed equally in the two phases, namely the hydrophilic part in the hydrophilic phase and the hydrophobic part in the lipophilic phase.
    HLB = 20 (Mh / M)
    M: the molecular mass of the molecule
    Mh: the molecular mass of the hydrophilic part.
    According to a preferred embodiment, as follows:
    the monomer of formula (I) has the formula
    Ri
    / R.
    in which,
    - RI, R2, R3 independently are a hydrogen atom or a methyl group,
    Z is chosen from the group comprising CH 2 , C (= O) -O, C (= O) -NH, and (C = O) -O-CH 2 -CH (OH) -CH 2 ,
    - X is a group chosen from alkanolamides and sorbitan esters, and comprising a hydrocarbon chain, saturated or unsaturated, linear, branched or cyclic, optionally aromatic.
    According to a preferred embodiment, the monomer of formula (I) is chosen from (meth) acrylate of sorbitan monooleate, 2-hydroxypropyl (meth) acrylate of diethanolamide monooleate or (meth) acrylery glyceryl of monooleate sorbitan.
    According to a preferred embodiment, the monomer of formula (I) is the following:
    This preferred monomer corresponds to the formula H3C- (CH 2 ) 7-CH = CH- (CH 2 ) 7 -C (= O) N (CH 2 CH 2 OH) - (CH 2 ) 2 -O-CH 2 - CH (OH) -CH 2 -OC (= O) -C (CH 3 ) = CH 2 .
    In a particular embodiment of the invention, the interfacial polymer according to the invention is obtained by polymerization of at least one monomer of formula (I).
    In a particular embodiment, the interfacial polymer according to the invention is obtained by polymerization of at least one monomer of formula (I) and of at least one nonionic monomer and / or at least one anionic monomer and / or at minus one cationic monomer.
    The different monomers used can be chosen from the respective lists mentioned above in the description of the water-soluble (co) polymer.
    Advantageously, the interfacial polymer comprises between 0.0001 and 10%, more advantageously between 0.0001 and 5%, and even more advantageously from 0.0001 to 1% of monomer of formula (I), by weight relative to the total weight of monomers.
    Where appropriate, the interfacial polymer comprises between 50 and 99.9999%, more advantageously between 60 and 99.9999% of nonionic monomer (distinct from the monomer of formula (I)), by weight relative to the total weight of monomers .
    Where appropriate, the interfacial polymer comprises between 10 and 99.9999%, more advantageously between 20 and 99.9999% of anionic monomer, by weight relative to the total weight of monomers.
    Where appropriate, the interfacial polymer comprises between 1 and 99.9999%, more advantageously between 10 and 99.9999% of cationic monomer, by weight relative to the total weight of monomers.
    The envelope
    According to the invention, the interfacial polymer forms an envelope around the droplets forming the hydrophilic phase. In addition to the monomers mentioned above, the interfacial polymer can comprise at least one structuring agent. The structural agent is advantageously chosen from diacrylamides or methacrylamides of diamines; acrylic esters of di, tri, or tetrahydroxy compounds; methacrylic esters of di, tri, or tetrahydroxy compounds; divinyl compounds preferably separated by an azo group; the diallylic compounds preferably separated by an azo group; vinyl esters of di or trifunctional acids; allyl esters of di or trifunctional acids; methylenebisacrylamide; diallylamine; triallylamine; tetraallylammonium chloride; divinylsulfone; polyethylene glycol dimethacrylate and diethylene glycol diallyl ether.
    Preparation process
    Another aspect of the invention relates to a process for preparing the dispersion as described above.
    According to the invention, the water-soluble (co) polymer is advantageously obtained by polymerization in reverse emulsion or in reverse microemulsion. This polymerization technique is well known to those skilled in the art. It consists in emulsifying, in a lipophilic phase, a hydrophilic phase containing the monomer (s). This emulsification is generally carried out using a water-in-oil surfactant. After polymerization of the monomer (s), an oil-in-water surfactant is optionally added to subsequently facilitate the inversion of the emulsion in water.
    The lipophilic phase of the dispersion according to the invention comprises at least one lipophilic solvent. The lipophilic phase is advantageously chosen from hydrocarbon oils having a boiling point of at least 100 ° C, preferably at least 135 ° C, more preferably at least 180 ° C. Preferably, the lipophilic phase is chosen from hydrocarbon oils having a boiling point which does not exceed 200 ° C. If the oil has a boiling range, the term boiling point refers to the lower limit of the boiling range.
    The lipophilic solvent is advantageously a hydrocarbon oil. This hydrocarbon oil can be chosen from aliphatic hydrocarbons, aromatic hydrocarbons or mixtures of these oils. Among these oils, we can cite, but are not limited to, water-immiscible solvents, such as paraffinic hydrocarbons; naphthene hydrocarbons; aromatic hydrocarbons; olefins; and their mixtures. The paraffinic hydrocarbons can be saturated, linear or branched paraffinic hydrocarbons. Aromatic hydrocarbons include, but are not limited to, toluene and xylene. The oil can be selected from vegetable oils, for example soybean oil, rapeseed oil, or any other oil produced from the seed of any of several varieties of the rapeseed plant. The oil can be obtained from renewable raw materials such as isoamyl laurate or renewable isoparaffins, such as those distributed by the company Total under the brand Biolife.
    According to a particular embodiment of the invention, the polymerization of the interfacial polymer is carried out during the polymerization of the water-soluble (co) polymer of the hydrophilic phase. In other words, and more precisely, a particular process, according to the invention, for preparing a dispersion of a hydrophilic phase in a lipophilic phase comprises the following steps:
    a) Preparation of a hydrophilic phase comprising at least one monomer distinct from the monomer of formula (I),
    b) Preparation of a lipophilic phase comprising a lipophilic solvent and at least one monomer of formula (I):

    Formula (I) in which,
    - RI, R2, R3 are independently chosen from the group comprising a hydrogen atom, a methyl group, a carboxylate group and Z-X,
    - Z is chosen from the group comprising C (= 0) -0; C (= O) -NH; OC (= O); NH-C (= O) -NH; NH-C (= 0) -0; and a carbon chain comprising from 1 to 20 unsaturated or unsaturated carbon atoms, substituted or unsubstituted, which may contain one or more heteroatoms chosen from nitrogen and oxygen,
    - X is a group chosen from alkanolamides, sorbitan esters, ethoxylated sorbitan esters, glyceryl esters, and polyglycosides; and comprising a hydrocarbon chain, saturated or unsaturated, linear, branched or cyclic, optionally aromatic,
    c) introduction of the hydrophilic phase into the lipophilic phase with stirring in order to form a hydrophilic phase dispersion in the lipophilic phase,
    d) once the dispersion has been formed, polymerization of the monomers of the hydrophilic phase and polymerization of at least one monomer of formula (I).
    The at least one monomer from step a) corresponds to the monomers mentioned above to define the water-soluble (co) polymer.
    The polymerization of step d) is advantageously initiated by the introduction of at least one radical initiator.
    According to the invention, the hydrophilic phase can comprise one or more structural agents.
    In the case where the polymerization of at least one monomer of formula (I) is carried out at the same time as the formation, by polymerization of the water-soluble (co) polymer, the monomer of formula (I) preferably has an HLB value less than 4.5, and advantageously greater than or equal to 1.
    According to the invention, the lipophilic phase can comprise one or more water-oil surfactants which do not carry polymerizable functions such as vinyl functions.
    According to the invention, after step d) the water in the hydrophilic phase can be partially or completely removed from the dispersion. As a technique for removing water, we can cite as an example distillation under reduced pressure. This distillation can be continuous or discontinuous, with azeotropic entrainment. Preferably, the distillation is continuous and a light oil (boiling point below 200 ° C) is used to facilitate the entrainment of water.
    According to another particular embodiment of the invention, the polymerization of the interfacial polymer is carried out after the formation, by polymerization, of the water-soluble (co) polymer of the hydrophilic phase. In other words, and more precisely, a particular process for preparing the dispersion of a hydrophilic phase in a lipophilic phase according to the invention comprises the following steps:
    aa) Preparation of a hydrophilic phase comprising at least one monomer distinct from the monomer of formula (I), bb) Preparation of a lipophilic phase comprising a lipophilic solvent and at least one water-in-oil surfactant not carrying a polymerizable function, this ) Introduction of the hydrophilic phase into the lipophilic phase with stirring in order to form a dispersion of the hydrophilic phase in the lipophilic phase, dd) Once the dispersion has formed, polymerization of the monomers of the hydrophilic phase, ee) Once the polymerization is complete, introduction of at least one monomer of formula (I):

    z-x
    Formula (I) in which,
    - RI, R2, R3 are independently chosen from the group comprising a hydrogen atom, a methyl group, a carboxylate group and
    Z-X,
    - Z is chosen from the group comprising C (= 0) -0; C (= O) -NH; OC (= O); NH-C (= O) -NH; NH-C (= 0) -0; and a carbon chain comprising from 1 to 20 unsaturated or unsaturated carbon atoms, substituted or unsubstituted, which may contain one or more heteroatoms chosen from nitrogen and oxygen,
    - X is a group chosen from alkanolamides, sorbitan esters, ethoxylated sorbitan esters, glyceryl esters, and polyglycosides; and comprising a hydrocarbon chain, saturated or unsaturated, linear, branched or cyclic, optionally aromatic, ff) Polymerization of at least one monomer of formula (I).
    The at least one monomer from step aa) corresponds to the monomers mentioned above to define the water-soluble (co) polymer.
    The polymerization of step dd) is advantageously initiated by the introduction of at least one radical initiator.
    The polymerization of step ff) is advantageously initiated by the introduction of at least one radical initiator.
    According to the invention, the hydrophilic phase can comprise one or more structural agents.
    According to the invention, in step ee) monomers, distinct from the monomer of formula (I), and / or at least one structural agent can be introduced into the dispersion with the monomer of formula (I).
    According to the invention, step ee) comprises the introduction into the dispersion, with the monomer of formula (I), of at least one monomer distinct from the monomer of formula (I), and / or at least one agent of structure.
    According to a particular embodiment of the invention, after step dd) and before step ee) the water from the hydrophilic phase can be partially or completely removed from the dispersion. As a technique for removing water, we can cite as an example distillation under reduced pressure. This distillation can be continuous or discontinuous, with azeotropic entrainment. Preferably, the distillation is continuous and a light oil (boiling point below 200 ° C) is used to facilitate the entrainment of water.
    According to a particular embodiment of the invention, the step of removing the water is done after step ee).
    Whatever their preparation process, the envelopes comprising the water-soluble (co) polymer can be in liquid or solid form. When the envelopes comprising the water-soluble (co) polymer are in liquid form, they are preferably in the form of a water-in-oil dispersion or in the form of a liquid polymer dispersion. When the envelopes comprising the water-soluble (co) polymer are in solid form, they are preferably in the form of a powder.
    According to a particular embodiment of the invention, the powder form can be obtained by drying the dispersion obtained in step d) or ff). As a drying technique, mention may be made of “spray drying”, drum drying, microwave drying or even drying in a fluidized bed.
    According to another particular embodiment of the invention, the polymerization of the interfacial polymer is carried out both during and after the polymerization of the water-soluble (co) polymer.
    As previously discussed, the dispersion may include an inverting agent such as an oil-in-water surfactant. It facilitates phase reversal when the dispersion is mixed with water or brine. Generally, they have an HLB value greater than 9, preferably greater than 10, and more precisely between 10 and 18. Those skilled in the art know how to select these reversing agents and adjust their quantity as described in the document WO 2014 / 128400.
    The reversing agent can be added to the dispersion according to the invention during its preparation or after its preparation, or in the concentrated dispersion or in the solid form obtained after drying of the dispersion.
    Enhanced oil and / or gas recovery process
    Another aspect of the invention relates to an enhanced oil and / or gas recovery process using the above-mentioned dispersion.
    The composition (dispersion) according to the invention has the functionality of viscosifying the water injected into the tanks containing oil or gas to ensure mobility control without recourse to crosslinking, that is to say inter chemical bridging. chains, is only necessary.
    More specifically, the present invention relates to a process for enhanced recovery of oil or gas, by sweeping an underground formation, comprising the injection, into the underground formation, of an aqueous injection fluid obtained by adding to water or a brine, the dispersion of a hydrophilic phase in a lipophilic phase according to the invention, or its concentrated form after removal of part of the water, or its solid form obtained after drying of said dispersion.
    In this process, the interfacial polymer degrades over time under the temperature and / or pH conditions of the underground formation, thus releasing the water-soluble (co) polymer once in the tank.
    Whatever the form used (dispersion, concentrated dispersion or solid form obtained from the dispersion) the protective effect of the envelope occurs and thus the polymers are protected from chemical and mechanical degradation, especially during injection.
    In other words, and more precisely, the enhanced oil and / or gas recovery process according to the invention comprises the following steps:
    - Preparation of an aqueous injection fluid by addition in water or in brine of the dispersion of a hydrophilic phase in a lipophilic phase according to the invention, or its concentrated form after elimination of part of the water , or its solid form obtained after drying of said dispersion, injection of the injection fluid into an underground formation,
    - Sweeping of the underground formation using the injected fluid,
    - Recovery of an aqueous and hydrocarbon mixture (oil and / or gas).
    According to the invention, the injection fluid advantageously comprises between 30 ppm and 50,000 ppm of the dispersion or of the concentrated dispersion or of the solid form obtained from the dispersion, more advantageously between 100 and 30,000 ppm, and again more advantageously between 300 and 15,000 ppm.
    According to the invention, the injection fluid advantageously comprises between 10 ppm and 15,000 ppm of water-soluble (co) polymer, more advantageously between 50 and 10,000 ppm, and even more advantageously between 100 and 5,000 ppm.
    By "water-soluble (co) polymer" is meant a water-soluble (co) polymer under normal conditions of use, that is to say at least at the concentrations indicated above.
    Thus, the water-soluble (co) polymer included in the hydrophilic phase is protected by the envelope formed from at least one interfacial polymer obtained by polymerization of at least one monomer of formula (I), the envelope being capable of being degraded. under the temperature and / or pH conditions of the underground formation.
    The method according to the invention makes it possible to preserve the polymer from mechanical and chemical degradations linked to the preparation of the composition injected with the polymer, and to its injection, while retaining good injectivity and excellent scanning of the underground formation.
    In fact, the interfacial polymer makes it possible to protect the water-soluble (co) polymer included in the hydrophilic phase from the shear generated by the preparation and injection of the injection fluid and from the chemical degradation linked to oxygen, metals, FEES. .
    Once the injection fluid has been injected, the water-soluble (co) polymer is released, following the degradation of the envelope formed by the interfacial polymer under the temperature and / or pH conditions of the underground formation. Thus, the scanning is carried out by an aqueous composition comprising at least one water-soluble (co) polymer which has not undergone mechanical or chemical degradation.
    Without wishing to be bound by any theory, the formation of the injection fluid by introduction of the dispersion according to the invention does not make it possible to release the water-soluble (co) polymer from its envelope, even in the presence of an inverter ( oil in water surfactant). The pH and / or the temperature of the underground formation allow the hydrolysis of the interfacial polymer and therefore the delayed release of the fully water-soluble (co) polymer. Unlike conventional EOR type processes, the present invention does not allow the release of the water-soluble (co) polymer during the formation of the injection fluid.
    The invention and the advantages which ensue therefrom will emerge more clearly from the following figures and examples given in order to illustrate the invention and not in a limiting manner.
    DESCRIPTION OF THE FIGURES
    Figure 1 is a schematic illustration of water-soluble polymers in an envelope according to the invention.
    Figure 2 illustrates the release of the water-soluble polymers from the dispersion of Example 1, measured by the increase in viscosity.
    FIG. 3 illustrates the release of the water-soluble polymers from the dispersion of Example 2, measured by the increase in viscosity.
    FIG. 4 illustrates the viscosity, as a function of the shear, of the dispersion of Example 2 with the envelope formed by the interfacial polymer, without an envelope and after release of the water-soluble (co) polymer.
    EXAMPLES OF EMBODIMENT OF THE INVENTION
    Example 1
    Part A: Preparation of the monomer XI corresponding to formula (I)
    0.16 g of glycidyl methacrylate (97%) is added to 20.0 g of oleyl diethanolamide (Witcamide 511 - Akzo nobel) with magnetic stirring. The medium is left under stirring for 12 hours at room temperature.
    Part B: Preparation of a dispersion according to the invention
    A hydrophilic phase is prepared containing 365.8 g of acrylamide (50%), 24.6 g of acrylic acid (100%), 234.6 g of sodium salt of acrylamido tertiary butyl sulfonic acid (50%), 29.0 g deionized water, 25.9g of sodium hydroxide (50%), 1.6g of an aqueous solution of sodium hypophosphite (5g / L), 0.94g of tert-butyl hydroperoxide (0.7%) 0.40 g of pentasodium salt of diethylene triamine penta acetic acid (Versenex 80) dispersed in a mixture of 280 g of aliphatic hydrocarbon D100 (Exxsol D100) and 20 g of the monomer XI. The pH is adjusted to 6.50.
    After homogenization and deoxygenation with nitrogen for 30 minutes, the polymerization is initiated by adding a solution of sodium bisulfite.
    Example 2
    Part A: Preparation of the monomer X2 corresponding to formula (I)
    15.7 g of glycidyl methacrylate (97%) are added dropwise to 20.0 g of oleyl diethanolamide (Witcamide 511 - Akzo nobel) with magnetic stirring. The medium is left under stirring for 12 hours at room temperature.
    Part B: Preparation of a dispersion without interfacial polymer (counterexample)
    A hydrophilic phase is prepared containing 363.8 g of acrylamide (50%), 24.6 g of acrylic acid (100%), 234.6 g of sodium salt of acrylamido tertiary butyl sulfonic acid (50%), 29.0 g deionized water, 25.9g of sodium hydroxide (50%), 1.6g of an aqueous solution of sodium hypophosphite (5g / L), 0.94g of tert-butyl hydroperoxide (0.7%) , 0.40 g of pentasodium salt of diethylene triamine penta acetic acid (Versenex 80) dispersed in a mixture of 280 g of aliphatic hydrocarbon D100 (Exxsol D100) and 20 g of oleyl diethanolamide (Witcamide 511 - Akzo nobel). The pH is adjusted to 6.50.
    After homogenization and deoxygenation with nitrogen for 30 minutes, the polymerization is initiated by adding a solution of sodium bisulfite.
    Part C: Preparation of a dispersion according to the invention
    36g of acrylamide (50%), 1.6g of tert-butyl hydroperoxide (0.7%) and 0.6g of monomer X2 are added to the dispersion obtained in part B. The formation of the interfacial polymer, by polymerization of X2, is initiated by adding a solution of sodium bisulfite (radical initiator).
    Example 3 - Liberation of the chains measured by rheology
    Aqueous solutions at 1% (10,000 ppm) by mass of polymer are produced by adding a dispersion according to the invention, described in Examples 1 and 2, with vigorous stirring in synthetic sea water.
    The solutions are placed in an oven at 58 ° C. and their viscosities are measured regularly using a Kinexus Pro + from Malvern Instruments. The increase in viscosity visible in Figures 2 (pH = 8.0) and 3 (pH = 6.2) comes from the release of the water-soluble polymer.
    Example 4 - Protection against mechanical degradation
    To demonstrate the mechanical protection of the polymer provided by the envelope, aqueous solutions at 1000 ppm of polymer of Example 2, with and without an envelope (according to the invention and counterexample), were prepared in water synthetic sea. The solutions were sheared by passing them through a small section pipe at different pressures. The samples are then collected at the outlet of the pipe and the viscosity at 7.3 s' 1 is measured at 25 ° C on a Kinexus Pro + from Malvern Instruments. The shear gradient is determined by measuring the flow at the outlet of the pipe.
    The data are presented in Figure 4. The uncoated polymer is rapidly degraded. Polymer solutions with an envelope keep constant viscosities very close to 1.0 cp. Each of the solutions according to the invention having been collected after shearing, that is to say at each measurement point, are, after measuring their viscosity, then activated by being placed for 4 days in an oven at 58 ° C. . Their viscosities after release of the water-soluble polymer are then measured. These remain very close to the viscosities of the non-sheared solutions and without initial envelope.
    Table 1: Viscosity of the polymer solution at 7.3 s' 1 , T = 25 ° C (cp) as a function of the shear (Figure 4).
    Shear gradient (s' 1 ) 0 119000 163000 195000 223000 253000 PI: Viscosity of the polymer without envelope 7.6 5.9 4.2 3.5 3.2 2.8 P2: Viscosity of the polymer with envelope 1.1 1.1 1.1 1.1 1.1 1.1 P3: Viscosity of the polymer after degradation of the envelope 7.4 7.4 7.2 7.2 7.2 7.6
    权利要求:
    Claims (14)
    [1" id="c-fr-0001]
    1. Dispersion of a hydrophilic phase into a lipophilic phase, comprising:
    a hydrophilic phase comprising at least one water-soluble (co) polymer,
    - a lipophilic phase, at least one interfacial polymer composed of at least one monomer of formula (I):
    R R r »2 ® i c =
    Formula (I) in which,
    - RI, R2, R3 are independently chosen from the group comprising a hydrogen atom, a methyl group, a carboxylate group and Z-X,
    - Z is chosen from the group comprising C (= 0) -0; C (= O) -NH; OC (= O); NH-C (= O) -NH; NH-C (= 0) -0; and a carbon chain comprising from 1 to 20 unsaturated or unsaturated carbon atoms, substituted or unsubstituted, which may contain one or more heteroatoms chosen from nitrogen and oxygen,
    X is a group chosen from alkanolamides, sorbitan esters, ethoxylated sorbitan esters, glyceryl esters, and polyglycosides; and comprising a hydrocarbon chain, saturated or unsaturated, linear, branched or cyclic, optionally aromatic.
    [2" id="c-fr-0002]
    2. Dispersion according to claim 1, characterized in that the water-soluble (co) polymer is obtained from at least one nonionic monomer and / or at least one anionic monomer and / or at least one cationic monomer and / or at minus one zwitterionic monomer.
    [3" id="c-fr-0003]
    3. Dispersion according to claim 2, characterized in that the nonionic monomer is chosen from the group comprising acrylamide, methacrylamide, N-isopropylacrylamide, Ν, Ν-dimethylacrylamide, N-methylolacrylamide, N-vinylformamide , N-vinyl acetamide, Nvinylpyridine N-vinylpyrrolidone, acryloyl morpholine, glycidyl methacrylate, glyceryl methacrylate and diacetone acrylamide.
    [4" id="c-fr-0004]
    4. Dispersion according to one of claims 2 to 3, characterized in that the anionic monomer is chosen from the group comprising the salts of 3-sulfopropyl methacrylate, and the unsalified, partially or fully salified monomers chosen from acid acrylic, methacrylic acid, itaconic acid, maleic acid, acrylamido tertiary butyl sulfonic acid, vinylsulphonic acid, and vinylphosphonic acid.
    [5" id="c-fr-0005]
    5. Dispersion according to one of claims 1 to 4, characterized in that the water-soluble (co) polymer is linear or structured.
    [6" id="c-fr-0006]
    6. Dispersion according to one of claims 1 to 5, characterized in that the interfacial polymer comprises, in addition to the monomer of formula (I), at least one nonionic monomer and / or at least one anionic monomer and / or at minus one cationic monomer.
    [7" id="c-fr-0007]
    7.
    Dispersion according to one of Claims 1 to 6, characterized in that the monomer of formula (I) has the following formula:
    / R.
    Formula (I) in which,
    - Rl, R2, R3 independently are a hydrogen atom or a methyl group,
    - Z is chosen from the group comprising CH 2 , C (= O) -O, C (= O) -NH, and - (C = O) -O-CH 2 -CH (OH) -CH 2 ,
    - X is a group chosen from alkanolamides and sorbitan esters;
    and comprising a hydrocarbon chain, saturated or unsaturated, linear, branched or cyclic, optionally aromatic.
    [8" id="c-fr-0008]
    8. Dispersion according to one of claims 1 to 7, characterized in that the monomer of formula (I) is chosen from (meth) acrylate of sorbitan monooleate, 2-hydroxypropyl (meth) acrylate of diethanolamide monooleate or (meth) acrylery glyceryl of sorbitan monooleate.
    [9" id="c-fr-0009]
    9. Dispersion according to one of claims 1 to 8, characterized in that the monomer of formula (I) has the following formula:
    [10" id="c-fr-0010]
    10. Method for preparing a dispersion of a hydrophilic phase in a lipophilic phase according to one of claims 1 to 9, comprising the following steps:
    a) Preparation of a hydrophilic phase comprising at least one monomer distinct from the monomer of formula (I),
    b) Preparation of a lipophilic phase comprising a lipophilic solvent and at least one monomer of formula (I):
    z-x
    Formula (I) in which,
    - RI, R2, R3 are independently chosen from the group comprising a hydrogen atom, a methyl group, a carboxylate group and
    Z-X,
    - Z is chosen from the group comprising C (= 0) -0; C (= O) -NH; OC (= O); NH-C (= O) -NH; NH-C (= 0) -0; and a carbon chain comprising from 1 to 20 unsaturated or unsaturated carbon atoms, substituted or unsubstituted, which may contain one or more heteroatoms chosen from nitrogen and oxygen,
    - X is a group chosen from alkanolamides, sorbitan esters, ethoxylated sorbitan esters, glyceryl esters, and polyglycosides; and comprising a hydrocarbon chain, saturated or unsaturated, linear, branched or cyclic, optionally aromatic,
    c) introduction of the hydrophilic phase into the lipophilic phase with stirring in order to form a hydrophilic phase dispersion in the lipophilic phase,
    d) once the dispersion has been formed, polymerization of the monomers of the hydrophilic phase and polymerization of at least one monomer of formula (I).
    [11" id="c-fr-0011]
    11. Method for preparing a dispersion of a hydrophilic phase in a lipophilic phase according to one of claims 1 to 9, comprising the following steps:
    aa) Preparation of a hydrophilic phase comprising at least one monomer distinct from the monomer of formula (I), bb) Preparation of a lipophilic phase comprising a lipophilic solvent and at least one water-in-oil surfactant not carrying a polymerizable function, this ) Introduction of the hydrophilic phase into the lipophilic phase with stirring in order to form a dispersion of the hydrophilic phase in the lipophilic phase, dd) Once the dispersion has formed, polymerization of the monomers of the hydrophilic phase, ee) Once the polymerization has been completed, introduction of at least one monomer of formula (I),
    Formula (I) in which,
    - RI, R2, R3 are independently chosen from the group comprising a hydrogen atom, a methyl group, a carboxylate group and Z-X,
    - Z is chosen from the group comprising C (= 0) -0; C (= O) -NH; OC (= O); NH-C (= O) -NH; NH-C (= 0) -0; and a carbon chain comprising from 1 to 20 unsaturated or unsaturated carbon atoms, substituted or unsubstituted, which may contain one or more heteroatoms chosen from nitrogen and oxygen,
    - X is a group chosen from alkanolamides, sorbitan esters, ethoxylated sorbitan esters, glyceryl esters, and polyglycosides; and comprising a hydrocarbon chain, saturated or unsaturated, linear, branched or cyclic, optionally aromatic, f) Polymerization of at least one monomer of formula (I).
    [12" id="c-fr-0012]
    12. Method according to claim 11, characterized in that step ee) comprises the introduction into the dispersion, with the monomer of formula (I), of at least one monomer distinct from the monomer of formula (I), and / or at least one structural agent.
    [13" id="c-fr-0013]
    13. A method of enhanced recovery of oil or gas, by sweeping an underground formation, comprising the injection into the underground formation of an injection fluid comprising the dispersion of a hydrophilic phase in a lipophilic phase according to claims 1 to 9.
    [14" id="c-fr-0014]
    14. Method according to claim 13, characterized in that it comprises the following steps:
    - Preparation of the injection fluid from the dispersion of a hydrophilic phase into a lipophilic phase, with water or brine,
    - Injection of the injection fluid into an underground formation,
    - Sweeping of the underground formation using the injected fluid,
    - Recovery of an aqueous and hydrocarbon mixture.
    1/3 (co) water-soluble polymer
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    同族专利:
    公开号 | 公开日
    FR3075219B1|2019-11-22|
    WO2019115619A1|2019-06-20|
    EP3724295A1|2020-10-21|
    CN111465673A|2020-07-28|
    US20200362229A1|2020-11-19|
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    法律状态:
    2018-12-21| PLFP| Fee payment|Year of fee payment: 2 |
    2019-06-21| PLSC| Publication of the preliminary search report|Effective date: 20190621 |
    2019-12-27| PLFP| Fee payment|Year of fee payment: 3 |
    2020-01-10| TP| Transmission of property|Owner name: S.P.C.M. SA, FR Effective date: 20191205 |
    2020-12-29| PLFP| Fee payment|Year of fee payment: 4 |
    2021-12-28| PLFP| Fee payment|Year of fee payment: 5 |
    优先权:
    申请号 | 申请日 | 专利标题
    FR1762196|2017-12-14|
    FR1762196A|FR3075219B1|2017-12-14|2017-12-14|COMPOSITION COMPRISING A WATER-SOLUBLE POLYMERENCAPSULATED IN AN ENVELOPE AND USE IN THE ASSISTED RECOVERY OF PETROLEUM AND GAS|FR1762196A| FR3075219B1|2017-12-14|2017-12-14|COMPOSITION COMPRISING A WATER-SOLUBLE POLYMERENCAPSULATED IN AN ENVELOPE AND USE IN THE ASSISTED RECOVERY OF PETROLEUM AND GAS|
    PCT/EP2018/084575| WO2019115619A1|2017-12-14|2018-12-12|Method for preparing a composition comprising a hydrosoluble polymer encapsulated in a shell and use of this composition in assisted oil and gas recovery|
    CN201880079562.6A| CN111465673A|2017-12-14|2018-12-12|Method for preparing a composition comprising a water-solublepolymer encapsulated in a shell and use of the composition in assisted oil and gas recovery|
    BR112020010530-9A| BR112020010530A2|2017-12-14|2018-12-12|METHODS FOR PREPARING A DISPERSION OF A HYDROPHYLIC PHASE, AND FOR ENHANCED OIL OR GAS RECOVERY.|
    US16/768,355| US20200362229A1|2017-12-14|2018-12-12|Method for preparing a composition comprising a hydrosoluble polymer encapsulated in a shell and use of this composition in assisted oil and gas recovery|
    EP18816057.6A| EP3724295A1|2017-12-14|2018-12-12|Method for preparing a composition comprising a hydrosoluble polymer encapsulated in a shell and use of this composition in assisted oil and gas recovery|
    EA202091140A| EA202091140A1|2017-12-14|2018-12-12|A METHOD FOR PRODUCING A COMPOSITION CONTAINING A WATER-SOLUBLEPOLYMER INCAPPED IN A CASING AND APPLICATION OF SUCH COMPOSITION IN OIL AND GAS PRODUCTION WITH AUXILIARY MEANS|
    ARP180103648A| AR113937A1|2017-12-14|2018-12-13|PROCEDURE FOR THE PREPARATION OF A COMPOSITION INCLUDING A WATER-SOLUBLEPOLYMER ENCAPSULATED IN AN ENCAPSULATION AND USE OF THIS COMPOSITION IN THE ASSISTED RECOVERY OF OIL AND GAS|
    CONC2020/0006370A| CO2020006370A2|2017-12-14|2020-05-26|Process for preparing a composition comprising a water-solublepolymer encapsulated in an envelope and use of this composition in the assisted recovery of oil and gas|
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