WO1982001007A1 - Stimulation and cleanup of oil-and/or gas-producing wells - Google Patents

Stimulation and cleanup of oil-and/or gas-producing wells Download PDF

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Publication number
WO1982001007A1
WO1982001007A1 PCT/US1981/000930 US8100930W WO8201007A1 WO 1982001007 A1 WO1982001007 A1 WO 1982001007A1 US 8100930 W US8100930 W US 8100930W WO 8201007 A1 WO8201007 A1 WO 8201007A1
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Prior art keywords
oligomer
methanol
foam
oligomers
weight
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French (fr)
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Mining & Mfg Co Minnesota
H Clark
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3M Co
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Minnesota Mining and Manufacturing Co
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Priority to DE8181902125T priority Critical patent/DE3173559D1/de
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    • 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
    • C08F220/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/02Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/04Acids; 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
    • C08F220/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/02Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/10Esters
    • C08F220/22Esters containing halogen
    • C08F220/24Esters containing halogen containing perhaloalkyl radicals
    • 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
    • C09K8/60Compositions for stimulating production by acting on the underground formation
    • C09K8/62Compositions for forming crevices or fractures
    • C09K8/70Compositions for forming crevices or fractures characterised by their form or by the form of their components, e.g. foams
    • C09K8/703Foams
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S507/00Earth boring, well treating, and oil field chemistry
    • Y10S507/922Fracture fluid
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S507/00Earth boring, well treating, and oil field chemistry
    • Y10S507/933Acidizing or formation destroying

Definitions

  • This invention relates to a method for treating oil- and/or gas-producing wells using foamable fluids containing methanol.
  • this invention relates to foamable methanol compositions.
  • this invention relates to certain novel fluorochemicals useful for foaming methanol.
  • Such well stimulation fluids generally operate by hydraulic fracturing of and/or acidic reaction with the formation, increasing the permeability of the formation by oil or gas and the rate of delivery of oil. or gas to the well-head.
  • Hydraulic fracturing has long been practiced in the art using fluids such as native crude oil, lease crude oil, diesel fuel, kerosene, and water, with or without propping agents, such as sand, suspended therein (see, e.g., U.S. Patent Nos. 3,070,165 and 3,089,846).
  • Acidic treatment of a formation is also well-known in the art and is. generally carried out using mineral acids such as HC1 (in limestone formations) and HP (in sandstone formations), see, e.g., Williams, Gidley, and Schechter, Acidizing Fundamentals, SPE (1979), esp. pp. 1-18 and 29-37. It is also common practice to inject well cleanup fluids into oil- and gas-producing wells in order to increase the productivity of such wells. Such cleanup fluids generally remove scale and/or other foreign matter from the well bore.
  • well cleanup fluids are well-known in the art, and are described in, e.g., Williams, Gidley, and Schechter, id., and in Allen and Roberts , Production Operations , Oil and Gas Consultants Intl. Inc . ( 1978 ) , see esp . Vol. II , pages 118 and 171-180.
  • well stimula tion and well cleanup fluids will sometimes be referred to hereafter as "well treatment fluids" .
  • Some oil- and gas-bearing, formations respond especially well to well treatment fluids containing methanol or aqueous methanol mixtures , particularly if such formations contain water-sensitive materials such as water-swellable clays. Such water-sensitive materials tend to interact with water present in the surrounding formation, and can swell and/or migrate within the formation , thereby reducing the permeability of the oil- or gas-bearing formation and diminishing the productivity thereof .
  • Foamable, methanol-containing well treatment fluids currently used in the field are generally made foamable by adding thereto water and conventional hydrocarbon-based surface-active agents, such as sulfated polyethoxylated alcohols. It would be desirable to eliminate some or all of such water in well treatment fluids used in water-sensitive formations.
  • Certain substantially water-free methanol- containing foamable well stimulation fluids, containing fluorochemical-based surface-active agents, are described in Clark, Pike, and Rengel, "The Use of Fluorochemical
  • Clark, Pike, and Rengel paper No. SPE 7894 contains a disclosure of a substantially water-free methanol-containing well stimulation fluid, a fluid rendered foamable by use of a fluorochemical surface-active agent identified therein as "FC-B".
  • FC-B is a fluoroaliphatic radical-containing surface-active agent having ester linkages and polyoxyalkylene solubilizing moieties. Foam-forming capabilities of a well treatment fluid can be demonstrated using a foam generator described in the Clark, Pike, and Rengel paper No. SPE 7894.
  • Foam quality represents the percentage of a foamed fluid which is occupied by trapped gas, with higher foam quality numbers representing more desirable foams.
  • Foam quality is commonly denoted using the Greek symbol gamma (r).
  • Foam half-life represents the time period in seconds required for one half of the liquid present in the foam to drain as a separate liquid phase , and is generally denoted by the symbol t 1 / 2 .
  • Reagent grade methanol containing 1% of the above-described fluorine-containing oligomer was shown in the Clark , Pike , and Rengel paper No . SPE 7894 to have a foam quality of 60 and a foam half-life of 25 seconds .
  • the present invention provides , in one aspect, a method for treating an oil- and/or gas-bearing formation by injecting therein a methanol-containing well treatment fluid containing an amount, sufficient to make said fluid foamable, of oligomer as methanol foaming agent, characterized in that said oligomer has:
  • Rf is a monovalent, fluorinated (preferably perfluorinated) aliphatic radical terminating in at least one perfluororaethyl group (e.g., C 6 F 13 -), and having 5 to 14 or more carbon atoms, and Q is a linkage or bridge, generally divalent (e.g.,
  • Q' is a linkage or bridge, generally divalent (e.g., -C 2 H 4 -) through which A is attached to said backbone, greater than 10% by weight AQ' moieties are present in said oligomer, and AQ' is a radical which, when the valence bonds of AQ' are satisfied by hydrogen atoms, has a solubility in methanol at 25°C of at least 20% by weight; said oligomer containing between 10 and 50% by weight fluorine, and said fluid having at 25°C a foam quality of at least 60 and a foam half-life of at least 50 seconds.
  • the present invention also provides foamable fluid compositions useful for well treatment.
  • the present invention provides novel fluoropolymers for use in foaming methanol or me thanol-containing solutions, characterized in that said fluoropolymers have three or more first units of the formula :
  • Rf is a monovalent, fluorinated aliphatic radical terminating in at least one perfluoromethyl group and having 5 to 14 or more carbon atoms;
  • Q is a linkage or bridge through which Rf is attached to said first unit;
  • Q' is a linkage or bridge through which A is attached to said second unit;
  • R 2 is H, CH 3 , or Cl
  • A contains at least one carboxyl group; greater than 10% by weight AQ' moieties are present in said oligomer; and each of said first and second units is the same as or different from other of said first and second units in said oligomer; said oligomer containing between 10 and 50% by weight fluorine.
  • the oligomeric backbone is generally composed of repeating units to which the R f Q and AQ' moieties are attached. Such repeating units can be carbon-carbon chains, such as polyvalent aliphatic, e.g., -CH 2 CH 2 - and -CH 2 CH(CH 2 -) 2 , polyvalent aromatic, e.g., , and linking groups which can connect such chains together, such-as.
  • the backbone for a specific oligomer useful in this invention will be dependent upon the ease of preparation of such an oligomer and the availability of necessary precursors thereof .
  • the backbone is a repeating unit having a carbon-carbon chain and results from free-radical initiated solution or emulsion polymerization of one or more fluoroaliphatic radical-containing acrylate monomers and one or more ethylenically unsaturated polar comonomers such as. substituted or unsubstituted acrylic or methacrylic acid.
  • fluoroaliphatic radical-containing oligomeric composition can result in other backbone structures, and are described in greater detail below.
  • the oligomers used in this invention are generally low molecular weight polymers (i.e., they have a number average molecular weight below about 100,000). Such oligomers are generally mixtures rather than pure compounds. As used herein, the word "oligomer” includes such mixtures.
  • the oligomers of this invention can be copolymers of 2, 3, 4 or more monomers, and can contain pendant moieties other than the R f Q- and AQ'- moieties mentioned above, as long as the utility of such oligomers as methanol foamers is not unduly diminished by the presence of such other pendant moieties in the oligomer. Also, the oligomers of this invention can be random or segmented copolymers.
  • Rf is a monovalent, fluorinated aliphatic, preferably saturated, organic radical having an average at least 5 carbon atoms.
  • the skeletal chain of Rf can be straight, branched, or, if sufficiently large, cyclic, and can include divalent oxygen atoms or trivalent nitrogen atoms bonded only to carbon atoms.
  • Rf is fully fluorinated, but hydrogen or chlorine atoms can be present as substituents on the skeletal chain, provided that not more than one atom of either hydrogen or chlorine is present for every two carbon atoms in the skeletal chain, and R f contains at least a terminal perfluoromethyl group.
  • Rf has about 6 to 10 carbon atoms.
  • the fluoroaliphatic radical-containing oligomers of this invention can contain R f radicals which are the same as, or different from, one another.
  • the function of the linkage or bridge Q is to bond the fluoroaliphatic radicals, R f , to the oligomer backbone.
  • Q is generally divalent, although it can be polyvalent (e.g., trivalent).
  • Q can be a valence bond, in which case a fluoroaliphatic radical is bonded or linked directly to the oligomer backbone.
  • Q can also be one or more linking groups such as polyvalent aliphatic, e.g., -CH 2 CH 2 - and -CH 2 CH(CH 2 -) 2 , polyvalent aromatic, oxy, thio, carbonyl, sulfone, sulfoxy, imino, e.g., -NH- and -N(C 2 H 5 )-, and combinations thereof, such as oxyalkylene, iminoalkylene, iminoarylene, sulfonamido, carbonamido, sulfonamidoalkylene, carbonamido-alkylene, urethane, e.g., -CH 2 CH 2 OCONH- and urea, e.g., -NHCONH-.
  • the linkage Q for a specific oligomer of this invention will be dependent, upon the ease of preparation of such oligomer and the availability of necessary precursors, thereof.
  • This linkage can have a wide variety of structures.
  • large Q is, the fluorine content (the locus of which is R f ) of the oligomeric composition is within the aforementioned, limits set forth in the above description.
  • the fluorine-content limits described above have an important effect upon the foam stability of methanol-containing. fluids of this invention. If a series of oligomers having different levels of fluorine content are prepared from monomers containing R f Q moieties and AQ' moieties, foam quality and foam half-life of solutions of such oligomers in methanol first increase and then decrease as fluorine content goes from 0 to more than 50 wt. %. Foam quality above about 60 and foam half-life above about 50 seconds at a. 1 wt. % concentration of oligomer in methanol are generally obtained at a fluorine content between about 10 and 50 weight percent.
  • Foam quality and foam half-life can sometimes change drastically with very slight changes in fluorine content, so empirical testing of oligomers containing low (viz., about 10 wt. %) or high (viz. about 50 weight %) amounts of fluorine is sometimes necessary to. determine if methanol solutions of such oligomers will provide adequate foam quality and foam half-life. If foam, quality and foam half-life for such oligomers (viz., those oligomers containing low or high amounts of fluorine) is desired to be increased, then fluorine content should be adjusted
  • the concentration of the oligomer in methanol should be increased.
  • the Q linkages can be the same as or different from one another.
  • the R f Q moieties can be the same as or different from one another.
  • the A group is a polar methanol-solubilizing group, preferably having hydroxyl or carboxyl functionality.
  • the A group can also have structures such as amido, amino, imino, sulfo (i.e., HO 3 S-), and phosphono (i.e., (HO) 2 OP-).
  • A is preferably monovalent.
  • Fluoroaliphatic radical-containing oligomers. of this invention can contain A groups which are the same as, or different from, one another.
  • the function of the linkage or bridge Q' is to bond the polar methanol-solubilizing groups.
  • A to the oligomer backbone.
  • Q' is generally divalent, although it can be polyvalent (e.g., trivalent).
  • Q' can be a valence bond, in hich case an A group is bonded or linked directly to the backbone.
  • Q' can also be one or more linking groups such as polyvalent aliphatic, e.g.,
  • polyvalent aromatic e.g. oxy, thio, carbonyl, sulfone, sulfoxy, imino, e.g., -NH- and -N(C 2 H 5 )-, and combinations thereof, such as oxyalkylene, iminoalkylene, iminoarylene, sulfonamido, carbonamido, sulfonamidoalky lene, carbonamidoalkylene, urethane, e.g., -CH 2 CH 2 OCONH- and urea, e.g., -NHCONH-.
  • the linkage Q' for a specific oligomer of this invention will be dependent upon the ease of preparation of such oligomer and the availability of necessary precursors thereof.
  • the A group and Q' linkage form a radical (referred to herein as AQ' ) which, when the valence bonds of said radical are satisfied by hydrogen atoms, has a solubility in methanol at 25°C of at least about 20% by weight.
  • AQ' a radical which, when the valence bonds of said radical are satisfied by hydrogen atoms, has a solubility in methanol at 25°C of at least about 20% by weight.
  • the A group is -OH
  • the Q' linkage is -C(O)OC 2 H 4 -
  • the AQ' radical is .C(O)OC 2 H 4 OH.
  • the resulting compound is HC(O)OC 2 K 4 OH, or hydroxyethyl formate.
  • the solubility of hydroxyethyl formate in methanol at 25°C is greater than 20% by weight.
  • Other AQ' radicals can be similarly evaluated to determine if they meet the above-described methanol solubility criterion.
  • the AQ' radicals can be the same as, or different from, one another.
  • the AQ' radicals can contain polar groups such as oxyalkylene linkages, poly(oxyalkylene) linkages, or ester linkages, but where such linkages are present, such radicals must also contain a polar methanol-solubilizing group A as described above, and such radicals must meet the above-described methanol solubility criterion.
  • the fluorine content of the fluorinated oligomers of this invention is located primarily within R f although small amounts of fluorine can be present in A, Q', or in the oligomeric backbone.
  • Fluoroaliphatic radical-containing oligomers used in the method of this invention and contained in the well treatment fluids of this invention are known in the art, see U.S. Patent Nos. 3,318,852, 3,431,497, 3,470,124, 3,574,791, 3,920,614 and 4,147,851, while others are novel per se and their preparation is described hereinafter.
  • Fluoroaliphatic radical-containing oligomers within the scope of this invention can be prepared from free-radically polymerizable monomers containing the R f Q moeities and comonomers containing the AQ' moieties.
  • Such fluoroaliphatic radical-containing oligomers are generally prepared using emulsion, bulk, or solution polymerization techniques well known to those skilled in the art.
  • solvents which can be used as media in solution polymerizations are tetrahydrofuran, ethyl acetate, butyl acetate, methyl ethyl ketone, methyl isobutyl ketone, methanol, ethanol, isopropyl alcohol, isobutyl alcohol, ethyleneglycol monoethyl ether, diethyleneglycol monoethyl ether, acetone, trichiorofluoromethane, 1, 1-2-trichloro- 1, 2, 2-trifluoroe thane, toluene, benzotrifluoride, xylene hexafluoride, 1, 1, 1-trichloroethane, and combinations thereof.
  • Tetrahydrofuran and mixtures of ethanol and ethyl acetate are preferred solvents for such polymerizations.
  • the preferred method for preparing such oligomers is by solution or emulsion polymerization of one or more fluoroaliphatic acrylate or methacrylate monomers with one or more ethylenically unsaturated polar comonomers.
  • Such ethylenically unsaturated polar comonomers have the general formula AQ'R', where A and Q' are as described above and R' contains a carbon-carbon double bond.
  • fluoroaliphatic acrylate and methacrylate monomers useful in such preparation include:
  • Representative ethylenically unsaturated polar comonomers useful in such preparation include:
  • CH 2 CHSO 3 H
  • CH 2 CHCH 2 SO 3 H
  • CH 2 CHOCH 2 CH(OH)CH 2 OH
  • CH 2 CHCONHCH 2 CH 2 CH 2 N(CH 3 ) 2 ,
  • fluoroaliphatic radical-containing oligomers useful in this invention can be prepared by solution or emulsion polymerization of one or more fluoroaliphatic vinyl monomers such as perfluoro-alkylacrylamides, perfluoroalkylthioacrylates, perfluoroalkylethylenes, vinyl and allyl esters of perfluoroalkanoic acids, perfluoroalkyl vinyl ethers, etc., with one or more ethylenically unsaturated polar comonomers such as those listed above.
  • fluoroaliphatic vinyl monomers such as perfluoro-alkylacrylamides, perfluoroalkylthioacrylates, perfluoroalkylethylenes, vinyl and allyl esters of perfluoroalkanoic acids, perfluoroalkyl vinyl ethers, etc.
  • fluoroaliphatic vinyl monomers useful in such preparations include:
  • the fluoroaliphatic radical-containing oligomers useful in this invention can also contain, other pendant groups which do not interfere with the function of such oligomers as methanol foamers.
  • Such pendant groups can be part of the oligomer component, corresponding to one or more copolymerizable ethylenically unsaturated monomers, e.g., ethylene, vinyl acetate, vinyl chloride, vinyl fluoride, vinylidene chloride, vinylidene fluoride, vinyl chloroacetate, acrylonitrile, vinylidene cyanide, styrene, alkylated styrenes, halogenated styrenes, alkyl and epoxyalkyl esters of acrylic acid, methacrylic acid and -chloroacrylic acid, methacrylonitrile, vinylcarbazole, vinyl pyridine, vinyl alkyl ethers, vinylalkyl ke tones, butadiene, chloroprene, fluoroprene,
  • a free-radical initiator is generally employed.
  • free-radical initiators include benzoyl peroxide, azobisisobutyronitrile, di(t-butyl) peroxide, cumene hydroperoxide, hydrogen peroxide, and trioctyl- methylammonium persulfate.
  • free-radical initiator can be used for such preparation.
  • a chain transfer agent can also be employed in the preparation of such oligomers.
  • chain transfer agents are well known in the art, and include n-octyl mercaptan, mercaptoacetic acid, and p- toluenethiol.
  • a preferred chain transfer agent is. n-octyl mercaptan.
  • chain transfer agent can be used, with larger amounts of chain transfer agent resulting in an oligomeric product having lower molecular weight.
  • the fluoroaliphatic radical-containing oligomers used in this invention are prepared using a chain transfer agent, in an amount of about 0.2 to 2 weight % chain transfer agent.
  • Solution polymerization of the fluoroaliphatic radical-containing oligomers used in this invention is carried, out by known procedures in a reaction vessel such as a stirred flask or a sealed vessel having external means for heating or cooling the reaction vessel.
  • the reaction temperature is generally between about 40 and 90oC, preferably between 55 and 70°C, and the reaction is generally maintained for a time period of about 6 to 24 hours.
  • the temperature and time required for essentially complete polymerization will depend on the reactivities, of the precursor monomers, the type and concentration of catalyst, nature of the solvent, etc.
  • reactions of acrylate monomers using 0.7 weight % of azobisiso- butyronitrile catalyst and ethyl acetate solvent, and carried out with agitation in a sealed glass reactor, are usually run for about 16 hours at about 60°C.
  • the fluoroaliphatic radical-containing oligomers of this invention can also be prepared by other conventional methods.
  • polymers such as polyacrylic acid and carboxymethylcellulose, which have pendant carboxyl groups (i.e., AQ' moieties), can be partially esterified with a fluoroaliphatic alcohol to introduce pendant fluoroaliphatic ester groups (i.e., R f Q moieties) thus yielding oligomers having both R f Q and AQ' moieties along the polymer chain.
  • AQ' moieties pendant carboxyl groups
  • R f Q moieties pendant fluoroaliphatic ester groups
  • oligomers useful in this invention can be prepared by the addition of fluoroaliphatic thiols or perfluoroalkyl iodides across some of the remaining double bonds in partially sulfonated butadiene-styrene copolymers, or butadiene-hydroxyethyl acrylate copolymers.
  • perfluoroaliphatic radicals and chlorine atoms can be added across some of. such remaining double bonds by the free-radically catalyzed reaction of such copolymers with perfluoroaikanesulfonyl chlorides.
  • oligomers can be prepared by the reaction of fluoroaliphatic alcohol or amine compounds with maleic anhydride copolymers, (e.g., ethylene-maleic anhydride copolyraer), to cause opening of the cyclic anhydride functional group resulting in the formation of pendant carboxyl groups and pendant fluoroaliphatic ester or amide groups.
  • a preferred class of well treatment fluid compositions of this invention contain methanol together with an amount, sufficient to make said fluid foamable, of oligomer as methanol foaming agent, said oligomer comprising three or more units of the formula:
  • Rf, Q, and Q' are as defined above;
  • R 1 is a or CH 3 ;
  • R 2 is H, CH 3 , or Cl;
  • A contains at least one carboxyl group; greater than about 10% by weight AQ' moieties are present in said oligomer; and each of said units is the same as or different from other of said units in said oligomer; said oligomer containing between about 10 and about 50% by weight fluorine, and said fluid having at 25°C a foam quality of at. least about 60 and a foam half-life of at least about 50 seconds.
  • Such oligomers can contain other repeating units and pendant groups which do not interfere with the function of the oligomer as a methanol foamer. Also, such oligomers can be random or segmented polymers.
  • Such oligomers can be prepared from free-radically initiated, polymerization of one or more fluoroaliphatic radical-substituted acrylate or methacrylate monomers with one or more carboxyl-containing ethylenically unsaturated comonomers.
  • Suitable fluoroaliphatic radical-substituted acrylate or methacrylate monomers include the representative fluoroaliphatic acrylates and methacrylates listed above.
  • Suitable carboxyl-containing ethylenically unsaturated comonomers include:
  • Acrylic acid is a preferred carboxyl-containing ethylenically unsaturated comonomer.
  • a novel class of fluoroaliphatic radical- containing oligomers useful as methanol foamers are oligomers consisting essentially of three or more units of the formula:
  • R f , Q, Q' , and R 2 are as defined above ;
  • A contains at least one carboxyl group ; greater than about 10% by weight AQ ' moieties are present in said oligomer ; and each of said units is the same as or different from other of said units in said oligomer; said oligomer containing between about 10 and about 50% b y weight fluorine .
  • Such oligomers can be random or seg mented. copolymers .
  • Such novel oligomers can be prepared from free-rad ically initiated polymerization of one or more fluoroaliphatic radical-subs tituted acrylate monomers with one or more carboxyl-containing ethylenically unsaturated comonomers .
  • Suitable carboxyl-containing ethylenically unsaturated comonomers include those shown above.
  • Such preferred members can also be prepared using addi tional , optional copolymerizable comonomers such as ethyl acrylate .
  • Foamable refers to the ability of such methanol solutions and methanol-containing fluids to be aerated, ag itated , or otherwise combined, with a gas to form a froth or foam.
  • the composition When a well treatment fluid composition of the present invention is prepared , the composition generally contains between about 0.02 and 2 weight % (based on the total weight of liquid components in such composition ) fluoroaliphatic radical-containing oligomer, preferably about 1% or less fluorinated oligomer.
  • fluoroaliphatic radical-containing oligomer preferably about 1% or less fluorinated oligomer.
  • Some of the oligomers used in this invention yield cloudy methanol solutions at such concentrations. Although such cloudiness is not believed to affect the utility of such oligomers as methanol foamers , some practitioners of this invention may prefer to use clear ( i . e . , transparent, with the clarity of water) methanol-containing well treatment fluids . Such clear fluids can sometimes be obtained by altering the oligomer polymerization conditions. Both clear and cloudy methanol-containing fluids are shown below in the Examples .
  • the amount of oligomer should be suf ficient to give a foam quality of at least about 60 and a foam halflife of at least about 50 seconds .
  • foam quality and foam half-life are measured using the foam generator test, described in the aforementioned Clark, Pike, and Rengel paper No. SPE 7894.
  • the well treatment fluids of this invention contain methanol, and can also contain water and any desired well treatment adjuvants.
  • Such adjuvants can include mineral acids (e.g., HCl and HF), organic acids (e.g., CH 3 COOH and HCOOH), clay swelling inhibitors (e.g., KC1), clay stabilizers (e.g., hydroxy alumina), iron chelating agents (e.g., citric acid), anti-emulsifying agents, gelling agents, friction reducers, corrosion inhibitors, or fluid loss additives.
  • clay swelling inhibitors e.g., KC1
  • clay stabilizers e.g., hydroxy alumina
  • iron chelating agents e.g., citric acid
  • anti-emulsifying agents gelling agents
  • friction reducers corrosion inhibitors
  • corrosion inhibitors or fluid loss additives.
  • proppants such as graded sand (e.g., Ottawa sand) river sand, glass, beads, aluminum pellets, or walnut shells.
  • the ratio of methanol and water (if any water is used) and the type and amount of adjuvants and propping agents used in the well treatment fluids of this invention can vary greatly and will depend upon the characteristics of the formation to be treated, the production and treatment history of the well to be treated, and other variables well known to those skilled in the art.
  • the resulting oligomeric product ( in tetrahydrofuran solution) was added to reagent grade methanol to form a 1% by weight solution of oligomer in methanol.
  • a 150 ml quantity of the oligomer/methanol solution was then placed in the pressure vessel of a foam generator described in the above-mentioned Clark, Pike, and Rengel paper No. SPE 7894.
  • the pressure vessel was 150 cm 3 stainless, steel gas. sampling cylinder (part no. 304-HDF4-150, commercially available from the Whitey Company), fitted with valves at each end.
  • the inlet end of the pressure vessel was supplied with nitrogen at one MPa pressure.
  • the outlet end of the presure vessel led a foam generator head having a 1.58 mm diameter chamber, 0.79 mm diameter x 1.27 mm long constriction, and a 1.78 mm diameter outlet chamber.
  • Four 0.79 mm diameter radial Venturis allowed atmospheric air to enter the outlet chamber about 1.3 mm downstream from the outlet end of the constriction.
  • the outlet end of the foam generator head was connected to a 150 mm x 64 mm O.D. copper delivery tube terminated with a 50 mm long x 5 mm I.D. glass tube.
  • the glass tube contained a rolled 30 mm x 30 mm section of 60 mesh stainless, steel wire gauze.
  • the foam quality was 69 and the foam half-life was 170 seconds.
  • Examples 2-17 Several fluoroaliphatic radical-containing oligomers were prepared and tested as in Example 1.
  • the oligomers of Examples 6 and 14 were prepared in a three-necked flask and stirred under nitrogen gas at 60- 70oC for about 20 hours .
  • Some of the oligomers shown below (e .g . , Examples 4 and 17) formed cloudy solutions in methanol while others (e .g. , Example 5 ) formed a clear solution .
  • a clear solution of an oligomer similar to the oligomer of Example 4 was obtained by altering the oligomer polymerization conditions as follows .
  • An oligomer was prepared using 28. 8 g
  • the initiator for the polymerization was 0.24 g azobisisobutyronitrile
  • the chain transfer agent was 0.18 n-octyl mercaptan
  • the solvent was a mixture of 30 g isopropyl alcohol and 30 g of methyl isobutyl ketone.
  • the resulting oligomer was added to methanol to form a 1 wt . % solution, and. tested as. in Example 1.
  • the solution had a foam quality of 61 and a foam half-life of 85.
  • Example 19 In a series of seven runs, the effect of adding various ad j uvants to the oligomer/methanol solution of Example 1 was evaluated . The results are set forth below in Table II.
  • Example 20 In a series of nine runs, the effect upon foam q uali ty and foam half-life of various oligomer concentrations was evaluated.
  • the oligomer/methanol solutions of runs 1-4 contained the oligomer of Example 1 in methanol .
  • the oligomer/methanol solutions of runs 5-9 contained the oligomer of Example 4.
  • the foam quality and foam half-life of the resulting compos itions are set forth below in Table III.
  • Example 1 In a series of 2 runs, the effect of combining the oligomer/methanol solution of Example 1 with a propping agent was evaluated.
  • a first (control) run 0.25 g of the oligomer of Example 1 and 25 g of methanol were combined and shaken vigorously for 5 seconds in a 60 ml "French square" glass bottle. The shaken solution was allowed to stand for 10 seconds, then the foam height above the solution was measured. The foam height was about 33 mm.
  • Example 1 Comparative Example In a. series of 7 runs, several compositions outside the scope of this invention were prepared and evaluated as in Example 1.
  • the oligomers of runs 6 and 7 were prepared in a three-necked flask and stirred under nitrogen gas at 60-70oC for about.20 hours.
  • the foam quality and foam half-life of the resulting compositions are set forth below in Table IV.
  • An oligomer prepared from the same monomers but containing about 46 wt.% fluorine had a foam quality of 60 and a foam half-life of 155 at a 1 wt.% concentration in methanol.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
  • Detergent Compositions (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
PCT/US1981/000930 1980-09-15 1981-07-10 Stimulation and cleanup of oil-and/or gas-producing wells Ceased WO1982001007A1 (en)

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US4840989A (en) * 1987-01-20 1989-06-20 Bayer Aktiengesellschaft Copolymer made from n-vinylamides and perfluoroalkyl group-containing, ethylenically unsaturated compounds, a process for their preparation, and their use
US4964329A (en) * 1986-11-21 1990-10-23 Broken Hill Proprietary Co., Ltd. Sound attenuation with foam
US5612431A (en) * 1994-09-21 1997-03-18 Minnesota Mining And Manufacturing Company Leaching of precious metal ore with fluoroaliphatic surfactant
US6355753B1 (en) 1997-05-20 2002-03-12 Daikin Industries Ltd. Polymer and antifouling agent composition containing the same
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US4609477A (en) * 1985-02-05 1986-09-02 Basf Corporation Liquid foaming additives used in the stimulation of oil and gas wells
US4964329A (en) * 1986-11-21 1990-10-23 Broken Hill Proprietary Co., Ltd. Sound attenuation with foam
GB2199869B (en) * 1986-11-21 1991-02-27 Broken Hill Pty Co Ltd Sound attenuation with foam
US4840989A (en) * 1987-01-20 1989-06-20 Bayer Aktiengesellschaft Copolymer made from n-vinylamides and perfluoroalkyl group-containing, ethylenically unsaturated compounds, a process for their preparation, and their use
US5612431A (en) * 1994-09-21 1997-03-18 Minnesota Mining And Manufacturing Company Leaching of precious metal ore with fluoroaliphatic surfactant
US5827348A (en) * 1994-09-21 1998-10-27 Minnesota Mining And Manufacturing Company Leaching of precious metal ore with fluoroaliphatic surfactant
US6355753B1 (en) 1997-05-20 2002-03-12 Daikin Industries Ltd. Polymer and antifouling agent composition containing the same
CN102365340A (zh) * 2009-03-25 2012-02-29 大金工业株式会社 包含含氟聚合物的表面活性剂
EP2412779A4 (en) * 2009-03-25 2014-01-15 Daikin Ind Ltd TENSID WITH A FLUOROUS POLYMER

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IT8149289A1 (it) 1983-03-14
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IT8149289A0 (it) 1981-09-14
CA1178194A (en) 1984-11-20
IT1171528B (it) 1987-06-10
EP0060843A1 (en) 1982-09-29
EP0060843A4 (en) 1983-02-04
US4557837A (en) 1985-12-10

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