WO2010144588A1 - Swellable polymer with anionic sites - Google Patents

Swellable polymer with anionic sites Download PDF

Info

Publication number
WO2010144588A1
WO2010144588A1 PCT/US2010/037988 US2010037988W WO2010144588A1 WO 2010144588 A1 WO2010144588 A1 WO 2010144588A1 US 2010037988 W US2010037988 W US 2010037988W WO 2010144588 A1 WO2010144588 A1 WO 2010144588A1
Authority
WO
WIPO (PCT)
Prior art keywords
crosslinker
labile
composition
cationic
particle
Prior art date
Application number
PCT/US2010/037988
Other languages
French (fr)
Inventor
Ahmad Moradi-Araghi
James Herbert Hedges
David Russell Zornes
Riley Byran Needham
Huili Guan
Jenn-Tai Liang
Cory Berkland
James Pryor Johnson
Min CHENG
Faye Lynn Scully
Original Assignee
Conocophillips Company-Ip Services Group
University Of Kansas
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 Conocophillips Company-Ip Services Group, University Of Kansas filed Critical Conocophillips Company-Ip Services Group
Priority to AU2010258802A priority Critical patent/AU2010258802B2/en
Priority to GB201120813A priority patent/GB2482835B8/en
Priority to MX2014006810A priority patent/MX347441B/en
Priority to RU2011153041/04A priority patent/RU2540068C2/en
Priority to MX2011013343A priority patent/MX2011013343A/en
Priority to CN2010800255227A priority patent/CN102459364A/en
Priority to CA2761528A priority patent/CA2761528C/en
Publication of WO2010144588A1 publication Critical patent/WO2010144588A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/58Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids
    • C09K8/588Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids characterised by the use of specific polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F20/00Homopolymers and 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
    • C08F20/02Monocarboxylic acids having less than ten carbon atoms, Derivatives thereof
    • C08F20/04Acids, Metal salts or ammonium salts thereof
    • C08F20/06Acrylic acid; Methacrylic acid; Metal salts or ammonium salts thereof
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F26/00Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a single or double bond to nitrogen or by a heterocyclic ring containing nitrogen
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/02Well-drilling compositions
    • C09K8/04Aqueous well-drilling compositions
    • C09K8/06Clay-free compositions
    • C09K8/12Clay-free compositions containing synthetic organic macromolecular compounds or their precursors
    • EFIXED CONSTRUCTIONS
    • E21EARTH OR ROCK DRILLING; MINING
    • E21BEARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16Enhanced recovery methods for obtaining hydrocarbons

Definitions

  • the invention relates to crosslinked swellable polymers containing anionic sites that after swelling can be further crosslinked in situ with cationic crosslinkers, such as polyvalent metal cations or cationic polymers, and methods for making same.
  • cationic crosslinkers such as polyvalent metal cations or cationic polymers
  • a particularly important use is as fluid diversion agents for sweep improvement in enhanced oil recovery applications and also as drilling fluids in petroleum production, but applications can also include uses in the hygiene and medical arts, packaging, agriculture, the cable industry, information technology, in the food industry, papermaking, use as flocculation aids, and the like.
  • a "smart gel” is a material that gels in response to a specific physical property. For example, it may gel at a specific temperature or pressure.
  • the water injection method used in oil recovery is where water is injected out into the reservoir to stimulate production. Water is injected for two reasons: 1. For pressure support of the reservoir (also known as voidage replacement). 2. To sweep or displace the oil from the reservoir, and push it towards an oil production well. Normally only 20% of the oil in a reservoir can be extracted, but water injection increases that percentage (known as the recovery factor) and maintains the production rate of a reservoir over a longer period oftime.
  • sweep recovery is limited by the so-called “thief zones,” whereby water preferentially travels through the more permeable regions of the reservoirs, bypassing less permeable zones, leaving unswept oil behind.
  • thief zones whereby water preferentially travels through the more permeable regions of the reservoirs, bypassing less permeable zones, leaving unswept oil behind.
  • One means of further improving recovery is to block thief zones with a polymer or other material, thus forcing water through the less permeable regions.
  • US6454003, US6984705 and US7300973 describe what might be called a "smart polymer” since its properties change in response to particular stimuli.
  • These patents describe an expandable crosslinked polymeric particle having an average particle diameter of about 0.05 to 10 microns.
  • the particle is highly crosslinked with two crosslinkers, one that is stable and a second that is labile.
  • the excess crosslinking makes the initial particles quite small, allowing efficient propagation through the pores of a reservoir.
  • the reversible (labile) internal crosslinks break, allowing the particle to further expand by absorbing additional injection fluid, usually water.
  • the initial polymeric particle is sometimes called the "kernel” before its expansion, in analogy to the way a kernel of popcorn "pops" in response to certain stimuli, such as heat.
  • this particle allows it to fill the high permeability zones — commonly called thief zones or streaks — and then be expanded so that the swollen particle blocks the thief zones and subsequent injections of fluid are forced to enter the remainder of the reservoir, more effectively sweeping the reservoir.
  • the method is limited in practice because subsequent water injections always remove some of the polymer, thus the thief zones become washed out and again transport most of the injection water limiting the injection fluid entering the less permeable zones.
  • the reason for the washout is not certain, but our own research suggests that the swollen polymer is not in gel form, thus although viscous, is a liquid and can be washed out of the porous substrate.
  • the invention generally relates to smart gels that have stable and labile crosslinkers, allowing swelling in situ in response to a particular stimuli. Further, the swelled polymeric particles contain anionic sites that become accessible on swelling of the polymer and can then be further crosslinked using cationic crosslinkers, such as polyvalent metal crosslinkers or cationic polymers to produce gels.
  • cationic crosslinkers such as polyvalent metal crosslinkers or cationic polymers to produce gels.
  • Some of the more common inorganic crosslinking agents include cations of chromium, iron, vanadium, aluminates, borates, titanium, zirconium, aluminum, and their salts, chelates and complexes thereof. Complexed or chelated metal cations are preferred because they slow the rate of gelation, as are nanoparticles that slowly release metal ions.
  • Common organic cationic polymers include polyethyleneimine and the polyquaternium polymers.
  • the anionic sites include the various acids such carboxylic, nitric, phosphoric, chromic, sulfuric, sulphonic, vinylogous carboxylic acids and the like.
  • Suitable polymers having anionic sites include biopolysaccharides, cellulose ethers, and acrylamide-based polymers, with negatively charged monomers.
  • the smart gels of the invention comprise a highly crosslinked expandable polymeric particles having labile crosslinkers and stable crosslinkers, wherein at least one of the monomers that makes up the polymer or copolymer contains anionic sites.
  • a suitable cationic crosslinker is added to the particles after they are made or after the labile crosslinker degrades or any time therebetween.
  • the cationic crosslinker can be injected after swelling of the polymer, but it can also be combined with the unexpanded particle in the initial injection fluid, and if necessary for the application, the rate of gelation can be delayed by means known in the art in order to allow the particle to fully swell before commencing the gelation.
  • anionic particles and a second population of cationic crosslinker loaded particles can be combined and used.
  • the polymer of the invention has particular use in oil recovery, as described above, and is preferably a hydrophilic polymer for this application.
  • such polymers would find uses in all of the arts where swellable polymers are in current use and loss is not desired, including as filler for diapers and other hygiene products, medical devices such as orthopedic insoles, ocular devices, and biomimetic implants, wipe and spill control agents, wire and cable water-blocking agents, ice shipping packs, controlled drug release, agricultural uses (e.g., soil additive to conserve water, plant root coating to increase water availability, and seed coating to increase germination rates), industrial thickeners, specialty packaging, tack reduction for natural rubber, fine coal dewatering, and the like.
  • polymer By “polymer” what is meant is polymerized monomers, including mixtures of two or more monomers.
  • a “stable crosslinker” is defined herein to be any crosslinker that is not degraded under the stimuli that causes the labile crosslinker to disintegrate.
  • Representative non-labile crosslinkers include methylene bisacrylamide, diallylamine, triallylamine, divinyl sulfone, diethyleneglycol diallyl ether, and the like and combinations thereof.
  • a preferred non-labile crosslinking monomer is methylene bisacrylamide.
  • labile crosslinker is defined herein to be any crosslinker that decays or is reversible on application of a particular stimulus, such as irradiation, suitable pH, temperature, etc. and combinations thereof.
  • Representative labile crosslinkers include acrylate or methacrylate esters of di, tri, tetra hydroxy compounds including ethyleneglycol diacrylate, polyethyleneglycol diacrylate, trimethylopropane trimethacrylate, ethoxylated trimethylol triacrylate, ethoxylated pentaerythritol tetracrylate, and the like; divinyl or diallyl compounds separated by an azo such as the diallylamide of 2,2'-Azobis(isbutyric acid) and the vinyl or allyl esters of di or tri functional acids, and combinations thereof.
  • Preferred labile crossl inking monomers include water soluble diacrylates such as polyethylene glycol (PEG) 200-1000 diacrylate, especially PEG 200 diacrylate and PEG 400 diacrylate, and polyfunctional vinyl derivatives of a polyalcohol such as ethoxylated (9- 20) trimethylol triacrylate and polymethyleneglycol diacrylate.
  • PEG polyethylene glycol
  • PEG 400 diacrylate especially PEG 200 diacrylate and PEG 400 diacrylate
  • polyfunctional vinyl derivatives of a polyalcohol such as ethoxylated (9- 20) trimethylol triacrylate and polymethyleneglycol diacrylate.
  • Y is a lower alkyl
  • n and m are independently an integer of between 1 and 10 and Rl and R2 are independently a lower alkyl.
  • BDEP 2-bis[2,2'-di(N-vinylformamido)ethoxy]propane
  • NVFEE 2-(N- vinylformamido)ethyl ether
  • cross linkers can be advantageously combined with the monomers described therein, such as N-vinyl pyrollidone,.N-vinyl formamide, N-vinylacetamide, N-vinylacetamine and other vinyl containing polymers and copolymers thereof, and may be preferred where the neurotoxic effects of acrylamide are to be avoided.
  • “Cationic crosslinkers” are defined herein to be molecules that can crosslink the anionic polymers, and include cationic polymers and polyvalent metals, chelated polyvalent metals, and compounds or complexes capable of yielding polyvalent metals.
  • complex or “complexed” what is meant is that the polyvalent metal crosslinker is present with or within another molecule that will release the metal ions under the conditions of use, and includes the use of metal salts, chelates, nanoparticles, and the like.
  • the proportion of stable to labile crosslinker can also vary depending on how much swelling on stimulus is required, but in the enhanced oil recovery applications a great deal of swelling is desired to effectively block the thief zones and increase the mobilization and/or recovery rate of hydrocarbon fluids present in the formations.
  • the concentration of labile crosslinker greatly exceeds the concentration of stable crosslinker.
  • the crosslinker content is about 1,000-200,000 ppm of labile crosslinker and from 0-300 ppm of non-labile crosslinkers.
  • Combinations of multiple stable and labile crosslinkers can also be employed advantageously.
  • Reaction to stimuli can also be controlled by labile crosslinker selection, as needed for particular reservoir conditions or for the application at issue.
  • judicious selection of labile crosslinkers one that degrades at a very high temperature and another at a lower temperature — can affect the temperature and pH at which the kernel pops.
  • crosslinkers include, but are not limited to, diacrylyl tertiary amides, diacrylylpiperazine, diallyltartardiamide (DATD), dihydroxyethylene-bis-acrylamide (DHEBA), and bis-acrylylcystamine (BAC), trimethylolpropane trimethacrylate (TMPTMA), propyleneglycol triacrylate (PGTA), tripropyleneglycol diacrylate (TPGDA), allyl methacrylate (AMA), triethyleneglycol dimethacrylate (TEGDMA), tetrahydrofurfuryl methacrylate (TFMA) and trimethylolpropane triacrylate (TMPTA).
  • Multifunctional crosslinkers include, but are not limited to, pentaerythritol triacrylate, 1,5 pentane diol dimethacrylate, and pentaerythritol triallylether.
  • carboxylate and/or other anionic constituents are the crosslinking sites in the polymer and that the polymer cannot gel if there are too few crosslinking sites in the polymer, i.e., less than about 1.0 mole percent based on the total number of monomeric groups in the polymer.
  • US4683949 shows gelation rates for a number of different polymers and conditions and is incorporated herein by reference.
  • the solvent of the gelation system is an aqueous liquid, such as deionized water, potable water, fresh water, or brine having a total dissolved solids concentration up to the solubility limit of the solids in water.
  • aqueous liquid such as deionized water, potable water, fresh water, or brine having a total dissolved solids concentration up to the solubility limit of the solids in water.
  • Inert fillers known in the art may also be added to the gelation system to reinforce the subsequent gel if desired or for use as proppants. Such fillers include crushed or naturally fine rock material or glass beads, sand and the like.
  • anionic monomers that can be used include the following acids and their sodium, potassium and ammonium salts: acrylic acid, methacrylic acid, maleic acid, itaconic acid, 2-propenoic acid, 2-methyl-2-propenoic acid, 2-acrylamido-2-methyl propane sulfonic acid, sulfopropyl acrylic acid and other water-soluble forms of these or other polymerizable carboxylic or sulphonic acids, sulphomethylated acrylamide, allyl sulphonic acid, vinyl sulphonic acid, and the like.
  • Preferred anionic monomers include sodium acrylates.
  • Nonionic monomers include acrylamide, N-isopropylacrylamide, N,N-dimethylacrylamide, N,N-diethylacrylamide, dimethylaminopropyl acrylamide, dimethylaminopropyl methacrylamide, acryloyl morpholine, hydroxyethyl acrylate, hydroxypropyl acrylate, hydroxyethyl methacrylate, hydroxypropyl methacrylate, dimethy lam inoethylacry late (DMAEA), dimethylaminoethyl methacrylate (DMAEM), maleic anhydride, N-vinyl pyrrolidone, vinyl acetate and N-vinyl formamide.
  • DAEA dimethy lam inoethylacry late
  • DMAEM dimethylaminoethyl methacrylate
  • Preferred nonionic monomers include acrylamide, N-methylacrylamide, N,N-dimethylacrylamide and methacrylamide.
  • Acrylamide is more preferred.
  • N-vinyl pyrollidone,.N-vinyl formamide, N-vinylacetamide, N-vinylacetamine and copolymers may be preferred with the acid labile ketal crosslinkers of US2008075667.
  • Cationic and betaine monomers can be combined with the polymeric particles of the invention, but their use is not preferred as they would compete for binding to the anionic sites. However, small amounts may be acceptable, provided the anionic sites predominate.
  • Representative swellable polymers also include polymers and copolymers of acrylamide and 2-acrylamido-2-methyl propane sulfonic acid (and its sodium salt), copolymers of acrylamide and sodium acrylate, terpolymers of acrylamide, 2-acrylamido-2- methyl propane sulfonic acid (and its sodium salt) and sodium acrylate and homopolymers of 2-acrylamido-2-methyl propane sulfonic acid (and its sodium salts), poly(2-hydroxyethyl methacrylate), poly(2-hydroxypropyl methacrylate), poly(isobutylene-co-maleic acid), and the like.
  • polyvalent metal crosslinker of the present invention is defined as a salt or a complex of a tri- or quatravalent metal cation wherein the metal cation is capable of crosslinking a polymer having anionic sites.
  • Exemplary polyvalent metal crosslinking agents useful in the practice of the present invention are complexes or chelates OfAl 3+ , Fe 3+ , Cr 3+ , Ti 4+ , Sn 4+ , Zr 4+ and the like.
  • Preferred crosslinking agents of the present invention contain Al 3+ , Zr 4+ or Cr 3+ , and their acetates, nitrates, phosphates, carbonates, tartrates, malonates, propionates, benzoates, or citrates thereof, and the like. Combinations of cationic crosslinkers can also be used.
  • the polyvalent metal cations can be employed in the form of complexes with an effective sequestering amount of one or more chelating or sequestering anions. Slow release nanoparticles and macroparticles can also be employed. Chromium and zirconium are the preferred cations in high salinity brines including hard brine. High salinity brine contains on the order of at least about 30,000 ppm total dissolved solids. Thus, the combination of the particular chelating or sequestering agent in conjunction with the preferred chromium(III) and Zr(IV) cations confers high brine tolerance.
  • the cationic polymers of the invention include homopolymers of the following: dimethyldiallyl ammonium chloride, ethyleneimine, methacrylamido propyl trimethyl ammonium chloride, 2-methacryloyloxyethyl trimethyl ammonium methosulfate and diquaternary ionene, and the like.
  • a preferred cationic crosslinker is polyethyleneimine (PEI), which has a high charge ratio.
  • the particles can be prepared by methods known in the art, including the inverse emulsion polymerization technique described in US6454003, US6729402 and US6984705.
  • Particle suspensions are prepared by mixing the particles with injection fluid, or inverse suspensions of particles are inverted with a surfactant and/or sufficient shearing and additional injection fluid can be added if needed.
  • the aqueous solution may also contain other conventional additives including chelating agents, pH adjusters, initiators and other conventional additives, accelerators, retardants, surfactants, stabilizers, etc., as appropriate for the particular application.
  • the rate of gelation with the polymers can be controlled, as is known in the art.
  • temperature and pH can affect the rate of gelation, as can the use of metal complexes or metal nanoparticles or other means to slow the rate of release of metal cations, as needed for a particular application.
  • the gels can be destroyed with the use of strong oxidizing agents such as sodium hypochlorite.
  • the invention is a composition comprising a fluid, a cationic crosslinker and expandable polymeric particles having anionic sites and both labile and stable crosslinkers.
  • the invention is a composition comprising expandable polymeric particles having anionic sites and both labile and stable crosslinkers, said particle combined with a fluid and a cationic crosslinker that is capable of crosslinking the anionic sites in the popped polymer and forming a gel that is resistant to washout.
  • the invention is a composition
  • a composition comprising highly crosslinked expandable polymeric particles having an unexpanded volume average particle size diameter of from about 0.05 to about 10 microns and a crosslinking agent content of from about 1,000 to about 200,000 ppm of labile crosslinkers and from 0 to about 300 ppm of stable crosslinkers, combined with a cationic crosslinker and a fluid.
  • the invention is a method of increasing the recovery of hydrocarbon fluids in a subterranean formation comprising injecting into the subterranean formation a composition comprising a fluid, a cationic crosslinker, and a highly crosslinked expandable polymeric particle having anionic sites, wherein polymeric particle has an unexpanded volume average particle size diameter of 0.05-10 microns and a crosslinker content of about 1,000-200,000 ppm of labile crosslinker and about 0-300 ppm of stable crosslinker, said polymeric particle has a smaller diameter than the pore throats of the subterranean formation, and said labile crosslinkers break under the conditions of temperature and suitable pH in the subterranean formation to allow the polymeric particle to expand, thus exposing the anionic sites so that said cationic crosslinker can react with the anionic sites to form a gel.
  • the polymeric particles can be a copolymer of acrylamide and sodium acrylate
  • the stable crosslinker can be methylene bisacrylamide
  • the labile crosslinker can be a polyethylene glycol diacrylate.
  • the cationic crosslinker is selected from polyethyleneimine, Al 3+ , Fe 3+ , Cr 3+ , Ti 4+ , Sn 4+ , or Zr 4+ .
  • the invention provides a novel polymer containing anionic sites that swells on a stimuli and is then additionally treated with a cationic crosslinker that acts to gel the polymer by providing additional crosslinking.
  • a cationic crosslinker that acts to gel the polymer by providing additional crosslinking.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Materials Engineering (AREA)
  • Geology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Polymers & Plastics (AREA)
  • Medicinal Chemistry (AREA)
  • Mining & Mineral Resources (AREA)
  • Health & Medical Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Environmental & Geological Engineering (AREA)
  • Fluid Mechanics (AREA)
  • Physics & Mathematics (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Medicinal Preparation (AREA)

Abstract

The invention is directed to stable crosslinked water-soluble swellable polymers and methods for making same. More particularly, the invention relates to a composition comprising expandable polymeric particles having anionic sites and labile crosslinkers and stable crosslinkers, said particle mixed with a fluid and a cationic crosslinker that is capable of further crosslinking the particle on degradation of the labile crosslinker and exposure of the anionic sites so as to form a gel. A particularly important use is as an injection fluid in petroleum production, where the expandable polymeric particles are injected into target zone and when the heat and/or pH of the target zone cause degradation of the labile crosslinker and the particle expands, the cationic crosslinker crosslinks the polymer to form a gel, thus diverting water to lower permeability regions and improving oil recovery.

Description

SWELLABLE POLYMER WITH ANIONIC SITES
CROSS-REFERENCE TO RELATED APPLICATIONS
This application is claims priority to U.S. Provisional Application No. 61/185626 filed June 10, 2009, which is incorporated herein by reference in its entirety.
FEDERALLY SPONSORED RESEARCH STATEMENT
Not applicable.
REFERENCE TO MICROFICHE APPENDIX
Not applicable.
FIELD OF THE INVENTION
The invention relates to crosslinked swellable polymers containing anionic sites that after swelling can be further crosslinked in situ with cationic crosslinkers, such as polyvalent metal cations or cationic polymers, and methods for making same. A particularly important use is as fluid diversion agents for sweep improvement in enhanced oil recovery applications and also as drilling fluids in petroleum production, but applications can also include uses in the hygiene and medical arts, packaging, agriculture, the cable industry, information technology, in the food industry, papermaking, use as flocculation aids, and the like.
BACKGROUND OF THE INVENTION
A "smart gel" is a material that gels in response to a specific physical property. For example, it may gel at a specific temperature or pressure. Although finding many industrial uses, our interest in smart gels lies in their uses in oil and gas production, and in particular as a diverting agent to improve oil recovery from reservoirs. The water injection method used in oil recovery is where water is injected out into the reservoir to stimulate production. Water is injected for two reasons: 1. For pressure support of the reservoir (also known as voidage replacement). 2. To sweep or displace the oil from the reservoir, and push it towards an oil production well. Normally only 20% of the oil in a reservoir can be extracted, but water injection increases that percentage (known as the recovery factor) and maintains the production rate of a reservoir over a longer period oftime.
However, sweep recovery is limited by the so-called "thief zones," whereby water preferentially travels through the more permeable regions of the reservoirs, bypassing less permeable zones, leaving unswept oil behind. One means of further improving recovery is to block thief zones with a polymer or other material, thus forcing water through the less permeable regions.
US6454003, US6984705 and US7300973 describe what might be called a "smart polymer" since its properties change in response to particular stimuli. These patents describe an expandable crosslinked polymeric particle having an average particle diameter of about 0.05 to 10 microns. The particle is highly crosslinked with two crosslinkers, one that is stable and a second that is labile. The excess crosslinking makes the initial particles quite small, allowing efficient propagation through the pores of a reservoir. On heating to reservoir temperature and/or at a predetermined pH or other stimuli, the reversible (labile) internal crosslinks break, allowing the particle to further expand by absorbing additional injection fluid, usually water. The initial polymeric particle is sometimes called the "kernel" before its expansion, in analogy to the way a kernel of popcorn "pops" in response to certain stimuli, such as heat.
The unique properties of this particle allows it to fill the high permeability zones — commonly called thief zones or streaks — and then be expanded so that the swollen particle blocks the thief zones and subsequent injections of fluid are forced to enter the remainder of the reservoir, more effectively sweeping the reservoir. However, the method is limited in practice because subsequent water injections always remove some of the polymer, thus the thief zones become washed out and again transport most of the injection water limiting the injection fluid entering the less permeable zones. The reason for the washout is not certain, but our own research suggests that the swollen polymer is not in gel form, thus although viscous, is a liquid and can be washed out of the porous substrate.
What is needed in the art is a "smart gel" that is less susceptible to loss under the conditions of use. In particular, a swellable polymer that is resistant to wash out by subsequent fluid injections is needed, but the polymers will have utility in any application where swellable polymers are desired.
SUMMARY OF THE INVENTION
The invention generally relates to smart gels that have stable and labile crosslinkers, allowing swelling in situ in response to a particular stimuli. Further, the swelled polymeric particles contain anionic sites that become accessible on swelling of the polymer and can then be further crosslinked using cationic crosslinkers, such as polyvalent metal crosslinkers or cationic polymers to produce gels.
Some of the more common inorganic crosslinking agents include cations of chromium, iron, vanadium, aluminates, borates, titanium, zirconium, aluminum, and their salts, chelates and complexes thereof. Complexed or chelated metal cations are preferred because they slow the rate of gelation, as are nanoparticles that slowly release metal ions. Common organic cationic polymers include polyethyleneimine and the polyquaternium polymers.
The anionic sites include the various acids such carboxylic, nitric, phosphoric, chromic, sulfuric, sulphonic, vinylogous carboxylic acids and the like. Suitable polymers having anionic sites include biopolysaccharides, cellulose ethers, and acrylamide-based polymers, with negatively charged monomers.
Preferably, the smart gels of the invention comprise a highly crosslinked expandable polymeric particles having labile crosslinkers and stable crosslinkers, wherein at least one of the monomers that makes up the polymer or copolymer contains anionic sites. A suitable cationic crosslinker is added to the particles after they are made or after the labile crosslinker degrades or any time therebetween. In certain embodiments it may be possible to convert a nonionic polymer to an anionic polymer, but the incorporation of anionic monomers is preferred to ensure adequate dispersion of anionic sites and for ease of use.
In reservoir applications, the cationic crosslinker can be injected after swelling of the polymer, but it can also be combined with the unexpanded particle in the initial injection fluid, and if necessary for the application, the rate of gelation can be delayed by means known in the art in order to allow the particle to fully swell before commencing the gelation. In yet another embodiment, anionic particles and a second population of cationic crosslinker loaded particles can be combined and used.
The polymer of the invention has particular use in oil recovery, as described above, and is preferably a hydrophilic polymer for this application. However, such polymers would find uses in all of the arts where swellable polymers are in current use and loss is not desired, including as filler for diapers and other hygiene products, medical devices such as orthopedic insoles, ocular devices, and biomimetic implants, wipe and spill control agents, wire and cable water-blocking agents, ice shipping packs, controlled drug release, agricultural uses (e.g., soil additive to conserve water, plant root coating to increase water availability, and seed coating to increase germination rates), industrial thickeners, specialty packaging, tack reduction for natural rubber, fine coal dewatering, and the like.
By "polymer" what is meant is polymerized monomers, including mixtures of two or more monomers.
A "stable crosslinker" is defined herein to be any crosslinker that is not degraded under the stimuli that causes the labile crosslinker to disintegrate. Representative non-labile crosslinkers include methylene bisacrylamide, diallylamine, triallylamine, divinyl sulfone, diethyleneglycol diallyl ether, and the like and combinations thereof. A preferred non-labile crosslinking monomer is methylene bisacrylamide.
The "labile crosslinker" is defined herein to be any crosslinker that decays or is reversible on application of a particular stimulus, such as irradiation, suitable pH, temperature, etc. and combinations thereof. Representative labile crosslinkers include acrylate or methacrylate esters of di, tri, tetra hydroxy compounds including ethyleneglycol diacrylate, polyethyleneglycol diacrylate, trimethylopropane trimethacrylate, ethoxylated trimethylol triacrylate, ethoxylated pentaerythritol tetracrylate, and the like; divinyl or diallyl compounds separated by an azo such as the diallylamide of 2,2'-Azobis(isbutyric acid) and the vinyl or allyl esters of di or tri functional acids, and combinations thereof. Preferred labile crossl inking monomers include water soluble diacrylates such as polyethylene glycol (PEG) 200-1000 diacrylate, especially PEG 200 diacrylate and PEG 400 diacrylate, and polyfunctional vinyl derivatives of a polyalcohol such as ethoxylated (9- 20) trimethylol triacrylate and polymethyleneglycol diacrylate.
US2008075667, herein incorporated by reference, describes additional acid labile ketal cross linkers that can be used in the invention. Such acid labile ketal crosslinker have one of the following formulas:
Figure imgf000006_0001
. (CH2Jn (CH2)m
Figure imgf000006_0002
wherein Y is a lower alkyl, n and m are independently an integer of between 1 and 10 and Rl and R2 are independently a lower alkyl. In particular, 2-bis[2,2'-di(N-vinylformamido)ethoxy]propane (BDEP) and 2-(N- vinylformamido)ethyl ether (NVFEE) are described and may be suitable in acidic environments, or where the acid is later added thereto. Such cross linkers can be advantageously combined with the monomers described therein, such as N-vinyl pyrollidone,.N-vinyl formamide, N-vinylacetamide, N-vinylacetamine and other vinyl containing polymers and copolymers thereof, and may be preferred where the neurotoxic effects of acrylamide are to be avoided.
"Cationic crosslinkers" are defined herein to be molecules that can crosslink the anionic polymers, and include cationic polymers and polyvalent metals, chelated polyvalent metals, and compounds or complexes capable of yielding polyvalent metals.
By "complex" or "complexed" what is meant is that the polyvalent metal crosslinker is present with or within another molecule that will release the metal ions under the conditions of use, and includes the use of metal salts, chelates, nanoparticles, and the like.
The proportion of stable to labile crosslinker can also vary depending on how much swelling on stimulus is required, but in the enhanced oil recovery applications a great deal of swelling is desired to effectively block the thief zones and increase the mobilization and/or recovery rate of hydrocarbon fluids present in the formations. Thus, the concentration of labile crosslinker greatly exceeds the concentration of stable crosslinker. To obtain sizes in the range of about 0.05 to about 10 microns suitable for injection fluid use the crosslinker content is about 1,000-200,000 ppm of labile crosslinker and from 0-300 ppm of non-labile crosslinkers.
Combinations of multiple stable and labile crosslinkers can also be employed advantageously. Reaction to stimuli can also be controlled by labile crosslinker selection, as needed for particular reservoir conditions or for the application at issue. For example, judicious selection of labile crosslinkers — one that degrades at a very high temperature and another at a lower temperature — can affect the temperature and pH at which the kernel pops.
Other crosslinkers include, but are not limited to, diacrylyl tertiary amides, diacrylylpiperazine, diallyltartardiamide (DATD), dihydroxyethylene-bis-acrylamide (DHEBA), and bis-acrylylcystamine (BAC), trimethylolpropane trimethacrylate (TMPTMA), propyleneglycol triacrylate (PGTA), tripropyleneglycol diacrylate (TPGDA), allyl methacrylate (AMA), triethyleneglycol dimethacrylate (TEGDMA), tetrahydrofurfuryl methacrylate (TFMA) and trimethylolpropane triacrylate (TMPTA). Multifunctional crosslinkers include, but are not limited to, pentaerythritol triacrylate, 1,5 pentane diol dimethacrylate, and pentaerythritol triallylether.
It is believed that the carboxylate and/or other anionic constituents are the crosslinking sites in the polymer and that the polymer cannot gel if there are too few crosslinking sites in the polymer, i.e., less than about 1.0 mole percent based on the total number of monomeric groups in the polymer. US4683949 shows gelation rates for a number of different polymers and conditions and is incorporated herein by reference.
The solvent of the gelation system is an aqueous liquid, such as deionized water, potable water, fresh water, or brine having a total dissolved solids concentration up to the solubility limit of the solids in water. Inert fillers known in the art may also be added to the gelation system to reinforce the subsequent gel if desired or for use as proppants. Such fillers include crushed or naturally fine rock material or glass beads, sand and the like.
Representative anionic monomers that can be used include the following acids and their sodium, potassium and ammonium salts: acrylic acid, methacrylic acid, maleic acid, itaconic acid, 2-propenoic acid, 2-methyl-2-propenoic acid, 2-acrylamido-2-methyl propane sulfonic acid, sulfopropyl acrylic acid and other water-soluble forms of these or other polymerizable carboxylic or sulphonic acids, sulphomethylated acrylamide, allyl sulphonic acid, vinyl sulphonic acid, and the like. Preferred anionic monomers include sodium acrylates.
Representative nonionic monomers include acrylamide, N-isopropylacrylamide, N,N-dimethylacrylamide, N,N-diethylacrylamide, dimethylaminopropyl acrylamide, dimethylaminopropyl methacrylamide, acryloyl morpholine, hydroxyethyl acrylate, hydroxypropyl acrylate, hydroxyethyl methacrylate, hydroxypropyl methacrylate, dimethy lam inoethylacry late (DMAEA), dimethylaminoethyl methacrylate (DMAEM), maleic anhydride, N-vinyl pyrrolidone, vinyl acetate and N-vinyl formamide. Preferred nonionic monomers include acrylamide, N-methylacrylamide, N,N-dimethylacrylamide and methacrylamide. Acrylamide is more preferred. N-vinyl pyrollidone,.N-vinyl formamide, N-vinylacetamide, N-vinylacetamine and copolymers may be preferred with the acid labile ketal crosslinkers of US2008075667.
Cationic and betaine monomers can be combined with the polymeric particles of the invention, but their use is not preferred as they would compete for binding to the anionic sites. However, small amounts may be acceptable, provided the anionic sites predominate.
Representative swellable polymers also include polymers and copolymers of acrylamide and 2-acrylamido-2-methyl propane sulfonic acid (and its sodium salt), copolymers of acrylamide and sodium acrylate, terpolymers of acrylamide, 2-acrylamido-2- methyl propane sulfonic acid (and its sodium salt) and sodium acrylate and homopolymers of 2-acrylamido-2-methyl propane sulfonic acid (and its sodium salts), poly(2-hydroxyethyl methacrylate), poly(2-hydroxypropyl methacrylate), poly(isobutylene-co-maleic acid), and the like.
The "polyvalent metal crosslinker" of the present invention is defined as a salt or a complex of a tri- or quatravalent metal cation wherein the metal cation is capable of crosslinking a polymer having anionic sites. Exemplary polyvalent metal crosslinking agents useful in the practice of the present invention are complexes or chelates OfAl3+, Fe3+, Cr3+, Ti4+, Sn4+, Zr4+ and the like. Preferred crosslinking agents of the present invention contain Al3+ , Zr4+ or Cr3+, and their acetates, nitrates, phosphates, carbonates, tartrates, malonates, propionates, benzoates, or citrates thereof, and the like. Combinations of cationic crosslinkers can also be used.
The polyvalent metal cations can be employed in the form of complexes with an effective sequestering amount of one or more chelating or sequestering anions. Slow release nanoparticles and macroparticles can also be employed. Chromium and zirconium are the preferred cations in high salinity brines including hard brine. High salinity brine contains on the order of at least about 30,000 ppm total dissolved solids. Thus, the combination of the particular chelating or sequestering agent in conjunction with the preferred chromium(III) and Zr(IV) cations confers high brine tolerance.
The cationic polymers of the invention include homopolymers of the following: dimethyldiallyl ammonium chloride, ethyleneimine, methacrylamido propyl trimethyl ammonium chloride, 2-methacryloyloxyethyl trimethyl ammonium methosulfate and diquaternary ionene, and the like. A preferred cationic crosslinker is polyethyleneimine (PEI), which has a high charge ratio.
The particles can be prepared by methods known in the art, including the inverse emulsion polymerization technique described in US6454003, US6729402 and US6984705. Particle suspensions are prepared by mixing the particles with injection fluid, or inverse suspensions of particles are inverted with a surfactant and/or sufficient shearing and additional injection fluid can be added if needed.
In addition to the expandable polymeric particles having anionic sites and both labile and stable crosslinkers and the cationic crosslinker, the aqueous solution may also contain other conventional additives including chelating agents, pH adjusters, initiators and other conventional additives, accelerators, retardants, surfactants, stabilizers, etc., as appropriate for the particular application.
The rate of gelation with the polymers can be controlled, as is known in the art. Thus, temperature and pH can affect the rate of gelation, as can the use of metal complexes or metal nanoparticles or other means to slow the rate of release of metal cations, as needed for a particular application. In addition, the gels can be destroyed with the use of strong oxidizing agents such as sodium hypochlorite.
In one embodiment, the invention is a composition comprising a fluid, a cationic crosslinker and expandable polymeric particles having anionic sites and both labile and stable crosslinkers. In another embodiment, the invention is a composition comprising expandable polymeric particles having anionic sites and both labile and stable crosslinkers, said particle combined with a fluid and a cationic crosslinker that is capable of crosslinking the anionic sites in the popped polymer and forming a gel that is resistant to washout.
In another embodiment, the invention is a composition comprising highly crosslinked expandable polymeric particles having an unexpanded volume average particle size diameter of from about 0.05 to about 10 microns and a crosslinking agent content of from about 1,000 to about 200,000 ppm of labile crosslinkers and from 0 to about 300 ppm of stable crosslinkers, combined with a cationic crosslinker and a fluid.
In another embodiment, the invention is a method of increasing the recovery of hydrocarbon fluids in a subterranean formation comprising injecting into the subterranean formation a composition comprising a fluid, a cationic crosslinker, and a highly crosslinked expandable polymeric particle having anionic sites, wherein polymeric particle has an unexpanded volume average particle size diameter of 0.05-10 microns and a crosslinker content of about 1,000-200,000 ppm of labile crosslinker and about 0-300 ppm of stable crosslinker, said polymeric particle has a smaller diameter than the pore throats of the subterranean formation, and said labile crosslinkers break under the conditions of temperature and suitable pH in the subterranean formation to allow the polymeric particle to expand, thus exposing the anionic sites so that said cationic crosslinker can react with the anionic sites to form a gel.
In preferred embodiments, the polymeric particles can be a copolymer of acrylamide and sodium acrylate, the stable crosslinker can be methylene bisacrylamide, and the labile crosslinker can be a polyethylene glycol diacrylate. The cationic crosslinker is selected from polyethyleneimine, Al3+, Fe3+, Cr3+, Ti4+, Sn4+, or Zr4+.
DESCRIPTION OF EMBODIMENTS OF THE INVENTION
The invention provides a novel polymer containing anionic sites that swells on a stimuli and is then additionally treated with a cationic crosslinker that acts to gel the polymer by providing additional crosslinking. Such smart gels have particular utility in sweeping reservoirs, but many uses are possible.
EXAMPLE 1: PRIOR ART
We ran a number of slim tube tests in which we injected about 1 pore volume of BRIGHTWATER® particles (NALCO®, copolymer of acrylamide and sodium AMPS crosslinked with methylene bis-acrylamide and PEG diacrylate) into 40' slim tubes packed with sand. The sand pack was then heated (150 -19O0F) to allow the polymer to pop. Afterwards, water was injected into the sand packs and the resistance to the flow of water measured. While the popped polymers initially exhibited good resistance factors, this behavior appeared to washout with additional water injection. Typically within one pore volume of water injection the Residual Resistance Factor (RRF) dropped to a number about 1-2. This behavior was observed with slim tubes which were packed with 6.7 Darcy sand as well as 1 Darcy sand. Therefore, the treatment effect of porous media with these particles was only temporary.
EXAMPLE 2: INVENTION
Since the prior art polymer is subject to washout, we propose that when combined with suitable anionic sites and further crosslinked with polyvalent metal cations or a cationic polymer, such as PEI, the resulting gel will remain resistant to washout! After the polymer reaches the target zone in the reservoir, the unstable internal crosslinkers PEG-200 or PEG-400 diacrylates hydrolyze and the particle then opens up (swells, pops). The addition of the cationic crosslinker such as Cr3+ or PEI will crosslink the expanded polymeric particles via the anionic sites, and is predicted to result in gel that is much more resistant to washout.
We injected a gelant mixture containing 0.5% anionic microparticles of the present invention along with crosslinker-loaded particles containing 100 ppm Cr(III) and 1200 ppm PEI into a 30' long slim tube (6 sections, 5' each) packed with 4.5 Darcy sand. The gelant was injected into the first 0.5 PV of the sandpack and then pushed slightly further into the tube with additional brine injection. The sandpack system was then shut in at 1500F to allow the gelation to occur. Several ampoules containing the gelant mixture were also placed in the oven to monitor the gelation progress. Brine was periodically injected into the sandpack and the resistance to the flow was measured. The flow resistance gradually increased over time, and eventually a persistent ultra-high (> 2000) RRF value was achieved, indicating superiority of the invention polymer over prior art example.
The following references are incorporated by reference herein in their entirety.
US6454003, US6729402 and US6984705
US3727688
US4068714
US3749172
US4683949

Claims

US2008075667What is claimed is:
1. A composition comprising expandable polymeric particles having anionic sites and being crosslinked with both labile crosslinkers and stable crosslinkers, said particle combined with a fluid and a cationic crosslinker that is capable of further crosslinking the particle on degradation of the labile crosslinker so as to form a gel.
2. The composition of claim 1, wherein the anionic site is selected from the group consisting of a carboxylate, a sulphate, a sulphonate, a nitrate, or a phosphate groups.
3. The composition of claim 1, wherein the cationic crosslinker is at least one selected from the group consisting of, Al3+, Fe3+, Cr3+, Ti4+, Sn4+, Zr4+Or polyethyleneimine (PEI).
4. The composition of claim 1 wherein the expandable polymeric particles comprise a copolymer of acrylamide and sodium acrylate.
5. The composition of claim 1, wherein the stable crosslinker is methylene bisacrylamide and the labile crosslinker is a diacrylate.
6. The composition of claim 1, wherein the expandable polymeric particles comprise a copolymer of acrylamide and sodium acrylate, the stable crosslinker comprises methylene bisacrylamide, and the labile crosslinker comprises a polyethylene glycol diacrylate, and the cationic crosslinker is a polyvalent metal cation or a cationic polymer.
7. The composition of claim 1, wherein the expandable polymeric particles comprise a copolymer of acrylamide and sodium acrylate, the stable crosslinker comprises methylene bisacrylamide, the labile crosslinker comprises a polyethylene glycol diacrylate, and the cationic crosslinker is at least one selected from the group consisting of a cationic polymer, Al3+, Fe3+, Cr3+, Ti4+, Sn4+, Zr4+ and complexes or nanoparticles containing same.
8. The composition of claim 1, wherein the labile crosslinker is an acid labile ketal of the formula:
Figure imgf000015_0001
or
Figure imgf000015_0002
wherein Y is a lower alkyl, where wherein n and m are independently an integer of between 1 and 10, and wherein Rl and R2 are independently a lower alkyl.
9. The composition of claim 1, wherein the labile crosslinker is 2-bis[2,2'-di(N- vinylformamido)ethoxy]propane or 2-(N-vinylformamido)ethyl ether.
10. The composition of claim 1, wherein the labile crosslinker is 2-bis[2,2'-di(N- vinylformamido)ethoxy]propane or 2-(N-vinylformamido)ethyl ether and the expandable polymeric particles comprise polymers of N-vinyl formamide, N-vinylacetamide, or N- vinylacetamine, or mixtures thereof.
11. A composition comprising highly crosslinked expandable hydrophilic polymeric particles having anionic sites and an unexpanded volume average particle size diameter of about 0.05 to about 10 microns and a crosslinking agent content of from about 1,000 to about 200,000 ppm of labile crosslinkers and from 0 to about 300 ppm of stable crosslinkers, combined with a cationic crosslinker and a fluid comprising water.
12. The composition of claim 1 1, wherein the cationic crosslinker is at least one selected from the group consisting of PEI, or Al3+, Fe3+, Cr3+, Ti4+, Sn4+, Zr4+ and complexes thereof or nanoparticles containing same.
13. The composition of claim 11 wherein the expandable hydrophilic polymeric particles comprise a copolymer of acrylamide and sodium acrylate.
14. The composition of claim 11, wherein the stable crosslinker is methylene bisacrylamide and the labile crosslinker is polyethylene glycol diacrylate.
15. The composition of claim 11, wherein the labile crosslinker is an acid labile ketal, or 2- bis[2,2'-di(N-vinylformamido)ethoxy]propane or 2-(N-vinylformamido)ethyl ether or the labile crosslinker comprises a diacrylate or polyethylene glycol diacrylate, and the expandable hydrophilic polymeric particles comprise polymers of N-vinyl formamide, N-vinylacetamide, N-vinylacetamine, acrylamide, sodium acrylate or mixtures thereof.
16. A method of increasing the recovery of hydrocarbon fluids from a subterranean formation comprising injecting into the subterranean formation a composition comprising water, a cationic crosslinker, and a highly crosslinked expandable hydrophilic polymeric particle having anionic sites, wherein:
i) said polymeric particle has an unexpanded volume average particle size diameter of 0.05-10 microns and a crosslinker content of about 1,000-200,000 ppm of labile crosslinker and about 0-300 ppm of stable crosslinker,
ii) said polymeric particle has a smaller diameter than the pore throats of the subterranean formation,
iii) said labile crosslinkers break under the conditions of temperature and suitable pH in the subterranean formation to allow the polymeric particle to expand, and iv) said cationic crosslinker then reacts with said expanded polymer to form a gel.
17. The method of claim 16, wherein the cationic crosslinker is a complexed polyvalent cation and is injected into the subterranean formation at the same time as the highly crosslinked expandable polymeric particle.
18. The method of claim 16, wherein the cationic crosslinker is a polyvalent cation and is a injected into the subterranean formation after expansion of the polymeric particle.
19. The method of claim 16, wherein the cationic crosslinker is PEI and is combined with the highly crosslinked expandable hydrophilic polymeric particle prior to injection into the subterranean formation.
PCT/US2010/037988 2009-06-10 2010-06-09 Swellable polymer with anionic sites WO2010144588A1 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
AU2010258802A AU2010258802B2 (en) 2009-06-10 2010-06-09 Swellable polymer with anionic sites
GB201120813A GB2482835B8 (en) 2009-06-10 2010-06-09 Swellable polymer with anionic sites
MX2014006810A MX347441B (en) 2009-06-10 2010-06-09 Swellable polymer with anionic sites.
RU2011153041/04A RU2540068C2 (en) 2009-06-10 2010-06-09 Swelling polymer with anionic sections
MX2011013343A MX2011013343A (en) 2009-06-10 2010-06-09 Swellable polymer with anionic sites.
CN2010800255227A CN102459364A (en) 2009-06-10 2010-06-09 Swellable polymer with anionic sites
CA2761528A CA2761528C (en) 2009-06-10 2010-06-09 Swellable polymer with anionic sites

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US18562609P 2009-06-10 2009-06-10
US61/185,626 2009-06-10

Publications (1)

Publication Number Publication Date
WO2010144588A1 true WO2010144588A1 (en) 2010-12-16

Family

ID=43305416

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2010/037988 WO2010144588A1 (en) 2009-06-10 2010-06-09 Swellable polymer with anionic sites

Country Status (9)

Country Link
US (2) US8669214B2 (en)
CN (2) CN105384869B (en)
AU (1) AU2010258802B2 (en)
CA (1) CA2761528C (en)
GB (1) GB2482835B8 (en)
MX (2) MX2011013343A (en)
MY (1) MY152086A (en)
RU (1) RU2540068C2 (en)
WO (1) WO2010144588A1 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9267075B2 (en) 2009-06-10 2016-02-23 Conocophillips Company Swellable polymer with anionic sites
WO2016084032A1 (en) * 2014-11-28 2016-06-02 Ecopetrol S.A. Formulations of colloidal dispersion gels and surfactants for the improved recovery of petroleum and method of obtaining these formulations
WO2017210486A1 (en) * 2016-06-02 2017-12-07 The Curators Of The University Of Missouri Re-assembling polymer particle package for conformance control and fluid loss control
US11214729B2 (en) 2018-08-31 2022-01-04 The Curators Of The University Of Missouri Re-crosslinking particle gel for CO2 conformance control and CO2 leakage blocking
US11268009B2 (en) 2016-06-02 2022-03-08 The Curators Of The University Of Missouri Fiber assisted re-crosslinkable polymer gel and preformed particle gels for fluid loss and conformance control
CN114478897A (en) * 2021-11-24 2022-05-13 四川轻化工大学 Slow-swelling pre-crosslinked gel particles and preparation method thereof
EP3856864A4 (en) * 2018-10-31 2022-07-06 Kemira Oyj Methods and compositions for enhanced oil recovery
US11549048B2 (en) 2016-06-02 2023-01-10 The Curators Of The University Of Missouri Re-assembling polymer particle package for conformance control and fluid loss control

Families Citing this family (34)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9856415B1 (en) 2007-12-11 2018-01-02 Superior Silica Sands, LLC Hydraulic fracture composition and method
US20170137703A1 (en) 2007-12-11 2017-05-18 Superior Silica Sands, LLC Hydraulic fracture composition and method
US9057014B2 (en) 2007-12-11 2015-06-16 Aquasmart Enterprises, Llc Hydraulic fracture composition and method
US10920494B2 (en) 2007-12-11 2021-02-16 Aquasmart Enterprises, Llc Hydraulic fracture composition and method
US20110166308A1 (en) * 2010-01-07 2011-07-07 Musa Osama M Polymers prepared from mixtures of multifunctional n-vinylformamide and hybrid reactive n-vinylformamide crosslinking monomer moieties and uses thereof
US8720557B2 (en) 2012-01-13 2014-05-13 Halliburton Energy Services, Inc. In-situ crosslinking with aluminum carboxylate for acid stimulation of a carbonate formation
US9120965B2 (en) 2012-01-27 2015-09-01 Nalco Company Composition and method for recovering hydrocarbon fluids from a subterranean reservoir
US20130220608A1 (en) * 2012-02-23 2013-08-29 Halliburton Energy Services, Inc. Modified particulate weighting agents and methods of using the same
CA2770347A1 (en) * 2012-03-02 2013-09-02 The Governors Of The University Of Alberta Temperature switchable polymers for fine coal dewatering
US9399728B2 (en) 2012-10-26 2016-07-26 Halliburton Energy Services, Inc. In-situ crosslinking and calcium ion complexation for acidizing a subterranean formation
CA2892380A1 (en) * 2012-11-26 2014-05-30 Conocophillips Company Crosslinking of swellable polymer with pei
WO2014113112A1 (en) * 2013-01-15 2014-07-24 Conocophillips Company Fluorescent tags for detection of swellable polymers
US11034883B2 (en) 2013-01-28 2021-06-15 The University Of Kansas Low molecular weight polyacrylates for EOR
WO2014130250A2 (en) 2013-02-22 2014-08-28 Conocophillips Company Low ph crossslinking of polymers
US9695350B2 (en) 2013-05-31 2017-07-04 Halliburton Energy Services, Inc. Ampholyte polymeric compounds in subterranean applications
WO2015072875A1 (en) 2013-11-13 2015-05-21 Schlumberger Canada Limited Methods of treating a subterranean formations with fluids comprising proppant
FR3014938B1 (en) * 2013-12-17 2018-04-13 IFP Energies Nouvelles TREATMENT OF PRODUCTION WATER IN ASSISTED RECOVERY BY INTRODUCTION OF TETRAVALENT CATIONS
WO2015126390A1 (en) * 2014-02-19 2015-08-27 Halliburton Energy Services, Inc. Multi-functional additive for oil or gas operations
MX2016016113A (en) * 2014-06-27 2017-03-08 Halliburton Energy Services Inc Controlled swelling of swellable polymers downhole.
CA2959595C (en) 2014-09-24 2018-07-03 Halliburton Energy Services, Inc. Polymeric metal crosslinker for shear tolerant fracturing fluid application
AU2016205306B2 (en) * 2015-01-06 2019-12-12 Conocophillips Company Low molecular weight polyacrylates for EOR
US10479926B2 (en) * 2015-02-17 2019-11-19 Halliburton Energy Services, Inc. Polyamino-functionalized nanoparticles as hardeners for particulate consolidation
US10161235B2 (en) 2016-06-03 2018-12-25 Enhanced Production, Inc. Hydraulic fracturing in highly heterogeneous formations by resisting formation and/or sealing micro-fractures
CN106800623B (en) * 2017-03-01 2018-11-27 苏州瑞科四通新材料有限公司 A kind of anti-algae composite membrane of anionic
RU2019122153A (en) 2017-03-16 2021-04-16 Хэллибертон Энерджи Сервисиз, Инк. SWELLING PACKERS AND METHODS FOR ACTIVATING SWELLING PACKERS IN A WELL ENVIRONMENT
US10081756B1 (en) 2017-05-17 2018-09-25 Saudi Arabian Oil Company Loss circulation material composition comprising oil-swellable and desolvated polymer gels
US10619432B2 (en) 2017-05-17 2020-04-14 Saudi Arabian Oil Company Oil-swellable, surface-treated elastomeric polymer and methods of using the same for controlling losses of non-aqueous wellbore treatment fluids to the subterranean formation
CA3021379A1 (en) * 2017-10-18 2019-04-18 Kemira Oyj Preformed particle gel for enhanced oil recovery
RU2726696C2 (en) * 2017-12-11 2020-07-15 Федеральное государственное бюджетное учреждение науки Пермского федерального исследовательского центра Уральского отделения Российской академии наук (ПФИЦ УрО РАН) Anti-turbulent additive for drilling muds
US11807700B2 (en) 2020-08-17 2023-11-07 Saudi Arabian Oil Company Electro-responsive hydrogel for reservoir and downhole application
NO20230296A1 (en) * 2020-09-08 2023-03-17 Univ Missouri Fiber assisted re-crosslinkable polymer gel and preformed particle gels for fluid loss and conformance control
CN112266434A (en) * 2020-10-13 2021-01-26 宁波锋成先进能源材料研究院有限公司 Nano cross-linked viscoelastic gel and preparation method and application thereof
US20230407163A1 (en) * 2020-11-04 2023-12-21 The Curators Of The University Of Missouri Nontoxic high temperature resistant hydrogels
US12000278B2 (en) 2021-12-16 2024-06-04 Saudi Arabian Oil Company Determining oil and water production rates in multiple production zones from a single production well

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20030116317A1 (en) * 2000-06-14 2003-06-26 Kin-Tai Chang Composition and method for recovering hydrocarbon fluids from a subterranean reservoir
US6960617B2 (en) * 2002-04-22 2005-11-01 Purdue Research Foundation Hydrogels having enhanced elasticity and mechanical strength properties
US20070204989A1 (en) * 2006-02-28 2007-09-06 Hongxin Tang Preformed particle gel for conformance control in an oil reservoir
US20080075667A1 (en) * 2005-12-16 2008-03-27 Berkland Cory J Nanoparticles, nanocapsules and nanogels

Family Cites Families (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3480546A (en) * 1964-02-28 1969-11-25 Dow Chemical Co Aqueous foam containing a waterswellable polymer flameproofing composition and process of making same
US3251194A (en) * 1964-04-03 1966-05-17 Dow Chemical Co Method of making an ice skating rink
US3749172A (en) * 1972-02-09 1973-07-31 Phillips Petroleum Co Methods of using gelled polymers in the treatment of wells
US3727688A (en) * 1972-02-09 1973-04-17 Phillips Petroleum Co Hydraulic fracturing method
US3798836A (en) * 1972-12-04 1974-03-26 Dow Chemical Co A hydroponic bed for growing plants
US4068714A (en) * 1975-12-24 1978-01-17 Phillips Petroleum Company Method for acidizing subterranean formations
US4683949A (en) * 1985-12-10 1987-08-04 Marathon Oil Company Conformance improvement in a subterranean hydrocarbon-bearing formation using a polymer gel
US4773481A (en) 1987-06-01 1988-09-27 Conoco Inc. Reducing permeability of highly permeable zones in underground formations
US5124188A (en) * 1990-04-02 1992-06-23 The Procter & Gamble Company Porous, absorbent, polymeric macrostructures and methods of making the same
EP0621041B1 (en) * 1993-04-23 2002-09-11 Mitsubishi Chemical Corporation Highly water-absorptive polymers having enhanced gel strength
WO2003082316A1 (en) * 2002-03-29 2003-10-09 The Regents Of The University Of California Microgel particles for the delivery of bioactive materials
US6750261B1 (en) * 2003-04-08 2004-06-15 3M Innovative Properties Company High internal phase emulsion foams containing polyelectrolytes
US8017014B2 (en) 2005-06-01 2011-09-13 Nalco Company Method for improving flux in a membrane bioreactor
US7902127B2 (en) * 2008-04-21 2011-03-08 Nalco Company Composition and method for recovering hydrocarbon fluids from a subterranean reservoir
CA2753520C (en) 2009-03-12 2017-10-24 Conocophillips Company Crosslinked swellable polymer
AR076870A1 (en) 2009-05-15 2011-07-13 Conocophillips Co COMPOSITIONS THAT INCLUDE EXPANDABLE POLYMER PARTICLES AND METHOD TO INCREASE THE RECOVERY OF HYDROCARBON FLUIDS IN A UNDERGROUND FORMATION
CN105384869B (en) 2009-06-10 2018-12-14 科诺科菲利浦公司 Polymers capable of swelling with anionic site
US8691736B2 (en) 2009-06-15 2014-04-08 Conocophillips Company Swellable polymer with cationic sites
WO2014113112A1 (en) * 2013-01-15 2014-07-24 Conocophillips Company Fluorescent tags for detection of swellable polymers

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20030116317A1 (en) * 2000-06-14 2003-06-26 Kin-Tai Chang Composition and method for recovering hydrocarbon fluids from a subterranean reservoir
US20030149212A1 (en) * 2000-06-14 2003-08-07 Kin-Tai Chang Composition for recovering hydrocarbon fluids from a subterranean reservoir
US6960617B2 (en) * 2002-04-22 2005-11-01 Purdue Research Foundation Hydrogels having enhanced elasticity and mechanical strength properties
US20080075667A1 (en) * 2005-12-16 2008-03-27 Berkland Cory J Nanoparticles, nanocapsules and nanogels
US20070204989A1 (en) * 2006-02-28 2007-09-06 Hongxin Tang Preformed particle gel for conformance control in an oil reservoir

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9267075B2 (en) 2009-06-10 2016-02-23 Conocophillips Company Swellable polymer with anionic sites
WO2016084032A1 (en) * 2014-11-28 2016-06-02 Ecopetrol S.A. Formulations of colloidal dispersion gels and surfactants for the improved recovery of petroleum and method of obtaining these formulations
WO2017210486A1 (en) * 2016-06-02 2017-12-07 The Curators Of The University Of Missouri Re-assembling polymer particle package for conformance control and fluid loss control
RU2744247C2 (en) * 2016-06-02 2021-03-04 Зэ Кьюрейтерс Оф Зэ Юниверсити Оф Миссури Package of repeatable cross-linked polymeric particles for configuration and liquid loss control
US11162016B2 (en) 2016-06-02 2021-11-02 The Curators Of The University Of Missouri Re-assembling polymer particle package for conformance control and fluid loss control
US11268009B2 (en) 2016-06-02 2022-03-08 The Curators Of The University Of Missouri Fiber assisted re-crosslinkable polymer gel and preformed particle gels for fluid loss and conformance control
US11549048B2 (en) 2016-06-02 2023-01-10 The Curators Of The University Of Missouri Re-assembling polymer particle package for conformance control and fluid loss control
US11214729B2 (en) 2018-08-31 2022-01-04 The Curators Of The University Of Missouri Re-crosslinking particle gel for CO2 conformance control and CO2 leakage blocking
EP3856864A4 (en) * 2018-10-31 2022-07-06 Kemira Oyj Methods and compositions for enhanced oil recovery
US11840664B2 (en) 2018-10-31 2023-12-12 Kemira Oyj Methods and compositions for enhanced oil recovery
CN114478897A (en) * 2021-11-24 2022-05-13 四川轻化工大学 Slow-swelling pre-crosslinked gel particles and preparation method thereof
CN114478897B (en) * 2021-11-24 2024-02-23 四川轻化工大学 Slow-expansion type pre-crosslinked gel particles and preparation method thereof

Also Published As

Publication number Publication date
US20140131043A1 (en) 2014-05-15
CA2761528A1 (en) 2010-12-16
CN105384869B (en) 2018-12-14
MX347441B (en) 2017-04-25
CN102459364A (en) 2012-05-16
AU2010258802B2 (en) 2013-09-12
MY152086A (en) 2014-08-15
RU2540068C2 (en) 2015-01-27
AU2010258802A1 (en) 2012-01-19
GB2482835B (en) 2013-05-15
GB2482835A (en) 2012-02-15
US20100314114A1 (en) 2010-12-16
GB2482835A8 (en) 2013-09-25
CA2761528C (en) 2017-06-06
CN105384869A (en) 2016-03-09
US8669214B2 (en) 2014-03-11
GB201120813D0 (en) 2012-01-11
MX2011013343A (en) 2012-04-30
US9267075B2 (en) 2016-02-23
GB2482835B8 (en) 2013-09-25

Similar Documents

Publication Publication Date Title
US9267075B2 (en) Swellable polymer with anionic sites
US11814578B2 (en) Delayed gelling agents
US9139762B2 (en) Swellable polymer with cationic sites
CA2753522C (en) Swellable polymers with hydrophobic groups
CA2753520C (en) Crosslinked swellable polymer
AU2013347850B2 (en) Crosslinking of swellable polymer with PEI

Legal Events

Date Code Title Description
WWE Wipo information: entry into national phase

Ref document number: 201080025522.7

Country of ref document: CN

121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 10786790

Country of ref document: EP

Kind code of ref document: A1

WWE Wipo information: entry into national phase

Ref document number: 2761528

Country of ref document: CA

ENP Entry into the national phase

Ref document number: 1120813

Country of ref document: GB

Kind code of ref document: A

Free format text: PCT FILING DATE = 20100609

WWE Wipo information: entry into national phase

Ref document number: 1120813.9

Country of ref document: GB

WWE Wipo information: entry into national phase

Ref document number: MX/A/2011/013343

Country of ref document: MX

NENP Non-entry into the national phase

Ref country code: DE

WWE Wipo information: entry into national phase

Ref document number: 2010258802

Country of ref document: AU

WWE Wipo information: entry into national phase

Ref document number: 2011153041

Country of ref document: RU

ENP Entry into the national phase

Ref document number: 2010258802

Country of ref document: AU

Date of ref document: 20100609

Kind code of ref document: A

122 Ep: pct application non-entry in european phase

Ref document number: 10786790

Country of ref document: EP

Kind code of ref document: A1