WO2006111712A2 - Ionic liquids and uses thereof - Google Patents

Ionic liquids and uses thereof Download PDF

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WO2006111712A2
WO2006111712A2 PCT/GB2006/001359 GB2006001359W WO2006111712A2 WO 2006111712 A2 WO2006111712 A2 WO 2006111712A2 GB 2006001359 W GB2006001359 W GB 2006001359W WO 2006111712 A2 WO2006111712 A2 WO 2006111712A2
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general formula
group
alkyl group
alkyl
salt
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PCT/GB2006/001359
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WO2006111712A3 (en
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Ian Ralph Collins
Martyn John Earle
Simon Peter Exton
Natalia Vladimirovna Plechkova
Kenneth Richard Seddon
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The Queen's University Of Belfast
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Priority claimed from GB0507987A external-priority patent/GB0507987D0/en
Priority claimed from GB0512824A external-priority patent/GB0512824D0/en
Application filed by The Queen's University Of Belfast filed Critical The Queen's University Of Belfast
Publication of WO2006111712A2 publication Critical patent/WO2006111712A2/en
Publication of WO2006111712A3 publication Critical patent/WO2006111712A3/en

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    • 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
    • C09K8/584Compositions 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 surfactants
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D213/00Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members
    • C07D213/02Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D233/00Heterocyclic compounds containing 1,3-diazole or hydrogenated 1,3-diazole rings, not condensed with other rings
    • C07D233/54Heterocyclic compounds containing 1,3-diazole or hydrogenated 1,3-diazole rings, not condensed with other rings having two double bonds between ring members or between ring members and non-ring members
    • C07D233/56Heterocyclic compounds containing 1,3-diazole or hydrogenated 1,3-diazole rings, not condensed with other rings having two double bonds between ring members or between ring members and non-ring members with only hydrogen atoms or radicals containing only hydrogen and carbon atoms, attached to ring carbon atoms
    • C07D233/58Heterocyclic compounds containing 1,3-diazole or hydrogenated 1,3-diazole rings, not condensed with other rings having two double bonds between ring members or between ring members and non-ring members with only hydrogen atoms or radicals containing only hydrogen and carbon atoms, attached to ring carbon atoms with only hydrogen atoms or radicals containing only hydrogen and carbon atoms, attached to ring nitrogen atoms
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02Phosphorus compounds
    • C07F9/28Phosphorus compounds with one or more P—C bonds
    • C07F9/54Quaternary phosphonium compounds
    • C07F9/5407Acyclic saturated phosphonium compounds
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02Phosphorus compounds
    • C07F9/28Phosphorus compounds with one or more P—C bonds
    • C07F9/54Quaternary phosphonium compounds
    • C07F9/5456Arylalkanephosphonium compounds
    • 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
    • C09K23/00Use of substances as emulsifying, wetting, dispersing, or foam-producing agents
    • 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
    • C09K23/00Use of substances as emulsifying, wetting, dispersing, or foam-producing agents
    • C09K23/017Mixtures of compounds
    • 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
    • C09K23/00Use of substances as emulsifying, wetting, dispersing, or foam-producing agents
    • C09K23/14Derivatives of phosphoric acid

Definitions

  • This invention relates to ionic liquids and certain uses thereof. Particularly, it relates to the use of ionic liquids as surfactants (emulsiflers), and to the use of ionic liquid surfactants (emulsifiers) for forming stable emulsions and microemulsions.
  • ionic liquids have been shown to be of great value in a wide variety of solvent applications owing to the ability to tailor their physical properties to the particular solvent application. This is achieved by varying the molecular structure of the components of the ionic liquid. Accordingly, ionic liquids have become known as "Designer Solvents" and have been subject to a great deal of interest in the chemical, pharmaceutical, petrochemical and chemical engineering industries.
  • An ionic liquid is an ionic material (typically an ion-pair) that is in a liquid state at a temperature of below 150°C, particularly, at a temperature of below 100 0 C. Owing to ionic liquids being comprised entirely of dissociated ions, they show vastly reduced vapour pressures when compared with traditional organic solvents thereby minimizing the risk of atmospheric contamination. As ionic liquids are essentially non- volatile, they have a further advantage when compared with traditional organic solvents in that they have no odour thereby reducing health concerns. Yet a further advantage of ionic liquids when compared with traditional organic solvents is that they can be composed of ions of low toxicity.
  • ionic liquids as solvents allows them to be tailored to have the desired solubility for the intended solute.
  • ionic liquids have found utility as solvents for a wide variety of materials including heavy oils, coal residues, inorganic crystalline materials and silicon compounds.
  • Ionic liquid solvents can also be tailored to have the desired miscibility with an intended cosolvent.
  • a wide variety of ionic liquids solvents are available which show the whole range of miscibility with water or organic cosolvents.
  • Ionic liquids are also available that form stable emulsions with water or organic solvents where the ionic liquid forms either the continuous or discontinuous phase of the emulsion.
  • the present invention relates to the synthesis of certain selected surface active ionic liquids that are capable of reducing the interfacial surface tension between two or more phases selected from the group consisting of solid, liquid, gaseous, ionic and supercritical phases.
  • the enhanced miscibility of the phases and/or the lowering of surface tension forces resulting from the employment of the ionic liquid surfactants of the present invention can be used to aid the formation of emulsions, microemulsions or foams.
  • the present invention relates to a surfactant characterized in that the surfactant is a salt of general formula C + A " that is in a liquid state at a temperature below 150°C and at least one of the cation, C + , and the anion, A " , has a hydrophobic tail group attached to an ionic head group.
  • both the cation, C + , and the anion, A " , of the surfactant have at least one hydrophobic tail group so that both the cation and anion have surface active properties.
  • the surfactant is in a liquid state at a temperature below 150°C and is characterized in that the surfactant is an ionic liquid salt of general formula C + A " and the cation, C , comprises at least one hydrophobic tail group attached to a cationic head group and the anion, A " , comprises at least one hydrophobic tail group attached to an anionic head group.
  • the cation, C + has at least one hydrophobic tail group
  • the cation, C + has 1 to 4 hydrophobic tail groups attached to the cationic head group.
  • the anion, A " has at least one hydrophobic tail group
  • the anion, A " has 1 or 2 hydrophobic tail groups attached to the anionic head group.
  • the hydrophobic tail groups are hydrocarbyl tail groups.
  • the hydrocarbyl tail group(s) of the cation, C + , and/or anion, A " may be a halogenated hydrocarbyl group such as a fluorinated hydrocarbyl group. It is also possible for the hydrocarbyl tail group to bear substituents provided that the substituents do not adversely affect the desired surface active properties of the cation and/or anion. Acceptable ' substituents include alkoxy and hydroxyl groups.
  • the hydrocarbyl tail group is an alkyl group, alkenyl group or alkynyl group having at least 8 carbon atoms.
  • the alkyl group, alkenyl group or alkynyl group has from 8 to 30 carbon atoms, more preferably 12 to 24 carbon atoms, most preferably 16 to 20 . carbon atoms.
  • the alkyl, alkenyl or alkynyl group may be a straight chain or branched chain group.
  • the hydrocarbyl tail group may also be an alkaryl substituent having at least 8, preferably, at least 10 carbon atoms, more preferably, at least 12 carbon atoms, for example, 12 to 24 carbon atoms.
  • the hydrocarbyl tail group may also be a poly(oxyethylene) group, -(CH 2 CH 2 O) x R (where R is H or methyl and x is an integer of from 4 to 15, preferably 5 to 10.
  • the cation, C + is selected from the group consisting of:
  • R 1 R 2 R 3 R 4 M wherein M is N or P; R and R are independently selected from methyl or ethyl groups;
  • R is a C 8 to C 30 alkyl group, preferably a C 12 to C 28 alkyl group, for example, a C 14 to
  • R 4 is selected from the group consisting of methyl, ethyl and a Cg to C 30 alkyl group
  • preferred quaternary ammonium or phosphonium cations of this class include hexadecyltrimethylphosphonium, hexadecyltriethylphosphonium, octadecyltrimethylphosphonium, octadecyltriethylphosphonium, dihexadecyldimethylphosphonium, dioctadecyldimethylphosphonium hexadecyltrimethylammonium, hexadecyltriethylammonium, octadecyltrimethylammonium, octadecyltriethylammonium, dihexadecyldimethylammonium, and dioctadecyldimethylammonium.
  • R 1 R 2 R 3 R 4 M wherein M is N or P; R 1 and R 2 are independently selected from methyl or ethyl groups;
  • R 3 is -(CH 2 ) ⁇ C 6 H 4 R' wherein n is an integer of from 0 to 5, preferably, 0 to 3; and R' is selected from the group consisting of H, Cl, Br, I, NO 2 , C 1 to C 30 alkyl groups (preferably C 1 to C 20 alkyl groups), -SO 2 R", -SOR” and -C(O)R" (wherein R" is a Ci to C 30 alkyl group, preferably a C 1 to C 20 alkyl group) with the proviso that the R 3 group has at least 8 carbon atoms; and
  • R 4 is a C 8 to C 30 alkyl group (preferably a C 12 to C 28 alkyl group, for example, a C 14 to C 24 alkyl group) or is an R 3 group.
  • R 2 is a C 5 to C 3 o alkyl group, preferably a C 10 to C 28 alkyl group, more preferably a C 14 to C 24 alkyl group;
  • R 1 and R 2 are independently selected from methyl and ethyl;
  • R 3 is a C 8 to C 30 alkyl group, preferably a C 12 to C 28 alkyl group, most preferably, a C 14 to C 24 alkyl group;
  • R 4 is H or a C 1 to C 4 alkyl, preferably, H, methyl or ethyl.
  • Quaternary ammonium ions of this type may be prepared by protonating or alkylating the corresponding amine oxide, R 1 R 2 R 3 N + O ' .
  • Quaternary ammonium salts of this class are derived from choline, [(CH 3 ) 3 N(CH 2 CH 2 OH)] + .
  • R 5 is a hydrocarbyl group selected from (i) C 8 to C 30 alkyl groups or (ii) -(CH 2 ) n C 6 H 4 R' wherein n is an integer of from 0 to 5, R' is selected from the group consisting of H, Cl, Br, I, NO 2 , C 1 to C 30 alkyl groups (preferably C 1 to C 20 alkyl groups), -SO 2 R", -SOR” and -C(O)R” (wherein R" is a C 1 to C 30 alkyl group, preferably a C 1 to C 20 alkyl group) with the proviso that R 5 has at least 8 carbon atoms.
  • Quaternary ammonium ions of this class may, for example, be prepared from tetramethylethylenediamine or tetraethylethylenediamine by reaction with R 5 X where X is a good leaving group, for example, a halide.
  • the cation may also comprise an aromatic or non-aromatic heterocyclic ring structure having at least one hydrophobic tail group, preferably a hydrocarbyl tail group as a substituent on the heterocyclic ring. It is envisaged that the heterocyclic ring may have from 1 to 3 hydrocarbyl substituents.
  • the heterocyclic ring structure of the cation is selected from imidazolium, imidazolinium, pyridinium, pyrazolium, thiazolium, isothiazolinium, azathiozolium, oxothiazolium, oxazinium, oxazolium, oxaborolium, dithiozolium, trizdium, selenozolium, oxaphopholium, pyrollium, borolium, furanium, ⁇ thiophenium, phospholium, pentazolium, indolium, indolinium, oxazolium, isooxazolium, isotriazolium, tetrazolium, benzofuranium, diborzofuranium, benzothiophenium, dibenzothiophenium, thiadiazolium, pyrimidinium, pyrazinium, pyridazinium, piperazinium, piperidinium,
  • Preferred heterocyclic cations include: (a) non-aromatic heterocycles such as:
  • M is N or P
  • R 1 is C 8 to C 30 alkyl group; and R 2 is selected from methyl, ethyl or a C 8 to C 30 alkyl group. Where R 1 and R 2 are both C 8 to C 30 alkyl groups, it is preferred that R 1 and R 2 are of different length, for example, R 1 may be a C 8 to C 12 alkyl group and R 2 a C 16 to C 30 alkyl group, (b) Imidazolium ions of the general formula:
  • R 1 is a C 8 to C 30 alkyl group, preferably a C 12 to C 28 alkyl group, for example, a C 16 to C 24 alkyl group;
  • R 2 is selected from H, methyl and ethyl, preferably H;
  • R 3 is selected from methyl, ethyl and C 8 to C 30 alkyl groups, preferably, methyl or ethyl;
  • R 4 and R 5 are H or a halide (for example, Cl or Br).
  • R 1 is hydrophobic substituent selected from (i) C 8 to C 30 alkyl groups
  • R' is selected from the group consisting of H, Cl 5 Br, I, NO 2 , C 1 to C 30 alkyl groups (preferably C 1 to C 20 alkyl groups), -SO 2 R", -SOR” and -C(O)R" (wherein R" is a C 1 to C 30 alkyl group, preferably a C 1 to C 20 alkyl group) with the proviso that - (CH 2 ) J1 C 6 H 4 R' contains at least 8 carbon atoms; and
  • R 2 and R 3 are independently selected from H and dimethylamino, or are R 1 groups.
  • Particularly preferred pyridinium ions of this class include dodecylpyridinium, 1,4- didodecylpyridinium, hexadecylpyridinium, 1,4-dihexadecylpyridinium, octadecylpyrinidium, 1 ,4-octadecylpyridinium, 4-(dimethylamino)dodecylpyridinium, 2-(dimethylamino)dodecylpyridinium, 4-(dimethylamino)hexadecylpyridinium and 2- (dimethylamino)hexadecylpyridmium.
  • the pyridinium ion may be prepared from 4- dimethylaminopyridine or 2-dimethylaminopyridine respectively, (d) an oxazole of general formulae:
  • R 1 is a hydrocarbyl substituent selected from (i) C 8 to C 30 alkyl groups (preferably C 12 to C 28 alkyl groups) and (ii) -(CH 2 ) n C 6 H 4 R' wherein n is an integer from
  • R' is selected from the group consisting of H, Cl, Br, I, NO 2 , C 6 to C 30 alkyl groups (preferably C 1 to C 20 alkyl groups), -SO 2 R", -SOR” and -C(O)R" (wherein R" is a C 1 to C 30 alkyl group, preferably a C 1 to C 20 alkyl group) with the proviso that -
  • R' contains at least 8 carbon atoms; and R and R 3 are independently selected from H, methyl or ethyl.
  • R is a hydrocarbyl substituent selected from (i) Cg to C 30 alkyl groups and (ii) - (CH 2 ) n C 6 H 4 R' wherein n is an integer from 0 to 5, R' is selected from the group consisting of H, Cl, Br, I, NO 2 , C 1 to C 30 alkyl groups (preferably C 1 to C 20 alkyl groups), -SO 2 R' ' , -SOR' ' and -C(O)R' ' (wherein R" is a C 1 to C 30 alkyl group, preferably a Ci to C 20 alkyl group) with the proviso that -(CH 2 ) H C 6 H 4 R' contains at least 8 carbon atoms.
  • the anion, A " is selected from the group consisting of: (a) dialkyl phosphase anions of the general formula: [R 1 R 2 P(O)O]- wherein R 1 and R 2 are independently selected from C 8 to C 30 , preferably C 12 to C 18 , alkyl groups.
  • the alkyl groups may be branched or unbranched. Particularly preferred alkyl groups include dodecyl, hexadecyl, octadecyl, and 2,4,4-trimethylpentyl.
  • a commercially available example of a dialkyl phosphase anion of general formula (II) is Cyanex-272TM (2,4,4-trimethylpentyl phosphase) :
  • the alkyl groups may be branched or unbranched.
  • ROSO 3 ' wherein R is a straight chain or branched chain alkyl group having at least 8 carbon atoms, preferably, a C 8 to C 30 alkyl group, more preferably a C 12 to C 24 alkyl group, for example, a Ci 6 to C 20 alkyl group.
  • alkyl sulfate anions include dodecyl sulfate, hexadecyl sulfate and octadecyl sulfate.
  • sulfated polyoxyethylene (POE) straight chain alcohols of general formula: R(OCH 2 CH 2 ) X SO 4 - wherein R is a C 8 to C 30 alkyl group and x is an integer in the range 1 to 10, preferably, 2 to 5.
  • RSO 3 - wherein R is a straight chain or branched chain alkyl group having at least 8 carbon atoms, preferably, a C 8 to C 30 alkyl group, more preferably a C 12 to C 24 alkyl group, for example, a C 16 to C 2 o alkyl group.
  • alkyl sulfonate anions include dodecanesulfonate and hexadecanesulfonate.
  • alkylbenzylsulfonates of general formula: RC 6 H 4 SO 3 " where R is a C 2 to C 30 alkyl group, preferably, a Cg to Ci 5 alkyl group.
  • the alkyl group may be in the 2-, 3-, or 4- position on the phenyl ring, preferably, the 4-position.
  • the alkyl group may be branched or unbranched.
  • the alkyl group is - CH(CH 3 )(CH 2 ) n CH 3 where n is an integer in the range 9 to 12.
  • Preferred alkylbenzyl sulfonates include dodecylbenzenesulfonate, hexadecylbenzenesulfonate and octadecylbenzenesulfonate.
  • R is a straight chain or branched chain C 4 to C 30 alkyl group, and R' is methyl or ethyl.
  • ROSO 3 ' wherein R is a straight chain or branched chain C 8 to C 30 alkyl group
  • sulfosuccinate esters of general formula: R 1 OOCCH 2 CH(SO 3 OCOOR 2 wherein R 1 and R 2 are straight chain or branched chain C 5 to C 30 alkyl groups.
  • arylalkanesulfonates of general formula:
  • R 1 is selected from the group consisting of H 5 Cl, Br, I, NO 2 , C 1 to C30 alkyl groups (preferably a C 1 to C 20 alkyl group), -SO 2 R', -SOR' and -C(O)R' (wherein R' is a C 1 to C 30 alkyl group, preferably a Ci to C 20 alkyl group.
  • Such sulfonates are prepared by sulfonating an olefin and then treating the intermediate product with an aromatic compound.
  • R 1 and R 2 are straight chain or branched chain C 8 to C 30 alkyl groups.
  • the ionic liquid surfactant may also be a protonated ionic liquid formed by the following reaction:
  • cation and/or the anion has at least one hydrophobic tail group, for example, a C 8 to C 30 alkyl substituent.
  • R 1 is a C 16 to C 30 alkyl group
  • R 2 is selected from H, methyl and ethyl
  • R 3 is selected from methyl, ethyl and C 8 to C 30 alkyl groups
  • R 4 and R 5 are H, or halogen.
  • R 1 is a C 8 to C 30 alkyl group
  • R 2 and R 3 are independently selected from (i) H; (ii) dimethylamino; (iii) C 8 to C 30 alkyl groups; and (iv) -(CH 2 ) H C 6 H 4 R' wherein n is an integer of from 0 to 5, R' is selected from the group consisting of H, Cl, Br, I, NO 2 , C 1 to C 30 alkyl groups, -SO 2 R", -SOR" and -C(O)R" (wherein R" is a C 1 to C 30 alkyl group) with the proviso that -(CH 2 ) H C 6 H 4 R' contains at least 8 carbon atoms.
  • a salt of the general formula Ic existing in a liquid state at a temperature below 150°C; in which A " is an anion; and in which the cation, C + , is selected from one of the quaternary ammonium or phosphonium groups (a) to (g) defined above.
  • R 1 and R 2 are independently selected from C 8 to C 30 alkyl groups; and in which the cation, C + , is an imidazolium ion of the general formula:
  • R 1 is an alkyl group having up to 15 carbon atoms
  • R 2 is selected from H 5 methyl and ethyl
  • R 3 is selected from methyl, ethyl and C 8 to C 30 alkyl groups
  • R 4 and R 5 are H or halogen.
  • the ionic liquid surfactants (emulsifiers) of the present. invention may be classified using the hydrophilic-lipophilic balance (HLB) system that employs a scale of 0 to 20 based on the affinity of the surfactants for oil or water. Surfactants with low HLB values are more lipophilic while surfactants with higher HLB values are more hydrophilic.
  • the HLB values of the ionic liquid surfactants may be determined empirically by comparison with conventional surfactants of predetermined HLB value.
  • ionic liquid surfactants will have the following properties or functions based on their HLB values:
  • surfactants with HLB values of 3 to 8 are more oil soluble and will form water in oil emulsions while surfactants having an HLB value of greater than 9, preferably, 9 to 18, are more water soluble and will form oil in water emulsions.
  • the present invention provides a water in oil or oil in water emulsion which comprises (i) an oil phase, (ii) an aqueous phase and (iii) an ionic liquid surfactant wherein the ionic liquid surfactant is a salt of general formula I: C + A ' (I) the salt of general formula I existing in a liquid state at a temperature below 150°C; at least one of the cation, C + , and anion, A ' , comprising a hydrophobic tail group attached to an ionic head group; and A " represents an anion containing phosphorus, or an alkyl sulfate anion of general formula: ROSO 3 " wherein R is an alkyl group having at least 8 carbon atoms.
  • the present invention provides a water in oil or oil in water emulsion which comprises (i) an oil phase, (ii) an aqueous phase and (iii) a novel ionic liquid surfactant as defined above.
  • An emulsion of the invention may be a microemulsion.
  • the microemulsion may be an oil in water microemulsion where the oil is dispersed in a continuous aqueous phase or a water in oil microemulsion where the water is dispersed in a continuous oil phase.
  • the microemulsion in a water in oil microemulsion.
  • the water in oil microemulsion of the present invention may be used for deploying water soluble or water dispersible oil field or gas field production chemicals as described in International Patent Application No. WO 0100747 or in enhanced oil recovery.
  • Microemulsions in general are known, see, for example "Microemulsions", Editor I D Robb, Plenum Press, New York, 1982 which is herein incorporated by reference. Microemulsions differ from conventional emulsions in that they form spontaneously upon mixing of the oil phase, aqueous phase and the surfactant. They also differ from ordinary emulsions in having droplets of very small size or in having microdomains having at least one dimension of length, breadth or thickness of very small size. Thus, microemulsions appear clear to the naked eye or even the optical microscope, compared to the larger droplets (greater than 100 nm diameter) of conventional cloudy emulsions.
  • the aqueous phase of the water in oil microemulsion is distributed in a continuous oil phase in the form of droplets having a diameter in the range 1 to 100 nm or in the form of microdomains having at least one dimension of length, breadth or thickness in the range 1 to 100 nm.
  • the aqueous phase of the water in oil microemulsion is distributed in the oil phase in the form of droplets, the droplets preferably have an average diameter in the range of 10 to 500 nm, more preferably 50 to 250 nm.
  • the droplet size distribution is generally such that at least 90% of the diameters are within 20% or especially 10% of the average diameter.
  • the microemulsions are transparent to the eye and are apparently isotropic.
  • the microdomains preferably have at least one dimension of length, breadth or thickness in the range 10 to 500 ran, more preferably 50 to 250 nni.
  • the oil phase is essentially any liquid which is immiscible with the aqueous phase.
  • the oil phase may be selected from the group consisting of liquid alkanes (preferably C 5 -C 20 alkanes, more preferably C 8 to C 15 alkanes, most preferably C 9 -C 12 alkanes, for example, n-hexane, n-nonane, n-decane, and n-undecane), alkenes, liquid alkyl halides (for example, carbon tetrachloride or dichloromethane) and liquid aromatic hydrocarbons (for example, benzene, toluene and xylene).
  • liquid alkanes preferably C 5 -C 20 alkanes, more preferably C 8 to C 15 alkanes, most preferably C 9 -C 12 alkanes, for example, n-hexane, n-nonane, n-decane, and n-undecan
  • the oil phase may also be a paraffin oil, a natural oil (for example, a vegetable or animal oil), diesel, kerosene, gas oil, crude oil, lubricant base oil, liquid carbon dioxide, liquid chlorofluorocarbons such as CCIiF 2 , CHCl 2 F and CH 3 CClF 2 (known as freons), tetrahydrofuran, dimethyl formamide and dimethyl sulfoxide.
  • a paraffin oil for example, a vegetable or animal oil
  • diesel kerosene
  • gas oil crude oil
  • lubricant base oil liquid carbon dioxide
  • liquid chlorofluorocarbons such as CCIiF 2 , CHCl 2 F and CH 3 CClF 2 (known as freons)
  • freons liquid chlorofluorocarbons
  • the aqueous phase may additionally comprise a water miscible solvent such as methanol, ethanol, n-propanol, iso-propanol, n-butanol, iso-butanol, tert-butanol, butyl monoglycol ether, butyl diglycol ether, butyl triglycol ether, ethylene glycol mono butyl ether and ethylene glycol.
  • a water miscible solvent such as methanol, ethanol, n-propanol, iso-propanol, n-butanol, iso-butanol, tert-butanol, butyl monoglycol ether, butyl diglycol ether, butyl triglycol ether, ethylene glycol mono butyl ether and ethylene glycol.
  • the amount of water miscible solvent which may be present in the aqueous phase is in the range 0.5 to 50 % by weight, preferably 5 to 30 % by weight based on the total weight of water and water miscible solvent.
  • an advantage of the ionic liquid surfactant of the present invention is that the microemulsion is stable even in the absence of a water miscible solvent.
  • a salt such as sodium chloride or magnesium sulfate is added to the aqueous phase of a conventional microemulsion in order to enhance the stability of the microemulsion.
  • the aqueous phase of a conventional microemulsion is generally saturated with the salt.
  • a further advantage of the microemulsion of the present invention is that there is no requirement to add a salt to stabilize the emulsion.
  • a salt may be included in the aqueous phase of the emulsion.
  • the volume fraction of the aqueous phase in the microemulsion is generally in the range from 1-50%, preferably 10 to 40%, more preferably 23 to 30%.
  • the ionic liquid surfactant is suitably present in the microemulsion in an amount ranging from 0.1 to 5 mole %, preferably 0.25 to 2 mole %, for example 0.5 to 1 mole %.
  • the aqueous phase of the microemulsion may comprise fresh, tap, river, sea, produced or formation water.
  • the aqueous phase may have a total salinity of 0-250 g/1, for example 5-50 g/1.
  • the aqueous phase may have a pH of 0.5-9.
  • the aqueous phase comprises a sea-water solution of a highly acidic production chemical such as, for example, a scale inhibitor, the aqueous phase usually has a highly acidic pH of 0.1 - 1.
  • the aqueous phase is neutralized prior to being mixed with the organic phase and surfactant to form the microemulsion.
  • both the cation and the anion of the ionic liquid surfactant that is used to form the microemulsion have at least one hydrocarbyl tail group.
  • the cation of the ionic liquid surfactant has at least one hydrophobic tail group having a chain length of at least 16 carbon atoms, preferably 18 to 30 carbon atoms while the anion of the ionic liquid surfactant has at least one hydrophobic tail group having a chain length of 8 to 12 carbon atoms, preferably 8 to 10 carbon atoms.
  • the anion of the ionic liquid may have at least one hydrophobic tail group having a chain length of at least 16 carbon atoms, preferably 18 to 30 carbon atoms while the cation has at least one hydrocarbyl tail group having a chain length of 8 to 12 carbon atoms, more preferably, 8 to 10 carbon atoms.
  • the cation and anion have hydrophobic tail groups that are of different length that this increases the stability of the microemulsion by enhancing the packing of the surfactant in the interfacial film.
  • Mixtures of ionic liquid surfactants may be employed to prepare the microemulsion, for example, 2 or 3 ionic liquid surfactants.
  • microemulsion is thermally stable. It is possible to devise microemulsions which are stable over a wide temperature range e.g. from ambient to 300 0 C or from 90 to about 150°C. However, it is not essential that the microemulsion is stable across the whole of the range of from ambient to 150°C. For example, the microemulsion may be stable between ambient and 70°C or between 40 and 80°C.
  • the microemulsion of the present invention forms spontaneously on gentle mixing of the aqueous phase, the oil phase and the ionic liquid surfactant in any order; conveniently, the aqueous phase is mixed last into a mixture of the oil phase and the ionic liquid surfactant.
  • microemulsion If the material made is initially cloudy, then a microemulsion has not been produced, and minor adjustments to the relative proportions of the ingredients or a change in the nature of the ionic liquid surfactant or the temperature may be needed.
  • the microemulsion can be characterized by x-ray diffraction to show the presence of the droplets or domains.
  • the ionic liquid surfactants may be used to form conventional emulsions, in which, for example, the internal phase of the emulsion is distributed in a continuous external phase in the form of droplets having a diameter in the range 0.01 to about 100 microns.
  • Conventional emulsions differ from microemulsions in that it is necessary to input energy to form the emulsion. In principle, a microemulsion and a conventional emulsion may coexist.
  • the conventional emulsion may be an oil in water emulsion where an internal oil phase in dispersed in the form of droplets in a continuous external aqueous phase or a water in oil emulsion where an internal aqueous phase is dispersed in the form of droplets in a continuous external oil phase.
  • the type of conventional emulsion is dependent upon the nature of the ionic liquid surfactant (emulsifier).
  • the ionic liquid surfactant that is employed to generate the emulsion is comprised of a cation, C + , having at least one hydrophobic tail group attached to a cationic head group and an anion, A " , having at least one hydrophobic tail group attached to an anionic head group.
  • ionic liquid surfactants may be employed to prepare the conventional emulsion of the present invention, for example, 2 or 3 ionic liquid surfactants.
  • a water in oil emulsion may be formed by dissolving minor amounts of the oil soluble ionic liquid surfactant in the oil that is to form the continuous oil phase of the emulsion.
  • the concentration of oil-soluble ionic liquid surfactant in the resulting solution may be in the range of from 0.1 to 5 mole %, preferably 0.25 to 2 mole %, most preferably 0.5 to 1 mole %.
  • the emulsion is preferably formed by pouring the aqueous phase into the solution of the oil-soluble ionic liquid surfactant in the oil phase while intensive blending is applied (thereby imparting energy to form the emulsion).
  • the blending operation for the emulsion should be designed to minimize the size of the internal phase water droplets since this may increase the stability of the emulsion.
  • the mixture should be vigorously stirred or sheared for about 5 to 20 minutes, the rate of shear being highly dependent on the size and type of mixing device employed. Stirring rate and times should be designed to form small aqueous droplets, preferably having average diameters of from about 0.3 to about 100 microns and preferably from about 1 to about 10 microns.
  • the internal phase of the emulsion should amount to from 10 to 70 percent, more preferably from 30 to 60 percent of the total volume of the emulsion. Density control of the water in oil emulsion may be used to enhance its stability.
  • weighting agents may be added to the internal aqueous phase of the emulsion.
  • soluble salts such as sodium or potassium chloride may be added to the internal aqueous phase.
  • the aqueous phase may comprise from 0.5 to 20 percent by weight of soluble salts.
  • the ionic liquid surfactant has an HLB value of greater than 9, preferably.
  • an oil in water emulsion may be formed by dissolving minor amounts of the water soluble ionic liquid surfactant in the aqueous phase.
  • the concentration of water-soluble ionic liquid surfactant in the resulting solution may be in the range of from 0.1 to 5 mole%, preferably 0.25. to 2 mole%.
  • the emulsion is preferably formed by pouring the oil phase into the solution of the water-soluble ionic liquid surfactant in the aqueous phase while intensive blending is applied, as described above for the preparation of a water in oil emulsion.
  • the blending operation for the emulsion should be designed to minimize the size of the internal phase oil droplets since this may increase the stability of the emulsion.
  • Stirring rate and times should be designed to form small oil droplets having average diameters of from about 0.3 to about 100 microns and preferably from about 1 to about 10 microns.
  • the internal oil of the emulsion should amount to from 1 to 80 percent, more preferably from 5 to 50 percent of the total volume of the emulsion.
  • the water in oil emulsion may be used to deploy a water-soluble or water-dispersible production chemical, as described above for a water in oil microemulsion.
  • the conventional emulsion may also act as the base fluid of a wellbore fluid, for example, a drilling fluid or completion fluid.
  • An advantage of the conventional emulsion is that the use of the ionic liquid surfactant renders the emulsion more stable under high temperature and/or high pressure conditions than emulsions formed using conventional emulsifiers.
  • the emulsions are also more tolerant of metal ions and are less likely to form scums.
  • ionic liquid surfactants of the present invention have many other applications including their use:
  • foam compositions for example, for mobility control in gas and/or gas condensate reservoirs where the foam is used to block a high permeability zone and to divert a gas into a low permeability zone.
  • suitable foaming agents include l-octadecyl-3-methylimidazolium bis(2,4,4- trimethylpentyl)phosphate and 1-octadecylpyridinium bis(2,4,4- trimethylpentyl)phosphate .
  • hydrophobic solvents particularly, terpene free hydrophobic solvents
  • the ionic liquid surfactant may act as a heat transfer agent (to transfer heat from the drill bit), as a lubricant for the drill bit, as a weighting agent or as a fluid loss control agent.
  • the surfactant may act as a gas hydrate inhibitor, corrosion inhibitor or drag reducer.
  • the invention therefore further provides the use of a salt as defined above in the above applications.
  • the invention provides a composition in the form of a foam, which comprises, as a foaming agent, a salt as defined above, especially a composition suitable for use in a gas and/or gas condensate reservoir.
  • Example 1 Preparation of l-octadecyl-3-methylimidazolium bis(2A4-1ximethyrpentyl)phosphonate rCismimirfisoCgbPCM
  • Example 13 Preparation of ionic liquid - water — hexane microemulsions Water (10 cm ), hexane (10 cm ) and ionic liquid (0.5 g) were mixed together in a 25 ml measuring cylinder. Three phases were observed and visualised by the addition of rhodamine B dye (ca. 1 microgram), with a lower aqueous phase, a middle microemulsion phase and an upper hexane phase. It was found that the volume of the middle microemulsion phase was dependent upon the structure of the ionic liquid surfactant.
  • Example 14 1 -ethyl-3-methylimidazolium bisf2 A4-trimethylpentyl)phosphonate
  • Potassium bis(2,4,4-trimethylpentyl)phosphonate (derived from KOH and Cyanex-272), (25.0 g of 0.4 M solution in water) and a solution of l-ethyl-3-methylimidazolium bromide (2.38 g, 12.5 mmol) in 20 cm 3 of deionised water were mixed together to form a hazy solution.
  • Toluene (20 ml) was added and the solution was placed on a rotary evaporator to remove the toluene / water. This was repeated twice. More toluene was added (20 ml) to give 3 phases and the middle (microemulsion) and upper phases were separated and washed with distilled water (20 ml).

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Abstract

The invention provides a water in oil or oil in water emulsion which comprises a (i) an oil phase, (ii) an aqueous phase and (iii) an ionic liquid surfactant wherein the ionic liquid surfactant is a salt of general formula (I): C+ A- (I) the salt of general formula (I) existing in a liquid state at a temperature below 15O0C; at least one of the cation, C+, and anion, A-, comprising a hydrophobic tail group attached to an ionic head group; and A- represents an anion containing phosphorus, or an alkyl sulfate anion of general formula: ROSO 3 - wherein R is an alkyl group having at least 8 carbon atoms. Various novel ionic liquid salts in which at least one of the cation and anion comprises a hydrophobic tail group attached to an ionic head group, are also provided by the invention.

Description

IONIC LIQUIDS AND USES THEREOF
This invention relates to ionic liquids and certain uses thereof. Particularly, it relates to the use of ionic liquids as surfactants (emulsiflers), and to the use of ionic liquid surfactants (emulsifiers) for forming stable emulsions and microemulsions. Room-temperature ionic liquids have been shown to be of great value in a wide variety of solvent applications owing to the ability to tailor their physical properties to the particular solvent application. This is achieved by varying the molecular structure of the components of the ionic liquid. Accordingly, ionic liquids have become known as "Designer Solvents" and have been subject to a great deal of interest in the chemical, pharmaceutical, petrochemical and chemical engineering industries.
An ionic liquid is an ionic material (typically an ion-pair) that is in a liquid state at a temperature of below 150°C, particularly, at a temperature of below 1000C. Owing to ionic liquids being comprised entirely of dissociated ions, they show vastly reduced vapour pressures when compared with traditional organic solvents thereby minimizing the risk of atmospheric contamination. As ionic liquids are essentially non- volatile, they have a further advantage when compared with traditional organic solvents in that they have no odour thereby reducing health concerns. Yet a further advantage of ionic liquids when compared with traditional organic solvents is that they can be composed of ions of low toxicity. The flexibility of ionic liquids as solvents allows them to be tailored to have the desired solubility for the intended solute. Thus, ionic liquids have found utility as solvents for a wide variety of materials including heavy oils, coal residues, inorganic crystalline materials and silicon compounds. Ionic liquid solvents can also be tailored to have the desired miscibility with an intended cosolvent. Thus, a wide variety of ionic liquids solvents are available which show the whole range of miscibility with water or organic cosolvents. Ionic liquids are also available that form stable emulsions with water or organic solvents where the ionic liquid forms either the continuous or discontinuous phase of the emulsion.
The present invention relates to the synthesis of certain selected surface active ionic liquids that are capable of reducing the interfacial surface tension between two or more phases selected from the group consisting of solid, liquid, gaseous, ionic and supercritical phases. The enhanced miscibility of the phases and/or the lowering of surface tension forces resulting from the employment of the ionic liquid surfactants of the present invention can be used to aid the formation of emulsions, microemulsions or foams.
In its broadest aspect, the present invention relates to a surfactant characterized in that the surfactant is a salt of general formula C+A" that is in a liquid state at a temperature below 150°C and at least one of the cation, C+, and the anion, A", has a hydrophobic tail group attached to an ionic head group.
Preferably, both the cation, C+, and the anion, A", of the surfactant (hereinafter "ionic liquid surfactant") have at least one hydrophobic tail group so that both the cation and anion have surface active properties. Thus, in a preferred embodiment of the present invention the surfactant is in a liquid state at a temperature below 150°C and is characterized in that the surfactant is an ionic liquid salt of general formula C+A" and the cation, C , comprises at least one hydrophobic tail group attached to a cationic head group and the anion, A", comprises at least one hydrophobic tail group attached to an anionic head group. Where the cation, C+, has at least one hydrophobic tail group, it is preferred that the cation, C+, has 1 to 4 hydrophobic tail groups attached to the cationic head group. Where the anion, A", has at least one hydrophobic tail group, it is preferred that the anion, A", has 1 or 2 hydrophobic tail groups attached to the anionic head group.
Preferably, the hydrophobic tail groups are hydrocarbyl tail groups. Suitably, the hydrocarbyl tail group(s) of the cation, C+, and/or anion, A", may be a halogenated hydrocarbyl group such as a fluorinated hydrocarbyl group. It is also possible for the hydrocarbyl tail group to bear substituents provided that the substituents do not adversely affect the desired surface active properties of the cation and/or anion. Acceptable' substituents include alkoxy and hydroxyl groups. Generally, the hydrocarbyl tail group is an alkyl group, alkenyl group or alkynyl group having at least 8 carbon atoms. Preferably, the alkyl group, alkenyl group or alkynyl group has from 8 to 30 carbon atoms, more preferably 12 to 24 carbon atoms, most preferably 16 to 20 . carbon atoms. The alkyl, alkenyl or alkynyl group may be a straight chain or branched chain group. The hydrocarbyl tail group may also be an alkaryl substituent having at least 8, preferably, at least 10 carbon atoms, more preferably, at least 12 carbon atoms, for example, 12 to 24 carbon atoms. The hydrocarbyl tail group may also be a poly(oxyethylene) group, -(CH2CH2O)xR (where R is H or methyl and x is an integer of from 4 to 15, preferably 5 to 10.
Suitably, the cation, C+ is selected from the group consisting of:
(a) quaternary ammonium or phosphonium ions of general formula:
[R1R2R3R4M]+ wherein M is N or P; R and R are independently selected from methyl or ethyl groups;
R is a C8 to C30 alkyl group, preferably a C12 to C28 alkyl group, for example, a C14 to
C24 alkyl group and
R4 is selected from the group consisting of methyl, ethyl and a Cg to C30 alkyl group,
(preferably a C12 to C28 alkyl group, for example, a C14 to C24 alkyl group). Particularly, preferred quaternary ammonium or phosphonium cations of this class include hexadecyltrimethylphosphonium, hexadecyltriethylphosphonium, octadecyltrimethylphosphonium, octadecyltriethylphosphonium, dihexadecyldimethylphosphonium, dioctadecyldimethylphosphonium hexadecyltrimethylammonium, hexadecyltriethylammonium, octadecyltrimethylammonium, octadecyltriethylammonium, dihexadecyldimethylammonium, and dioctadecyldimethylammonium.
(b) quaternary ammonium or phosphonium ions of general formula:
[R1R2R3R4M]+ wherein M is N or P; R1 and R2 are independently selected from methyl or ethyl groups;
R3 is -(CH2)πC6H4R' wherein n is an integer of from 0 to 5, preferably, 0 to 3; and R' is selected from the group consisting of H, Cl, Br, I, NO2, C1 to C30 alkyl groups (preferably C1 to C20 alkyl groups), -SO2R", -SOR" and -C(O)R" (wherein R" is a Ci to C30 alkyl group, preferably a C1 to C20 alkyl group) with the proviso that the R3 group has at least 8 carbon atoms; and
R4 is a C8 to C30 alkyl group (preferably a C12 to C28 alkyl group, for example, a C14 to C24 alkyl group) or is an R3 group.
(c) triethanolamine ester quaternary ammonium or phosphonium ions of general formula:
[(R2CO2CH2CH2)2M(R1)CH2CH2OH]+ wherein M is N or P; R1 is methyl or ethyl; and
R2 is a C5 to C3o alkyl group, preferably a C10 to C28 alkyl group, more preferably a C14 to C24 alkyl group;
(d) quaternised polyoxyethylenated (POE) long-chain amines:
[R1R2NKCH2CH2O)xH)2I+ wherein R1 and R2 are independently selected from methyl and ethyl; and x is an integer of from 4 to 15, preferably, 5 to 10;
(e) quaternary ammonium ions of general formula:
[R1R2R3NOR4J+ wherein R1 and R2 are independently selected from methyl and ethyl; R3 is a C8 to C30 alkyl group, preferably a C12 to C28 alkyl group, most preferably, a C14 to C24 alkyl group; and
R4 is H or a C1 to C4 alkyl, preferably, H, methyl or ethyl.
Quaternary ammonium ions of this type may be prepared by protonating or alkylating the corresponding amine oxide, R1R2R3N+O'. (f) quaternary ammonium ions of general formula: [(CH3)3N(CH2CH2O)XR1]+ wherein x is an integer of from 1 to 5, preferably 2 to 3 and R1 is a C1 to C30 alkyl group with the proviso that the -(CH2CH2O)xR1 substituent has at least 8 carbon atoms.
Quaternary ammonium salts of this class are derived from choline, [(CH3)3N(CH2CH2OH)]+.
(g) quaternary ammonium ions of general formula: [R1R2NCH2CH2NR3R4R5J+ wherein R1, R2, R3 and R4 are independently selected from methyl and ethyl; and R5 is a hydrocarbyl group selected from (i) C8 to C30 alkyl groups or (ii) -(CH2)nC6H4R' wherein n is an integer of from 0 to 5, R' is selected from the group consisting of H, Cl, Br, I, NO2, C1 to C30 alkyl groups (preferably C1 to C20 alkyl groups), -SO2R", -SOR" and -C(O)R" (wherein R" is a C1 to C30 alkyl group, preferably a C1 to C20 alkyl group) with the proviso that R5 has at least 8 carbon atoms.
Quaternary ammonium ions of this class may, for example, be prepared from tetramethylethylenediamine or tetraethylethylenediamine by reaction with R5X where X is a good leaving group, for example, a halide.
The cation may also comprise an aromatic or non-aromatic heterocyclic ring structure having at least one hydrophobic tail group, preferably a hydrocarbyl tail group as a substituent on the heterocyclic ring. It is envisaged that the heterocyclic ring may have from 1 to 3 hydrocarbyl substituents. Suitably, the heterocyclic ring structure of the cation is selected from imidazolium, imidazolinium, pyridinium, pyrazolium, thiazolium, isothiazolinium, azathiozolium, oxothiazolium, oxazinium, oxazolium, oxaborolium, dithiozolium, trizdium, selenozolium, oxaphopholium, pyrollium, borolium, furanium,< thiophenium, phospholium, pentazolium, indolium, indolinium, oxazolium, isooxazolium, isotriazolium, tetrazolium, benzofuranium, diborzofuranium, benzothiophenium, dibenzothiophenium, thiadiazolium, pyrimidinium, pyrazinium, pyridazinium, piperazinium, piperidinium, morpholenium, pyranium, annolinium, phthalzinium, quinazolinium, quinaxalinium, quinolinium, isoquinolinium, thazinium, oxazinium, and azaannulenium. Preferably, the heterocyclic ring structure has at least one N heteroatom, and optionally an O heteroatom.
Preferred heterocyclic cations include: (a) non-aromatic heterocycles such as:
Figure imgf000006_0001
wherein M is N or P;
R1 is C8 to C30 alkyl group; and R2 is selected from methyl, ethyl or a C8 to C30 alkyl group. Where R1 and R2 are both C8 to C30 alkyl groups, it is preferred that R1 and R2 are of different length, for example, R1 may be a C8 to C12 alkyl group and R2 a C16 to C30 alkyl group, (b) Imidazolium ions of the general formula:
Figure imgf000007_0001
wherein R1 is a C8 to C30 alkyl group, preferably a C12 to C28 alkyl group, for example, a C16 to C24 alkyl group;
R2 is selected from H, methyl and ethyl, preferably H; R3 is selected from methyl, ethyl and C8 to C30 alkyl groups, preferably, methyl or ethyl; and
R4 and R5 are H or a halide (for example, Cl or Br). (c) pyridinium ions of the general formula:
Figure imgf000007_0002
wherein R1 is hydrophobic substituent selected from (i) C8 to C30 alkyl groups
(preferably, C12 to C20 alkyl groups) and (ii) -(CHb)nCeH4R' wherein n is an integer of from 0 to 5, R' is selected from the group consisting of H, Cl5 Br, I, NO2, C1 to C30 alkyl groups (preferably C1 to C20 alkyl groups), -SO2R", -SOR" and -C(O)R" (wherein R" is a C1 to C30 alkyl group, preferably a C1 to C20 alkyl group) with the proviso that - (CH2)J1C6H4R' contains at least 8 carbon atoms; and
R2 and R3 are independently selected from H and dimethylamino, or are R1 groups. Particularly preferred pyridinium ions of this class include dodecylpyridinium, 1,4- didodecylpyridinium, hexadecylpyridinium, 1,4-dihexadecylpyridinium, octadecylpyrinidium, 1 ,4-octadecylpyridinium, 4-(dimethylamino)dodecylpyridinium, 2-(dimethylamino)dodecylpyridinium, 4-(dimethylamino)hexadecylpyridinium and 2- (dimethylamino)hexadecylpyridmium. Where the pyridinium ion has a dimethylamino substituent in the 2- or 4- position, the pyridinium ion may be prepared from 4- dimethylaminopyridine or 2-dimethylaminopyridine respectively, (d) an oxazole of general formulae:
Figure imgf000008_0001
wherein R1 is a hydrocarbyl substituent selected from (i) C8 to C30 alkyl groups (preferably C12 to C28 alkyl groups) and (ii) -(CH2)nC6H4R' wherein n is an integer from
0 to 5, R' is selected from the group consisting of H, Cl, Br, I, NO2, C6 to C30 alkyl groups (preferably C1 to C20 alkyl groups), -SO2R", -SOR" and -C(O)R" (wherein R" is a C1 to C30 alkyl group, preferably a C1 to C20 alkyl group) with the proviso that -
(CH2)nC6H4R' contains at least 8 carbon atoms; and R and R3 are independently selected from H, methyl or ethyl.
(e) derivatives of l,5-diazabicyclonon-5-ene (DBN) and l,9-diazabicycloundec-7-ene
(DBU) of general formulae:
Figure imgf000009_0001
wherein R is a hydrocarbyl substituent selected from (i) Cg to C30 alkyl groups and (ii) - (CH2)nC6H4R' wherein n is an integer from 0 to 5, R' is selected from the group consisting of H, Cl, Br, I, NO2, C1 to C30 alkyl groups (preferably C1 to C20 alkyl groups), -SO2R' ' , -SOR' ' and -C(O)R' ' (wherein R" is a C1 to C30 alkyl group, preferably a Ci to C20 alkyl group) with the proviso that -(CH2)HC6H4R' contains at least 8 carbon atoms.
Preferably, the anion, A", is selected from the group consisting of: (a) dialkyl phosphase anions of the general formula: [R1R2P(O)O]- wherein R1 and R2 are independently selected from C8 to C30, preferably C12 to C18, alkyl groups. The alkyl groups may be branched or unbranched. Particularly preferred alkyl groups include dodecyl, hexadecyl, octadecyl, and 2,4,4-trimethylpentyl. A commercially available example of a dialkyl phosphase anion of general formula (II) is Cyanex-272™ (2,4,4-trimethylpentyl phosphase) :
Figure imgf000009_0002
(b) phosphates of general formula: [(R1O)(R2O)P(O)O]- wherein R1 and R2 are independently selected from C8 to C30 alkyl groups, preferably, C12 to C18 alkyl groups. The alkyl groups may be branched or unbranched.
(c) phosphoric acid esters of general formulae:
[R(OCH2CH2)xOP(O)(O)2f [(R(OCH2CHa)xO)2P(O)O]- wherein x is an integer of from 4 to 15 and R is an alkyl group, preferably, methyl or ethyl.
(d) alkyl sulfate anions of general formula:
ROSO3 ' wherein R is a straight chain or branched chain alkyl group having at least 8 carbon atoms, preferably, a C8 to C30 alkyl group, more preferably a C12 to C24 alkyl group, for example, a Ci6 to C20 alkyl group. Examples of alkyl sulfate anions include dodecyl sulfate, hexadecyl sulfate and octadecyl sulfate.
(e) sulfated polyoxyethylene (POE) straight chain alcohols of general formula: R(OCH2CH2)XSO4- wherein R is a C8 to C30 alkyl group and x is an integer in the range 1 to 10, preferably, 2 to 5.
(f) alkyl sulfonate anions of general formula:
RSO3- wherein R is a straight chain or branched chain alkyl group having at least 8 carbon atoms, preferably, a C8 to C30 alkyl group, more preferably a C12 to C24 alkyl group, for example, a C16 to C2o alkyl group. Examples of alkyl sulfonate anions include dodecanesulfonate and hexadecanesulfonate.
(g) alkylbenzylsulfonates of general formula: RC6H4SO3 " where R is a C2 to C30 alkyl group, preferably, a Cg to Ci5 alkyl group. The alkyl group may be in the 2-, 3-, or 4- position on the phenyl ring, preferably, the 4-position. The alkyl group may be branched or unbranched. Preferably, the alkyl group is - CH(CH3)(CH2)nCH3 where n is an integer in the range 9 to 12. Preferred alkylbenzyl sulfonates include dodecylbenzenesulfonate, hexadecylbenzenesulfonate and octadecylbenzenesulfonate. (h) N-acyl-n-alkyltaurates of general formula:
RC(O)N(R')CH2CH2SO3 " wherein R is a straight chain or branched chain C4 to C30 alkyl group, and R' is methyl or ethyl.
(i) isethionates of general formula
RCOOCH2CH2SO3- wherein R is a straight chain or branched chain C5 to C30 alkyl group. G) sulfonic acid esters of general formula:
ROSO3 ' wherein R is a straight chain or branched chain C8 to C30 alkyl group, (k) sulfosuccinate esters of general formula: R1OOCCH2CH(SO3OCOOR2 wherein R1 and R2 are straight chain or branched chain C5 to C30 alkyl groups. (1) arylalkanesulfonates of general formula:
R(CH2)mCH(C6H4R1)(CH2)nSO3- wherein m and n are integers in the range 1 to 10; R is H or a C1 to C30 alkyl group; and
R1 is selected from the group consisting of H5 Cl, Br, I, NO2, C1 to C30 alkyl groups (preferably a C1 to C20 alkyl group), -SO2R', -SOR' and -C(O)R' (wherein R' is a C1 to C30 alkyl group, preferably a Ci to C20 alkyl group. Such sulfonates are prepared by sulfonating an olefin and then treating the intermediate product with an aromatic compound.
(m) alkyldiphenylether(di)sulfonates of general formula:
RC6H3(SO3OOC6H4SO3 " wherein R is a C1 to C30 alkyl group. Such alkyldiphenylether(di)sulfonates are prepared by alkylating diphenyl ether and then sulfonating the reaction product. (n) carboxylate anions of general formula:
RC(O)O" wherein R is a straight chain or branched chain C7 to C30 alkyl or alkenyl group. For example, the carboxylate may be CH3(CHa)10CO2 " (laurate), CH3(CH2)12CO2" (myristate), CH3(CH2)Ii6CO2 " (stearate), CH3(CH2)18CO2 " (arachidate), CH3(CH2)5CH=CH(CH2)7CO2 " (palmitoleate), CH3(CH2)7CH=CH(CH2)7CO2 " (oleate), CH3(CH2)4CH=CHCH2CH=CH(CH2)7CO2 " (linoleate), CH3CH2CH=CHCH2CH=CHCH2CH=CH(CH2)7CO2 " (linolenate), CH3(CH2)4(CH=CHCH2)4(CH2)22 " (arachidonate). (o) borate anions of general formula: [(RCH2CH2)SR1B]" wherein R is H or methyl and R1 is a straight chain or branched chain C8 to C30 alkyl group. Borate anions of this class may be prepared by reacting CH2=CHR (R is H or methyl) with BH3-Y (where Y forms a complex with BH3, for example, BH3.Y is a borane tetrahydrofuran complex) followed by reaction of the intermediate compound
(RCH2CH2)3B with R1ClTNa.
(p) borate anions of general formula:
ΓΛ
O O R1" R2
wherein R1 and R2 are straight chain or branched chain C8 to C30 alkyl groups.
The ionic liquid surfactant may also be a protonated ionic liquid formed by the following reaction:
Aπion-H + [Anion]"
Figure imgf000012_0001
wherein the cation and/or the anion has at least one hydrophobic tail group, for example, a C8 to C30 alkyl substituent.
Many of the salts described above are novel, and the invention provides per se all novel salts described herein. Specific groups of novel salts include, but are not limited to, the following. A salt of the general formula Ia:
C+ A" (Ia) the salt of general formula Ia existing in a liquid state at a temperature below 150°C; in which A" is an anion; and in which the cation, C+, comprises an imidazolium ion of the general formula:
Figure imgf000013_0001
wherein R1 is a C16 to C30 alkyl group; R2 is selected from H, methyl and ethyl; R3 is selected from methyl, ethyl and C8 to C30 alkyl groups; and R4 and R5 are H, or halogen.
A salt of the general formula Ib:
C+ A" (Ib) the salt of general formula Ib existing in a liquid state at a temperature below 150°C; in which A" is an anion; and in which the cation, C+, comprises a pyridinium ion of the general formula:
Figure imgf000013_0002
wherein R1 is a C8 to C30 alkyl group; and
R2 and R3 are independently selected from (i) H; (ii) dimethylamino; (iii) C8 to C30 alkyl groups; and (iv) -(CH2)HC6H4R' wherein n is an integer of from 0 to 5, R' is selected from the group consisting of H, Cl, Br, I, NO2, C1 to C30 alkyl groups, -SO2R", -SOR" and -C(O)R" (wherein R" is a C1 to C30 alkyl group) with the proviso that -(CH2)HC6H4R' contains at least 8 carbon atoms. A salt of the general formula Ic: C+ A" (Ic)
the salt of general formula Ic existing in a liquid state at a temperature below 150°C; in which A" is an anion; and in which the cation, C+, is selected from one of the quaternary ammonium or phosphonium groups (a) to (g) defined above. A salt of the general formula Id:
C+ A" (Id)
the salt of general formula Id existing in a liquid state at a temperature below 150°C; in which A' is an anion; and in which the cation, C+, is selected from one of the heterocyclic groups (a), (d) and (e) defined above A salt of the general formula Ie:
C+ A' (Ie)
the salt of general formula Ie existing in a liquid state at a temperature below 150°C; in which A" is an anion of the general formula:
[R1R2P(O)O]" wherein R1 and R2 are independently selected from C8 to C30 alkyl groups; and in which the cation, C+, is an imidazolium ion of the general formula:
Figure imgf000014_0001
wherein R1 is an alkyl group having up to 15 carbon atoms; R2 is selected from H5 methyl and ethyl; R3 is selected from methyl, ethyl and C8 to C30 alkyl groups; and R4 and R5 are H or halogen. The ionic liquid surfactants (emulsifiers) of the present. invention may be classified using the hydrophilic-lipophilic balance (HLB) system that employs a scale of 0 to 20 based on the affinity of the surfactants for oil or water. Surfactants with low HLB values are more lipophilic while surfactants with higher HLB values are more hydrophilic. The HLB values of the ionic liquid surfactants may be determined empirically by comparison with conventional surfactants of predetermined HLB value.
In general, ionic liquid surfactants will have the following properties or functions based on their HLB values:
1-3 antifoaming properties 3-8 water in oil emulsification
7-9 wetting properties
9-18 oil in water emulsification
15-20 solubilizing properties.
In particular, surfactants with HLB values of 3 to 8 are more oil soluble and will form water in oil emulsions while surfactants having an HLB value of greater than 9, preferably, 9 to 18, are more water soluble and will form oil in water emulsions.
In one of its aspects, the present invention provides a water in oil or oil in water emulsion which comprises (i) an oil phase, (ii) an aqueous phase and (iii) an ionic liquid surfactant wherein the ionic liquid surfactant is a salt of general formula I: C+ A' (I) the salt of general formula I existing in a liquid state at a temperature below 150°C; at least one of the cation, C+, and anion, A', comprising a hydrophobic tail group attached to an ionic head group; and A" represents an anion containing phosphorus, or an alkyl sulfate anion of general formula: ROSO3 " wherein R is an alkyl group having at least 8 carbon atoms.
Preferred salts for use in this aspect of the invention are given above. Particularly preferred salts are those in which the anion A' is selected from the groups (a), (b) and (c), especially (a), given above. In a further aspect, the present invention provides a water in oil or oil in water emulsion which comprises (i) an oil phase, (ii) an aqueous phase and (iii) a novel ionic liquid surfactant as defined above. An emulsion of the invention may be a microemulsion. An advantage of the microemulsion of the present invention is that it has a low interfacial tension of less than 1 mNm'1.
As discussed above, depending upon the HLB value of the ionic liquid surfactant, the microemulsion may be an oil in water microemulsion where the oil is dispersed in a continuous aqueous phase or a water in oil microemulsion where the water is dispersed in a continuous oil phase. Preferably, the microemulsion in a water in oil microemulsion. The water in oil microemulsion of the present invention may be used for deploying water soluble or water dispersible oil field or gas field production chemicals as described in International Patent Application No. WO 0100747 or in enhanced oil recovery.
Microemulsions in general are known, see, for example "Microemulsions", Editor I D Robb, Plenum Press, New York, 1982 which is herein incorporated by reference. Microemulsions differ from conventional emulsions in that they form spontaneously upon mixing of the oil phase, aqueous phase and the surfactant. They also differ from ordinary emulsions in having droplets of very small size or in having microdomains having at least one dimension of length, breadth or thickness of very small size. Thus, microemulsions appear clear to the naked eye or even the optical microscope, compared to the larger droplets (greater than 100 nm diameter) of conventional cloudy emulsions.
Suitably, the aqueous phase of the water in oil microemulsion is distributed in a continuous oil phase in the form of droplets having a diameter in the range 1 to 100 nm or in the form of microdomains having at least one dimension of length, breadth or thickness in the range 1 to 100 nm. Where the aqueous phase of the water in oil microemulsion is distributed in the oil phase in the form of droplets, the droplets preferably have an average diameter in the range of 10 to 500 nm, more preferably 50 to 250 nm. The droplet size distribution is generally such that at least 90% of the diameters are within 20% or especially 10% of the average diameter. The microemulsions are transparent to the eye and are apparently isotropic.
Where the aqueous phase of the water in oil microemulsion is distributed in the oil phase in the form of microdomains, the microdomains preferably have at least one dimension of length, breadth or thickness in the range 10 to 500 ran, more preferably 50 to 250 nni.
The oil phase is essentially any liquid which is immiscible with the aqueous phase. For example the oil phase may be selected from the group consisting of liquid alkanes (preferably C5-C20 alkanes, more preferably C8 to C15 alkanes, most preferably C9-C12 alkanes, for example, n-hexane, n-nonane, n-decane, and n-undecane), alkenes, liquid alkyl halides (for example, carbon tetrachloride or dichloromethane) and liquid aromatic hydrocarbons (for example, benzene, toluene and xylene). The oil phase may also be a paraffin oil, a natural oil (for example, a vegetable or animal oil), diesel, kerosene, gas oil, crude oil, lubricant base oil, liquid carbon dioxide, liquid chlorofluorocarbons such as CCIiF2, CHCl2F and CH3CClF2 (known as freons), tetrahydrofuran, dimethyl formamide and dimethyl sulfoxide.
The aqueous phase may additionally comprise a water miscible solvent such as methanol, ethanol, n-propanol, iso-propanol, n-butanol, iso-butanol, tert-butanol, butyl monoglycol ether, butyl diglycol ether, butyl triglycol ether, ethylene glycol mono butyl ether and ethylene glycol. Without wishing to be bound by any theory, it is believed that the presence of a water miscible solvent in the aqueous phase stabilizes the microemulsion so that less ionic liquid surfactant is required to form a stable microemulsion. The amount of water miscible solvent which may be present in the aqueous phase is in the range 0.5 to 50 % by weight, preferably 5 to 30 % by weight based on the total weight of water and water miscible solvent. However, an advantage of the ionic liquid surfactant of the present invention is that the microemulsion is stable even in the absence of a water miscible solvent.
Generally, a salt such as sodium chloride or magnesium sulfate is added to the aqueous phase of a conventional microemulsion in order to enhance the stability of the microemulsion. Thus, the aqueous phase of a conventional microemulsion is generally saturated with the salt. However, a further advantage of the microemulsion of the present invention is that there is no requirement to add a salt to stabilize the emulsion. However, if deemed desirable, a salt may be included in the aqueous phase of the emulsion.
The volume fraction of the aqueous phase in the microemulsion is generally in the range from 1-50%, preferably 10 to 40%, more preferably 23 to 30%. The ionic liquid surfactant is suitably present in the microemulsion in an amount ranging from 0.1 to 5 mole %, preferably 0.25 to 2 mole %, for example 0.5 to 1 mole %.
Where the water in oil microemulsion of the present invention is used to deploy a water-soluble or water-dispersible production chemical, the aqueous phase of the microemulsion may comprise fresh, tap, river, sea, produced or formation water. The aqueous phase may have a total salinity of 0-250 g/1, for example 5-50 g/1. The aqueous phase may have a pH of 0.5-9. Where the aqueous phase comprises a sea-water solution of a highly acidic production chemical such as, for example, a scale inhibitor, the aqueous phase usually has a highly acidic pH of 0.1 - 1. In such cases it may be necessary to neutralise the acidity of the aqueous phase by using ammonium hydroxide or an alkali metal hydroxide, especially sodium hydroxide, potassium hydroxide or lithium hydroxide, in order to bring the pH of the formulation to within a preferred range of from 2-6. Preferably, the aqueous phase is neutralized prior to being mixed with the organic phase and surfactant to form the microemulsion.
Preferably, both the cation and the anion of the ionic liquid surfactant that is used to form the microemulsion have at least one hydrocarbyl tail group. Suitably, the cation of the ionic liquid surfactant has at least one hydrophobic tail group having a chain length of at least 16 carbon atoms, preferably 18 to 30 carbon atoms while the anion of the ionic liquid surfactant has at least one hydrophobic tail group having a chain length of 8 to 12 carbon atoms, preferably 8 to 10 carbon atoms. Alternatively, the anion of the ionic liquid may have at least one hydrophobic tail group having a chain length of at least 16 carbon atoms, preferably 18 to 30 carbon atoms while the cation has at least one hydrocarbyl tail group having a chain length of 8 to 12 carbon atoms, more preferably, 8 to 10 carbon atoms. Without wishing to be bound by any theory it is believed that where the cation and anion have hydrophobic tail groups that are of different length that this increases the stability of the microemulsion by enhancing the packing of the surfactant in the interfacial film. Mixtures of ionic liquid surfactants may be employed to prepare the microemulsion, for example, 2 or 3 ionic liquid surfactants.
It is important that the microemulsion is thermally stable. It is possible to devise microemulsions which are stable over a wide temperature range e.g. from ambient to 3000C or from 90 to about 150°C. However, it is not essential that the microemulsion is stable across the whole of the range of from ambient to 150°C. For example, the microemulsion may be stable between ambient and 70°C or between 40 and 80°C. The microemulsion of the present invention forms spontaneously on gentle mixing of the aqueous phase, the oil phase and the ionic liquid surfactant in any order; conveniently, the aqueous phase is mixed last into a mixture of the oil phase and the ionic liquid surfactant. If the material made is initially cloudy, then a microemulsion has not been produced, and minor adjustments to the relative proportions of the ingredients or a change in the nature of the ionic liquid surfactant or the temperature may be needed. The microemulsion can be characterized by x-ray diffraction to show the presence of the droplets or domains.
It is also envisaged that the ionic liquid surfactants may be used to form conventional emulsions, in which, for example, the internal phase of the emulsion is distributed in a continuous external phase in the form of droplets having a diameter in the range 0.01 to about 100 microns. Conventional emulsions differ from microemulsions in that it is necessary to input energy to form the emulsion. In principle, a microemulsion and a conventional emulsion may coexist.
The conventional emulsion may be an oil in water emulsion where an internal oil phase in dispersed in the form of droplets in a continuous external aqueous phase or a water in oil emulsion where an internal aqueous phase is dispersed in the form of droplets in a continuous external oil phase. As discussed above, the type of conventional emulsion is dependent upon the nature of the ionic liquid surfactant (emulsifier).
Preferably, the ionic liquid surfactant that is employed to generate the emulsion is comprised of a cation, C+, having at least one hydrophobic tail group attached to a cationic head group and an anion, A", having at least one hydrophobic tail group attached to an anionic head group.
Mixtures of ionic liquid surfactants may be employed to prepare the conventional emulsion of the present invention, for example, 2 or 3 ionic liquid surfactants.
Where the ionic liquid surfactant has an HLB value of 3 to 8 and the surfactant is oil soluble, a water in oil emulsion may be formed by dissolving minor amounts of the oil soluble ionic liquid surfactant in the oil that is to form the continuous oil phase of the emulsion. The concentration of oil-soluble ionic liquid surfactant in the resulting solution may be in the range of from 0.1 to 5 mole %, preferably 0.25 to 2 mole %, most preferably 0.5 to 1 mole %. The emulsion is preferably formed by pouring the aqueous phase into the solution of the oil-soluble ionic liquid surfactant in the oil phase while intensive blending is applied (thereby imparting energy to form the emulsion). The blending operation for the emulsion should be designed to minimize the size of the internal phase water droplets since this may increase the stability of the emulsion. The mixture should be vigorously stirred or sheared for about 5 to 20 minutes, the rate of shear being highly dependent on the size and type of mixing device employed. Stirring rate and times should be designed to form small aqueous droplets, preferably having average diameters of from about 0.3 to about 100 microns and preferably from about 1 to about 10 microns.
Preferably, the internal phase of the emulsion should amount to from 10 to 70 percent, more preferably from 30 to 60 percent of the total volume of the emulsion. Density control of the water in oil emulsion may be used to enhance its stability.
This may be accomplished by addition of weighting agents to the internal aqueous phase of the emulsion. For example, minor amounts of soluble salts such as sodium or potassium chloride may be added to the internal aqueous phase. Suitably, the aqueous phase may comprise from 0.5 to 20 percent by weight of soluble salts. Where the ionic liquid surfactant has an HLB value of greater than 9, preferably.
9 to 18, and is water soluble, an oil in water emulsion may be formed by dissolving minor amounts of the water soluble ionic liquid surfactant in the aqueous phase. The concentration of water-soluble ionic liquid surfactant in the resulting solution may be in the range of from 0.1 to 5 mole%, preferably 0.25. to 2 mole%. The emulsion is preferably formed by pouring the oil phase into the solution of the water-soluble ionic liquid surfactant in the aqueous phase while intensive blending is applied, as described above for the preparation of a water in oil emulsion. The blending operation for the emulsion should be designed to minimize the size of the internal phase oil droplets since this may increase the stability of the emulsion. Stirring rate and times should be designed to form small oil droplets having average diameters of from about 0.3 to about 100 microns and preferably from about 1 to about 10 microns.
Preferably, the internal oil of the emulsion should amount to from 1 to 80 percent, more preferably from 5 to 50 percent of the total volume of the emulsion. Suitably, the water in oil emulsion may be used to deploy a water-soluble or water-dispersible production chemical, as described above for a water in oil microemulsion. The conventional emulsion may also act as the base fluid of a wellbore fluid, for example, a drilling fluid or completion fluid. An advantage of the conventional emulsion is that the use of the ionic liquid surfactant renders the emulsion more stable under high temperature and/or high pressure conditions than emulsions formed using conventional emulsifiers. The emulsions are also more tolerant of metal ions and are less likely to form scums.
The ionic liquid surfactants of the present invention have many other applications including their use:
1) to prepare foam compositions, for example, for mobility control in gas and/or gas condensate reservoirs where the foam is used to block a high permeability zone and to divert a gas into a low permeability zone. Examples of suitable foaming agents include l-octadecyl-3-methylimidazolium bis(2,4,4- trimethylpentyl)phosphate and 1-octadecylpyridinium bis(2,4,4- trimethylpentyl)phosphate .
2) as cleaning agents or degreasers (where the ionic liquid surfactant acts as an emulsifier or a wetting agent).
3) in personal hygiene products (where the ionic liquid surfactant acts as an emulsifier or a wetting agent).
4) as hydrophobic solvents, particularly, terpene free hydrophobic solvents
5) as a component of drilling fluids, for example, the ionic liquid surfactant may act as a heat transfer agent (to transfer heat from the drill bit), as a lubricant for the drill bit, as a weighting agent or as a fluid loss control agent. 6) as additives during oil production, for example, the surfactant may act as a gas hydrate inhibitor, corrosion inhibitor or drag reducer.
7) as additives during water flooding operations (enhanced oil recovery from oil wells)
8) as lubricants or lubricant additives 9) as hydraulic fluids or hydraulic fluid additives
10) for dispersion of oil spillages
11) as liquid media for chemical reactions (for example, micellar catalysis).
12) as phase transfer agents. 13) designer microemulsion compositions.
14) mechanical fluids such as milling or cutting fluids.
15) drug delivery agents.
The invention therefore further provides the use of a salt as defined above in the above applications. In one such embodiment, the invention provides a composition in the form of a foam, which comprises, as a foaming agent, a salt as defined above, especially a composition suitable for use in a gas and/or gas condensate reservoir.
The present invention is illustrated by the following Examples. Example 1 Preparation of l-octadecyl-3-methylimidazolium bis(2A4-1ximethyrpentyl)phosphonate rCismimirfisoCgbPCM
Bis(2,4,4-trimethylpentyl)phosphonic acid (Cyanex-272), (2.90 g, 10 mmol) and 1- octadecyl-3-methylimidazolium (3.54 g, 10 mmol) chloride were separately dissolved in 20 cm3 of deionized water. The two solutions were mixed and sodium hydroxide (0.40 g, 10 mmol) was added. The resulting mixture was heated to a temperature of 80 °C and was then cooled to give two phases. The upper "hydrophobic" ionic liquid phase was separated and dried under vacuum to give a viscous oil: [C18mim][(isoCs)2PO2]; mp determined by differential scanning calorimetry (DSC) = -26°C, 9.0 Jg'1. Example 2 Preparation of [Cismim] F(JSo-CsHn)2PO?! / water / hexane microemulsion
Water (40 g), hexane (50 g) and [C18mim][(iso-C8)2PO2] (5 g) were mixed in a conical flask. Three phases spontaneously formed on mixing: a lower aqueous phase, a middle microemulsion phase and an upper hexane phase. The estimated volumes of these phases are as follows: Upper 20ml (hexane)
Middle 50ml (water in oil microemulsion)
Lower 35ml (water).
The compositions of the three phases were determined by NMR analysis (solvent = methanol-d4). Composition (values in mol% rounded to the nearest 1%): Upper 100% Hexane
Middle 60% water, 39% hexane, 1% [C18mim][(/-octyl)2P02]
Bottom 99% water, 1 % hexane, 17 ppm [C18mim] [(/-octyl)2PO2] Composition (weight %): Upper 100% Hexane
Middle 22% water, 69% hexane, 9% [Cigmim] [(/-octyl)2PO2]
Lower 96% water, 4% hexane, 0.05 % [Cigmim] [(f-octyl)2PO2] Example 3
Preparation of l-dodecyl-3-methylirnidazolium bis(2,4,4-trimethylpentyl)phosphonate rCijmimir(iso-Cj> Hn)2PO2I
An aqueous solution of potassium bis(2,4,4-trimethylpentyl)phosphinate (0.4 M) was derived from KOH and bis(2,4,4-trimethylpentyl)phosphonic acid (Cyanex 272™). 1- dodecyl-3-methylimidazolium chloride (3.54 g, 10 mmol) was separately dissolved in 20 cm3 of deionised water and the resulting solution was mixed with 25 cm3 of the aqueous solution of potassium bis(2,4,4-trimethylpentyl)phosphonate. The resulting mixture was stirred for 2 hours, then the ionic liquid product was extracted with ethyl acetate. The ethyl acetate was removed on a rotary evaporator and the product dried under vacuum to give a viscous oil: [C12mim][(iso-C8 Hn)2PO2]; mp (glass transition) (DSC) = -47.3 0Q M Jg"1. Example 4
Preparation of l-decyl-3-methylimidazolium bisC2,4,4-trimethylpentyl)ρhosphonate rCmmimirfiso-Cs Hn)2PO2] Potassium bis(2,4,4-trimethylpentyl)phosphonate (derived from KOH and Cyanex-272), (25. ml of 0.4 M solution in water, 10 mmol) and a solution of l-decyl-3- methylimidazolium (2.58 g, 10 mmol) chloride in 20 cm3 of deionised water were mixed together. The resulting mixture was stirred for 2 hours, then the product was extracted with ethyl acetate. The ethyl acetate was removed on a rotary evaporator and the product dried under vacuum to give a viscous oil: [C10mim][(iso-C8H17)2PO2] mp (glass transition) (DSC) = -46.1 0C, 1.3 Jg'1. Example 5
Preparation of a FCHJmJm][CiSo-CsHnI2PO2] / water / hexane microemulsion Water (10 ml), hexane (10 ml) and [C1OmIm][OsO-C8Hn)2PO2] (0.5 g) were mixed together in a 25 ml measuring cylinder. Three phases were observed to separate on standing and were visualised by the addition of rhodamine B dye {pa. 1 microgram). The phases were a lower aqueous phase, a middle microemulsion phase and an upper hexane phase. Example 6
Preparation of l-heptyl-3-methylimidazolium bisf2A4-trimethylpentyl)phosphonate rc7miml rfiso-CaHifbPOil
Potassium bis(2,4,4-trimethylpentyl)phosphonate (derived from KOH and Cyanex-272), (16.36 ml of 0.4 M solution in water) and a solution of 1 -heptyl-3-methylimidazolium chloride (1.42 g, 6.56 mmol) in 20 cm3 of deionised water were mixed together. The resulting mixture was stirred for 2 hours, then the product was extracted with ethyl acetate. The ethyl acetate was removed on a rotary evaporator and the product dried under vacuum to give a viscous oil: [C7mim][(iso-C8)2PO2]. Example 7
Preparation of l-butyl-3-methylimidazolium bis(2A4-trimethylpentyl)phosphonate rC4mimir(iso-CsHif)zPOz1
Potassium bis(2,4,4-trimethylpentyl)phosphonate (derived from KOH and Cyanex-272),
(11.88 ml of 0.4 M solution in water) and a solution of l-butyl-3-methylimidazolium (0.83 g, 4.75 mmol) chloride in 20 cm3 of deionised water were mixed together. The resulting mixture was stirred for 2 hours, then the product was extracted with ethyl acetate. The ethyl acetate.was removed on a rotary evaporator and the product dried under vacuum to give a waxy solid: [C4inim][(iso-C8H17)2PO2].
Example 8 Preparation of l-octadecyl-3-methylimidazolium dodecylsulfate
Figure imgf000024_0001
Sodium octadecylsulfate (1.20 g, 4.20 mmol) and l-octadecyl-3-methylimidazolium chloride (1.55 g, 4.20 mmol) were separately dissolved in 20 cm3 of deionised water.
The two solutions were mixed together and stirred for 2 hours before being cooled to a temperature of 0 0C. A white precipitate was formed on cooling and was separated by filtration and dried under vacuum to give [C1SmIm][C12H25SO4]; nip (DSC) = 81.3 °C
(solid to liquid crystal), 83 Jg"1, and 148.0 0C, 2.8 Jg"1.
Example 9
Preparation of l-dodecyl-3-methylimidazolium dodecylsulfate [Cnmim] [Ci2H21SO4]
Sodium dodecylsulfate (1.05 g, 3.65 mmol) and l-dodecyl-3-methylimidazolium (1.05 g, 3.65 mmol) chloride were separately dissolved in 20 cm3 of deionised water and the solutions were then mixed together. The resulting mixture was stirred for 2 hours before being extracted with ethyl acetate. The ethyl acetate was removed on a rotary evaporator and the product dried under vacuum to give [C12mim] [C12H25SO4]; mp (DSC) = 239 °C (decomposes slowly), 15.7 Jg'1. Example 10 Preparation of l-heptyl-3-methylimidazolium dodecylsulfate [CTmJmIrCi2H2SSO4]
Sodium dodecylsulfate (1.85 g, 6.40 mmol) and l-heptyl-3-methylimidazolium (1.39 g, 6.40 mmol) chloride were separately dissolved in 20 cm3 of deionised water and the solutions were then mixed together. The resulting mixture was stirred for 2 hours before being extracted with ethyl acetate. The ethyl acetate was removed on a rotary evaporator and the product dried under vacuum to give [C7mim] [C12H25SO4] as a waxy solid.
Example 11 Preparation of l-butyl-3-methylimidazolium dodecylsulfate
Figure imgf000025_0001
Sodium dodecylsulfate (1.70 g, 5.90 mmol) and l-butyl-3-methylimidazolium chloride (1.03 g, 5.90 mmol) were separately dissolved in 20 cm3 of deionised water and the solutions were then mixed together. The resulting mixture was stirred for 2 hours before being extracted with ethyl acetate. The ethyl acetate was removed on a rotary evaporator and the product dried under vacuum to give [C4mim] [C12H25SO4] as a waxy solid.
Example 12
Preparation of 1-octadecylpyridinium bis(2A4-trimethyrpentyr)phosphonate rCisPvirfiso-CR HIf)2PO2] Potassium bis(2,4,4-trimethylpentyl)phosphonate (derived from KOH and Cyanex-272), (25 ml of 0.4 M solution in water, 10 mmol) and a solution of 1-octadecylpyridinium bromide (2.58 g, 10 mmol) in 20 cm3 of deionised water were mixed together. The resulting mixture was stirred for 2 hours, then the product was extracted with ethyl acetate. The ethyl acetate was removed on a rotary evaporator and the product dried under vacuum to give a paste: [Cispy] [(1So-CsHn)2PO2]. Example 13 Preparation of ionic liquid - water — hexane microemulsions Water (10 cm ), hexane (10 cm ) and ionic liquid (0.5 g) were mixed together in a 25 ml measuring cylinder. Three phases were observed and visualised by the addition of rhodamine B dye (ca. 1 microgram), with a lower aqueous phase, a middle microemulsion phase and an upper hexane phase. It was found that the volume of the middle microemulsion phase was dependent upon the structure of the ionic liquid surfactant.
Volume of middle microemulsion phase (rounded to the nearest 0.5 ml) [C18mim] [(Z-OCt)2 PO2] (0.5 g) 5.5 ml
[Ci8py][0-oct)2 PO2] (0.5 g) 3.5 ml
[Cionώn] Ki-OCt)2 PO2] (0.5 g) 3.5 ml
Example 14 1 -ethyl-3-methylimidazolium bisf2 A4-trimethylpentyl)phosphonate |"C2mim] [(iso-Cs Hn)2PO2I
Potassium bis(2,4,4-trimethylpentyl)phosphonate (derived from KOH and Cyanex-272), (25.0 g of 0.4 M solution in water) and a solution of l-ethyl-3-methylimidazolium bromide (2.38 g, 12.5 mmol) in 20 cm3 of deionised water were mixed together to form a hazy solution. Toluene (20 ml) was added and the solution was placed on a rotary evaporator to remove the toluene / water. This was repeated twice. More toluene was added (20 ml) to give 3 phases and the middle (microemulsion) and upper phases were separated and washed with distilled water (20 ml). The toluene and water were removed from the combined upper and middle phases and the resulting product was dried under vacuum to give a viscous oil: [C2mim][(iso-C8)2PO2]. Thus, [C2mim][(iso- C8H17)2PO2] forms a microemulsion when mixed with toluene/water but is soluble in water in the presence of hexane.

Claims

Claims
1. A water in oil or oil in water emulsion which comprises (i) an oil phase, (ii) an aqueous phase and (iii) an ionic liquid surfactant wherein the ionic liquid surfactant is a salt ofgeneral formula l:
C+ A" (D the salt of general formula I existing in a liquid state at a temperature below 150°C; at least one of the cation, C+, and anion, A", comprising a hydrophobic tail group attached to an ionic head group; and A- represents an anion containing phosphorus, or an alkyl sulfate anion of general formula:
ROSO3- wherein R is an alkyl group having at least 8 carbon atoms.
2. An emulsion as claimed in claim 1, in the form of a microemulsion having an interfacial tension of less than 1 rnNm"1.
3. An emulsion as claimed in either claim 1 or claim 2, in the form of a water in oil microemulsion in which the aqueous phase is distributed in a continuous oil phase in the form of droplets having a diameter in the range 1 to 100 nm or in the form of microdomains having at least one dimension of length, breadth or thickness in the range 1 to 100 nm.
4. An emulsion as claimed in claim 1, in which the internal phase of the emulsion is distributed in a continuous external phase in the form of droplets having a diameter in the range 0.01 to 100 microns.
5. An emulsion as claimed in any one of claims 1 to 4, in which the oil phase is selected from the group consisting of liquid alkanes, alkenes, liquid alkyl halides, liquid aromatic hydrocarbons, paraffin oils, vegetable or animal oils, diesel, kerosene, gas oil, crude oil, lubricant base oil, liquid carbon dioxide, liquid chlorofluorocarbons, tetrahydrofuran, dimethyl formamide and dimethyl sulfoxide.
6. An emulsion as claimed in any one of claims 1 to 5 in which the aqueous phase additionally comprises a water miscible solvent.
7. An emulsion as claimed in any one of claims 1 to 6, in which the cation, C+, comprises at least one hydrophobic tail group attached to a cationic head group and the anion, A', comprises at least one hydrophobic tail group attached to an anionic head group.
8. An emulsion as claimed in any one of claims 1 to 7, where the cation, C+, has 1 to 4 hydrophobic tail groups attached to a cationic head group.
9. An emulsion as claimed in any one of claims 1 to 8, where the anion, A", has 1 or 2 hydrophobic tail groups attached to an anionic head group.
10. An emulsion as claimed in any one of claims 1 to 9, in which the or each hydrophobic tail group present in the salt of the general formula I is a hydrocarbyl tail group optionally substituted by one or more groups selected from halogen atoms and alkoxy and hydroxyl groups, or is a poly(oxyethylene) group.
11. An emulsion as claimed in claim 10, in which the or each hydrophobic tail group present in the compound of the general formula I is an alkyl, alkenyl, alkynyl or alkaryl group having at least 8 carbon atoms, or a poly(oxyethylene) group -(CH2CH2O)xR (where R is H or methyl and x is an integer of from 4 to 15.
12. An emulsion as claimed in any one of claims 1 to 11, in which the cation C+ is selected from the group consisting of:
(a) quaternary ammonium or phosphonium ions of general formula: [R1R2R3R4M]+ wherein M is N or P; R1 and R2 are independently selected from methyl or ethyl groups;
R3 is a Cs to C30 alkyl group; and
R4 is selected from the group consisting of methyl, ethyl and a C8 to C30 alkyl group; (b) quaternary ammonium or phosphonium ions of general formula: [R1R2R3R4M]+ wherein M is N or P;
R1 and R2 are independently selected from methyl or ethyl groups; R3 is -(CH2)nC6H4R' wherein n is an integer of from 0 to 5; and
R' is selected from the group consisting of H, Cl, Br, I, NO2, C1 to C30 alkyl groups,
-SO2R", -SOR" and -C(O)R" (wherein R" is a C1 to C30 alkyl group), with the proviso that the R3 group has at least 8 carbon atoms; and
R4 is a Cg to C30 alkyl group or is an R3 group; (c) triethanolamine ester quaternary ammonium or phosphonium ions of general formula:
[(R2CO2CH2CH2)2M(RI)CH2CH2OH]+ wherein M is N or P;
R1 is methyl or ethyl; and R2 is a C5 to C30 alkyl group;
(d) quaternised polyoxyethylenated long-chain amines: [R1R2^(CH2CH2O)xH)2]-1- wherein R1 and R2 are independently selected from methyl and ethyl; and x is an integer of from 4 to 15; (e) quaternary ammonium ions of general formula: [R1R2R3NOR4J+ wherein R1 and R2 are independently selected from methyl and ethyl;
R3 is a Cg to C30 alkyl group; and
R4 is H or a C1 to C4 alkyl group; (f) quaternary ammonium ions of general formula: [(CHs)3N(CH2CH2O)xR1]- wherein x is,an integer of from 1 to 5 and R1 is a C1 to C30 alkyl group with the proviso that the -(CH2CH2O)xR1 substituent has at least 8 carbon atoms;
(g) quaternary ammonium ions of general formula: [R1R2NCH2CH2NR3R4R5]+ wherein R1, R2, R3 and R4 are independently selected from methyl and ethyl; and
R5 is a hydrocarbyl group selected from (i) Cg to C30 alkyl groups or (ii) -(CH2)HC6H4R' wherein n is an integer of from O to 5, R' is selected from the group consisting of H, Cl, Br, I5 NO2, C1 to C30 alkyl groups, -SO2R", -SOR" and -C(O)R" (wherein R" is a C1 to C30 alkyl group) with the proviso that R5 has at least 8 carbon atoms; (h) an aromatic or non-aromatic heterocyclic ring structure having at least one hydrophobic tail group, said heterocyclic ring being selected from imidazolium, imidazolinium, pyridinium, pyrazolium, thiazolium, isothiazolinium, azathiozolium, oxothiazolium, oxazinium, oxazolium, oxaborolium, dithiozolium, trizdium, selenozolium, oxaphopholium, pyrollium, borolium, furanium, thiophenium, phospholium, pentazolium, indolium, indolinium, oxazolium, isooxazolium, isotriazolium, tetrazolium, benzofuranium, diborzofuranium, benzothiophenium, dibenzothiophenium, thiadiazolium, pyrimidinium, pyrazinium, pyridazinium, piperazinium, piperidinium, moφholenium, pyranium, annolinium, phthalzinium, quinazolinium, quinaxalinium, quinolinium, isoquinolinium, thazinium, oxazinium, and azaannulenium.
13. An emulsion as claimed in claim 12, in which the cation C+ is selected from:
(aa) hexadecyltrimethylphosphonium, hexadecyltriethylphosphonium, octadecyltrimethylphosphonium, octadecyltriethylphosphonium, dihexadecyldimethylphosphonium, dioctadecyldimethylphosphonium hexadecyltrimethylammonium, hexadecyltriethylammonium, octadecyltrimethylammonium, octadecyltriethylammonium, dihexadecyldimethylammonium, and dioctadecyldimethylammonium;
(ha) a non-aromatic heterocycle having one of the following general formulae:
Figure imgf000030_0001
wherein M is N or P;
R1 is a C8 to C30 alkyl group; and
R is selected from methyl, ethyl or a C8 to C30 alkyl group;
(lib) Imidazolium ions of the general formula:
Figure imgf000031_0001
wherein R1 is a C8 to C30 alkyl group;
R2 is selected from H, methyl and ethyl;
R3 is selected from methyl, ethyl and C8 to C30 alkyl groups; and
R4 and R5 are H or halogen;
(he) pyridinium ions of the general formula:
Figure imgf000031_0002
wherein R1 is hydrophobic substituent selected from (i) C8 to C30 alkyl groups and (ii) -(CH2)HC6H4R' wherein n is an integer of from 0 to 5, R' is selected from the group consisting of H, Cl, Br5 1, NO2, C1 to C30 alkyl groups, -SO2R", -SOR" and -C(O)R" (wherein R" is a C1 to C30 alkyl group) with the proviso that -(CH2)HC6H4R' contains at least 8 carbon atoms; and
R2 and R3 are independently selected from H and dimethylamino, or are R1 groups; (hd) an oxazole of one of the general formulae:
Figure imgf000032_0001
wherein R1 is a hydrocarbyl substituent selected from (i) C8 to C30 alkyl groups and (ii)
-(CH2)nC6H4R' wherein n is an integer from 0 to 5, R' is selected from the group consisting of H, Cl, Br, I5 NO2, C6 to C30 alkyl group, -SO2R", -SOR" and -C(O)R"
(wherein R" is a C1 to C30 alkyl group) with the proviso that -(CH2)HC6H4R' contains at least 8 carbon atoms; and R2 and R3 are independently selected from H, methyl or ethyl;
(he) derivatives of l,5-diazabicyclonon-5-ene and l,9-diazabicycloundec-7-ene of one of the general formulae:
Figure imgf000032_0002
wherein R is a hydrocarbyl substituent selected from (i) C8 to C30 alkyl groups and (ii) -(CH2)nC6HL}R' wherein n is an integer from O to 5, R' is selected from the group consisting of H, Cl, Br, I, NO2, C1 to C30 alkyl groups, -SO2R", -SOR" and -C(O)R" (wherein R" is a C1 to C30 alkyl group) with the proviso that -(CH2)HC6H4R' contains at least 8 carbon atoms.
14. An emulsion as claimed in claim 13, in which the cation C+ is selected from an imidazolium ion of the general formula given in (hb) of claim 13 in which R1 is a C16 to C24 alkyl group; R2 is a hydrogen atom; R3 is selected from methyl and ethyl; and each of R4 and R5 is a hydrogen atom; or the cation C+ is dodecylpyridinium, 1,4- didodecylpyridinium, hexadecylpyridinium, 1 ,4-dihexadecylpyridinium, octadecylpyrinidiuni, 1 ,4-octadecylpyridinium, 4-(dimethylamino)dodecylpyridinium, 2-(dimethylamino)dodecylpyridinium, 4-(dimethylamino)hexadecylpyridiniuni or 2- (dimethylamino)hexadecylpyridinium.
15. An emulsion as claimed in any one of claims 1 to 14, in which in the salt of the general formula I, the anion, A", is selected from the group consisting of: (a) anions of the general formula:, [R1R2P(O)O]- wherein R and R are independently selected from C8 to C30 alkyl groups (b) anions of general formula:
[(R1O)(R2O)P(O)O]" wherein R1 and R2 are independently selected from C8 to C30 alkyl groups, (c) anions of one of the general formulae:
[R(OCH2CHz)xOP(O)(O)2]2- [(R(OCH2CH2)XO)2P(O)O]- wherein x is an integer of from 4 to 15 and R is an alkyl group.
16. An. emulsion as claimed in claim 15, in which the salt of the general formula
I is selected from: 1 -octadecyl-3-methylimidazolium bis(2,4,4-trimethylpentyl)phosphonate; l-dodecyl-3-methylimidazolium bis(2,4,4-trimethylpentyl)phosphonate;
1 -decyl-3 -methylimidazolium bis(2,4,4-trimethylpentyl)phosphonate; l-heptyl-3-methylimidazolium bis(2,4,4-trimethylpentyl)phosphonate; l-butyl-3-methylimidazolium bis(2,4,4-trimethylpentyl)phosphonate; 1-octadecylpyridinium bis(2,4,4-trimethylpentyl)phosphonate; l-ethyl-3-methylimidazolium bis(2,4,4-trimethylpentyl)phosphonate;
1 -octadecyl-3 -methylimidazolium dodecylsulfate;
1 -dodecyl-3 -methylimidazolium dodecylsulfate; l-heptyl-3 -methylimidazolium dodecylsulfate; and l-butyl-3 -methylimidazolium dodecylsulfate.
17. A method of making an emulsion as claimed in any one of claims 1 to 16, which comprises mixing together an aqueous liquid, an oil, and a salt of the general formula I as defined in any one of claims 1 and 7 to 16.
18. The use of a salt of the general formula I as defined in any one of claims 1 and 7 to 16 as a surfactant.
19. A salt of the general formula Ia:
C+ A" (Ia) the salt of general formula Ia existing in a liquid state at a temperature below 15O0C; in which A" is an anion; and in which the cation, C+, comprises an imidazolium ion of the general formula:
Figure imgf000034_0001
wherein R1 is a C16 to C30 alkyl group; R2 is selected from H, methyl and ethyl;
R3 is selected from methyl, ethyl and C8 to C30 alkyl groups; and R4 and R5 are H or halogen.
20. A salt as claimed in claim 19, in which R1 is a C16 to C24 alkyl group; R2 is a hydrogen atom; R3 is selected from methyl and ethyl; and each of R4 and R5 is a hydrogen atom.
21. A salt as claimed in claim 19, which is l-octadecyl-3-methylimidazolium bis(2,4,4-trimethylpentyl)phosphonate or 1 -octadecyl-3-methylimidazolium dodecylsulfate.
22. A salt of the general formula Ib: C+ A" (Ib) the salt of general formula Ib existing in a liquid state at a temperature below 150°C; in which A- is an anion; and in which the cation, C+, comprises a pyridinium ion of the general formula:
Figure imgf000035_0001
wherein R1 is a C8 to C30 alkyl group; and
R2 and R3 are independently selected from (i) H; (ii) dimethylamino; (iii) Cg to C30 alkyl groups; and (iv) -(CHi)nC6H4R' wherein n is an integer of from 0 to 5, R' is selected from the group consisting of H, Cl, Br, I, NO2, C1 to C30 alkyl groups, -SO2R", -SOR" and -C(O)R" (wherein R" is a Ci to C30 alkyl group) with the proviso that -(CH2)nC6H4R' contains at least 8 carbon atoms.
23. A salt as claimed in claim 22, in which the cation C+ is dodecylpyridinium, 1 ,4-didodecylpyridinium, hexadecylpyridinium, 1 ,4-dihexadecylpyridinium, octadecylpyrinidium, 1,4-octadecylpyridinium, 4-(dimethylamino)dodecylpyridinium, 2-(dimethylamino)dodecylpyridinium, 4-(dimethylamino)hexadecylpyridinium or 2- (dimethylamino)hexadecylpyridinium.
24. A salt as claimed in claim 22, which is 1-octadecylpyridinium bis(2,4,4- trimethylpentyl)phosphonate.
25. A salt of the general formula Ic:
C+ A" (Ic) the salt of general formula Ic existing in a liquid state at a temperature below 1500C; in which A" is an anion; and in which the cation, C+, is selected from the group consisting of:
(a) quaternary ammonium or phosphonium ions of general formula: [R1R2R3R4M]+ wherein M is N or P;
R1 and R2 are independently selected from methyl or ethyl groups;
R3 is a Cg to C30 alkyl group; and
R4 is selected from the group consisting of methyl, ethyl and a Cg to C30 alkyl group; (b) quaternary ammonium or phosphonium ions of general formula: [R1R2R3R4M]+ wherein M is N or P;
R1 and R2 are independently selected from methyl or ethyl groups;
R3 is -(CH2)DC6H4R' wherein n is an integer of from 0 to 5; and R' is selected from the group consisting of H, Cl, Br, I, NO2, C1 to C30 alkyl groups,
-SO2R", -SOR" and -C(O)R" (wherein R" is a C1 to C30 alkyl group), with the proviso that the R3 group has at least 8 carbon atoms; and
R is a Cg to C30 alkyl group or is an R3 group;
(c) triethanolamine ester quaternary ammonium or phosphonium ions of general formula:
[(R2CO2CH2CH2)2M(R1)CH2CH2OH]+ wherein M is N or P;
R1 is methyl or ethyl; and
R2 is a C5 to C30 alkyl group; (d) quaternised polyoxyethylenated long-chain amines: tR1R2N((CH2CH2O)xH)2]+ wherein R1 and R2 are independently selected from methyl and ethyl; and x is an integer of from 4 to 15;
(e) quaternary ammonium ions of general formula: [R1R2R3NOR4J+ wherein R1 and R2 are independently selected from methyl and ethyl;
R3 is a Cg to C3O alkyl group; and
R4 is H or a C1 to C4 alkyl group; (f) quaternary ammonium ions of general formula:
[(CHs)3N(CH2CH2O)xR1I+ wherein x is an integer of from 1 to 5 and R1 is a C1 to C30 alkyl group with the proviso that the -(CH2CH2O)xR1 substituent has at least 8 carbon atoms; (g) quaternary ammonium ions of general formula:
[R1R2NCH2CH2NR3R4R5J+ wherein R1, R2, R3 and R4 are independently selected from methyl and ethyl; and R5 is a hydrocarbyl group selected from (i) C8 to C30 alkyl groups or (ii) -(CH2)nC6H4R' wherein n is an integer of from O to 5, R' is selected from the group consisting of H, Cl, Br, I, NO2, C1 to C30 alkyl groups, -SO2R", -SOR' ' and -C(O)R' ' (wherein R" is a Ci to C30 alkyl group) with the proviso that R5 has at least 8 carbon atoms.
26. A salt as claimed in claim 25, in which the cation C+ is selected from: hexadecyltrimethylphosphonium, hexadecyltriethylphosphonium, octadecyltrimethylphosphonium, octadecyltriethylphosphonium, dihexadecyldimethylphosphonium, dioctadecyldimethylphosphonium hexadecyltrimethylammonium, hexadecyltriethylammonium, octadecyltrimethylammonium, octadecyltriethylammonium, dihexadecyldimethylammonium, and dioctadecyldimethylammonium.
27. A salt of the general formula Id:
C+ A" (Id)
the salt of general formula Id existing in a liquid state at a temperature below 1500C; in which A' is an anion; and in which the cation, C+, is selected from the group consisting of: (a) a non-aromatic heterocycle of one of the general formulae:
Figure imgf000038_0001
wherein M is N or P; R1 is a Cg to C30 alkyl group; and
R2 is selected from methyl, ethyl or a C8 to C30 alkyl group; (b) an oxazole of one of the general formulae:
Figure imgf000038_0002
wherein R1 is a hydrocarbyl substituent selected from (i) C8 to C30 alkyl groups and (ii) -(CH2)nC6H4R' wherein n is an integer from 0 to 5, R'* is selected from the group consisting of H, Cl, Br, I, NO2, C6 to C30 alkyl group, -SO2R", -SOR" and -C(O)R" (wherein R" is a C1 to C30 alkyl group) with the proviso that -(CH2)HC6H4R' contains at least 8 carbon atoms; and R2 and R3 are independently selected from H, methyl or ethyl; and (c) derivatives of l,5-diazabicyclonon-5-ene and l,9-diazabicycloundec-7-ene of general formulae:
Figure imgf000038_0003
wherein R is a hydrocarbyl substituent selected from (i) C8 to C30 alkyl groups and (ii) ~(CH2)nC6H4R' wherein n is an integer from O to 5, R' is selected from the group consisting of H, Cl, Br, I, NO2, Cj to C30 alkyl groups, -SO2R", -SOR" and -C(O)R" (wherein R" is a C1 to C30 alkyl group) with the proviso that -(CH2)HC6H4R' contains at least 8 carbon atoms.
28. A salt as claimed in any one of claims 19, 20, 22, 23, arid 25 to 27, in which the anion A" comprises at least one hydrophobic tail group attached to an anionic head group.
29. A salt as claimed in claim 28, in which the anion, A", is selected from the group consisting of:
(a) anions of the general formula:
[R1R2P(O)O]- wherein R1 and R2 are independently selected from C8 to C30 alkyl groups;
(b) anions of general formula: [(R1O)(R2O)P(O)O]- wherein R1 and R2 are independently selected from C8 to C30 alkyl groups;
(c) anions of one of the general formulae:
[R(OCH2CH2)xOP(O)(O)2f [(R(OCH2CH2)XO)2P(O)O]- wherein x is an integer of from 4 to 15 and R is an alkyl group;
(d) alkyl sulfate anions of general formula:
ROSO3 " wherein R is an alkyl group having at least 8 carbon atoms;
(e) sulfated polyoxyethylene straight chain alcohols of general formula:
Figure imgf000039_0001
wherein R is a C8 to C30 alkyl group and x is an integer in the range 1 to 10;
(f) alkyl sulfonate anions of general formula:
RSO3- wherein R is an alkyl group having at least 8 carbon atoms; (g) alkylbenzylsulfonates of general formula:
RC6H4SO3 " where R is a C2 to C30 alkyl group; (h) N-acyl-n-alkyltaurates of general formula: RC(O)N(R')CH2CH2SO3 " wherein R is a C4 to C30 alkyl group, and R' is methyl or ethyl; (i) isethionates of general formula
RCOOCH2CH2SO3 " wherein R is a C5 to C30 alkyl group;
(j) sulfonic acid esters of general formula:
ROSO3- wherein R is a Cg to C30 alkyl group; (k) sulfosuccinate esters of general formula: R1OOCCH2CH(SO3OCOOR2 wherein R1 and R2 are C5 to C30 alkyl groups; (1) arylalkanesulfonates of general formula:
R(CH2)mCH(C6H4R1)(CH2)nSO3- wherein m and n are integers in the range 1 to 10; R is H or a C1 to C30 alkyl group; and
R1 is selected from the group consisting of H, Cl, Br, I, NO2, C1 to C30 alkyl groups, -SO2R', -SOR' and -C(O)R' (wherein R' is a C1 to C30 alkyl group); (m) alkyldiphenylether(di)sulfonates of general formula:
RC6H3(SO3OOC6H4SO3- wherein R is a C1 to C30 alkyl group;
(n) carboxylate anions of general formula:
RC(O)O" wherein R is a C7 to C30 alkyl or alkenyl group; (o) borate anions of general formula: [(RCH2CH2)3R1B]- wherein R is H or methyl and R1 is a Cg to C30 alkyl group; and (p) borate anions of general formula:
. ΓΛ
R V1' R02
wherein R1 and R2 are C8 to C30 alkyl groups.
30. A salt as claimed in claim 29, in which the anion, A', is selected from the group consisting of:
(a) anions of the general formula: [R1R2P(O)O]" wherein R1 and R2 are independently selected from C8 to C30 alkyl groups
(b) anions of general formula:
[(R1O)(R2O)P(O)O]" wherein R1 and R2 are independently selected from C8 to C30 alkyl groups. (c) anions of one of the general formulae: [R(OCH2CH2)xOP(θχθ)2f [(R(OCH2CH2)XO)2P(O)O]- wherein x is an integer of from 4 to 15 and R is an alkyl group; and (d) alkyl sulfate anions of general formula: ROSO3 " wherein R is an alkyl group having at least 8 carbon atoms.
31. A salt of the general formula Ie:
C+ A- (Ie)
the salt of general formula Ie existing in a liquid state at a temperature below 150°C; in which A- is an anion of the general formula:
[R1R2P(O)O]" wherein R1 and R2 are independently selected from C8 to C30 alkyl groups; and in which the cation, C+, is an imidazolium ion of the general formula:
Figure imgf000041_0001
wherein R1 is an alkyl group having up to 15 carbon atoms; R2 is selected from H, methyl and ethyl; R3 is selected from methyl, ethyl and C8 to C30 alkyl groups; and R4 and R5 are H or halogen.
32. A salt as claimed in claim 31, in which R1 is an alkyl group having from 8 to 12 carbon atoms.
33. A salt as claimed in either claim 31 or claim 32, in which in the cation C+ R2 is a hydrogen atom; R3 is selected from methyl and ethyl; and each of R4 and R5 is a hydrogen atom.
34. A salt as claimed in any one of claims 31 to 33, in which in the anion A' R1 and R are independently selected from C12 to C18 alkyl groups.
35. A salt as claimed in claim 31, which is: l-dodecyl-3-methylimidazoliumbis(2,4,4-trimethylpentyl)phosphonate; l-decyl-3-methylimidazolium bis(2,4,4-trimethylpentyl)phosphonate;
1 -heptyl-3-methylimidazolium bis(2,4,4-trimethylpentyl)phosphonate; l-butyl-3-methylimidazolium bis(2,4,4-trimethylpentyl)phosphonate; 1-octadecylpyridinium bis(2,4,4-trimethylpentyl)phosphonate; and l-ethyl-3-methylimidazolium bis(2,4,4-trimethylpentyl)phosphonate.
36. A water in oil or oil in water emulsion which comprises (i) an oil phase, (ii) an aqueous phase and (iii) an ionic liquid surfactant wherein the ionic liquid surfactant is a salt as claimed in any one of claims 19 to 35.
37. An emulsion as claimed in claim 36, in the form of a microemulsion having an interfacial tension of less than 1 mNm"1.
38. An emulsion as claimed in either claim 36 or claim 37, in the form of a water in oil microemulsion in which the aqueous phase is distributed in a continuous oil phase in the form of droplets having a diameter in the range 1 to 100 nm or in the form of microdomains having at least one dimension of length, breadth or thickness in the range 1 to 100 nm.
39. An emulsion as claimed in claim 36, in which the internal phase of the emulsion is distributed in a continuous external phase in the form of droplets having a diameter in the range 0.01 to 100 microns.
40. An emulsion as claimed in any one of claims 36 to 39, in which the oil phase is selected from the group consisting of liquid alkanes, alkenes, liquid alkyl halides, liquid aromatic hydrocarbons, paraffin oils, vegetable or animal oils, diesel, kerosene, gas oil, crude oil, lubricant base oil, liquid carbon dioxide, liquid chlorofluorocarbons, tetrahydrofuran, dimethyl formamide and dimethyl sulfoxide.
41. An emulsion as claimed in any one of claims 36 to 40 in which the aqueous phase additionally comprises a water miscible solvent.
42. A composition in the form of a foam, which comprises, as a foaming agent, a salt as defined in any one of claims 1, 7 to 16, and 19 to 35.
43. A composition as claimed in claim 42, suitable for use in a gas and/or gas condensate reservoir.
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Cited By (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1920824A1 (en) * 2006-10-17 2008-05-14 The Queen's University of Belfast Ionic liquids and uses thereof
WO2009071875A1 (en) * 2007-12-07 2009-06-11 Bp Exploration Operating Company Limited Improved aqueous-based wellbore fluids
GB2457151A (en) * 2008-02-11 2009-08-12 Clearwater Int Llc Compositions and methods for gas and oil well treatment
US20110152130A1 (en) * 2008-03-12 2011-06-23 University Of Wyoming Dual Function Gas Hydrate Inhibitors
US8276664B2 (en) 2007-08-13 2012-10-02 Baker Hughes Incorporated Well treatment operations using spherical cellulosic particulates
WO2013096216A1 (en) * 2011-12-21 2013-06-27 Shell Oil Company Method and composition for inhibiting foam in a hydrocarbon mixture
US8481474B1 (en) 2012-05-15 2013-07-09 Ecolab Usa Inc. Quaternized alkyl imidazoline ionic liquids used for enhanced food soil removal
US20130205654A1 (en) * 2012-02-10 2013-08-15 Maxim Peretolchin Imidazolium salts as additives for fuels
US8525155B2 (en) 2008-07-14 2013-09-03 Esionic Es, Inc. Phosphonium ionic liquids, compositions, methods of making and electronic devices formed there from
US8580886B2 (en) 2011-09-20 2013-11-12 Dow Corning Corporation Method for the preparation and use of bis (alkoxysilylorgano)-dicarboxylates
WO2014042783A1 (en) * 2012-09-14 2014-03-20 Liquid Light, Inc. Multiphase electrochemical reduction of co2
US8716207B2 (en) 2012-06-05 2014-05-06 Ecolab Usa Inc. Solidification mechanism incorporating ionic liquids
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US8747674B2 (en) 2009-12-28 2014-06-10 Petroleo Brasileiro S.A.—Petrobras Process for treatment of water/oil emulsions
US20140171348A1 (en) * 2012-12-14 2014-06-19 Exxonmobil Research And Engineering Company Ionic liquids as lubricating oil base stocks, cobase stocks and multifunctional functional fluids
WO2014167375A1 (en) * 2013-04-09 2014-10-16 Services Petroliers Schlumberger Composition and methods for completing subterranean wells
US8927775B2 (en) 2008-07-14 2015-01-06 Esionic Es, Inc. Phosphonium ionic liquids, salts, compositions, methods of making and devices formed there from
US9150472B2 (en) 2011-12-21 2015-10-06 Shell Oil Company Method and composition for inhibiting asphaltene deposition in a hydrocarbon mixture
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US9404052B2 (en) 2011-04-11 2016-08-02 Instituto Mexicano Del Petroleo Dehydrating and desalting median, heavy and extra-heavy oils using ionic liquids and their formulations
US9416307B2 (en) 2011-12-21 2016-08-16 Shell Oil Company Method and composition for inhibiting wax in a hydrocarbon mixture
WO2016161208A1 (en) * 2015-03-31 2016-10-06 Uop Llc Hydrocarbon processes using halometallate ionic liquid micro-emulsions
US9518072B2 (en) 2011-12-02 2016-12-13 Dow Corning Corporation Ester-functional silanes and the preparation and use thereof; and use of iminium compounds as phase transfer catalysts
EP3071321A4 (en) * 2013-11-18 2017-06-07 Indian Institute Of Technology Madras Systems and methods for screening solvents for dissolving tank bottom sludge
US10596561B2 (en) 2015-03-31 2020-03-24 Uop Llc Halometallate ionic liquid micro-emulsions
CN115245797A (en) * 2022-07-19 2022-10-28 山东大学 Preparation of dual-temperature response type ionic liquid microemulsion gel and application of gel in thermoelectric dual-response intelligent window

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8907133B2 (en) 2008-07-14 2014-12-09 Esionic Es, Inc. Electrolyte compositions and electrochemical double layer capacitors formed there from

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2368287A (en) * 1941-08-28 1945-01-30 Ilford Ltd Photographic element and method of making it
GB719445A (en) * 1951-12-22 1954-12-01 Gen Aniline & Film Corp Branched chain alcohol derivatives
US3759982A (en) * 1970-05-26 1973-09-18 Kendall & Co Anionic complexes of monomeric emulsion stabilizers
US4540448A (en) * 1983-03-24 1985-09-10 Societe Nationale Elf Aquitaine Microemulsion-based acid composition and its uses, particularly for cleaning operations
US4595512A (en) * 1980-04-18 1986-06-17 Societe Nationale Elf Aquitaine Process for the preparation of microemulsions between an acid phase and a hyrdophobic phase
EP0331079A1 (en) * 1988-02-29 1989-09-06 Kao Corporation Aerosol preparations
EP1315038A2 (en) * 2001-11-21 2003-05-28 Eastman Kodak Company Dispersions of ionic liquids for photothermographic systems and methods of making such dispersions
WO2004024279A2 (en) * 2002-08-14 2004-03-25 Large Scale Proteomics Corporation Electrophoresis process using ionic liquids
WO2004052340A1 (en) * 2002-12-06 2004-06-24 Novartis Ag Microparticles prepared using an ionic liquid
US20040262578A1 (en) * 2001-09-17 2004-12-30 Peter Wasserscheid Ionic liquids

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2368287A (en) * 1941-08-28 1945-01-30 Ilford Ltd Photographic element and method of making it
GB719445A (en) * 1951-12-22 1954-12-01 Gen Aniline & Film Corp Branched chain alcohol derivatives
US3759982A (en) * 1970-05-26 1973-09-18 Kendall & Co Anionic complexes of monomeric emulsion stabilizers
US4595512A (en) * 1980-04-18 1986-06-17 Societe Nationale Elf Aquitaine Process for the preparation of microemulsions between an acid phase and a hyrdophobic phase
US4540448A (en) * 1983-03-24 1985-09-10 Societe Nationale Elf Aquitaine Microemulsion-based acid composition and its uses, particularly for cleaning operations
EP0331079A1 (en) * 1988-02-29 1989-09-06 Kao Corporation Aerosol preparations
US20040262578A1 (en) * 2001-09-17 2004-12-30 Peter Wasserscheid Ionic liquids
EP1315038A2 (en) * 2001-11-21 2003-05-28 Eastman Kodak Company Dispersions of ionic liquids for photothermographic systems and methods of making such dispersions
WO2004024279A2 (en) * 2002-08-14 2004-03-25 Large Scale Proteomics Corporation Electrophoresis process using ionic liquids
WO2004052340A1 (en) * 2002-12-06 2004-06-24 Novartis Ag Microparticles prepared using an ionic liquid

Cited By (50)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1920824A1 (en) * 2006-10-17 2008-05-14 The Queen's University of Belfast Ionic liquids and uses thereof
US8276664B2 (en) 2007-08-13 2012-10-02 Baker Hughes Incorporated Well treatment operations using spherical cellulosic particulates
AU2008332957B2 (en) * 2007-12-07 2014-05-01 The Queen's University Of Belfast Improved aqueous-based wellbore fluids
WO2009071875A1 (en) * 2007-12-07 2009-06-11 Bp Exploration Operating Company Limited Improved aqueous-based wellbore fluids
US20100256020A1 (en) * 2007-12-07 2010-10-07 The Queen's University Of Belfast Aqueous-based wellbore fluids
US20100256019A1 (en) * 2007-12-07 2010-10-07 The Queen's University Of Belfast Aqueous-based wellbore fluids
AU2008332955B2 (en) * 2007-12-07 2014-05-22 The Queen's University Of Belfast Improved aqueous-based wellbore fluids
EA020066B1 (en) * 2007-12-07 2014-08-29 Дзе Куин'С Юнивёсити Оф Белфаст Wellbore fluids and use thereof
US11603486B2 (en) * 2007-12-07 2023-03-14 The Queen's University Belfast Aqueous-based wellbore fluids
US10844263B2 (en) * 2007-12-07 2020-11-24 The Queen's University Belfast Aqueous-based wellbore fluids
EP2235135B1 (en) * 2007-12-07 2016-12-21 The Queen's University of Belfast Improved aqueous-based wellbore fluids for use to stabilise clay-containing formation
GB2457151B (en) * 2008-02-11 2012-05-23 Clearwater Int Llc Compositions and methods for gas and oil well treatment
GB2457151A (en) * 2008-02-11 2009-08-12 Clearwater Int Llc Compositions and methods for gas and oil well treatment
US20110152130A1 (en) * 2008-03-12 2011-06-23 University Of Wyoming Dual Function Gas Hydrate Inhibitors
US8586797B2 (en) 2008-07-14 2013-11-19 Esionic Es, Inc. Phosphonium ionic liquids, compositions, methods of making and devices formed there from
US8586798B2 (en) 2008-07-14 2013-11-19 Esionic Es, Inc. Heat transfer medium, phosphonium ionic liquids, and methods of making
US8525155B2 (en) 2008-07-14 2013-09-03 Esionic Es, Inc. Phosphonium ionic liquids, compositions, methods of making and electronic devices formed there from
US8927775B2 (en) 2008-07-14 2015-01-06 Esionic Es, Inc. Phosphonium ionic liquids, salts, compositions, methods of making and devices formed there from
US8846246B2 (en) 2008-07-14 2014-09-30 Esionic Es, Inc. Phosphonium ionic liquids, compositions, methods of making and electrolytic films formed there from
US8778534B2 (en) 2008-07-14 2014-07-15 Esionic Es, Inc. Phosphonium ionic liquids, compositions, methods of making and batteries formed there from
US8747674B2 (en) 2009-12-28 2014-06-10 Petroleo Brasileiro S.A.—Petrobras Process for treatment of water/oil emulsions
US9404052B2 (en) 2011-04-11 2016-08-02 Instituto Mexicano Del Petroleo Dehydrating and desalting median, heavy and extra-heavy oils using ionic liquids and their formulations
US8580886B2 (en) 2011-09-20 2013-11-12 Dow Corning Corporation Method for the preparation and use of bis (alkoxysilylorgano)-dicarboxylates
US9518072B2 (en) 2011-12-02 2016-12-13 Dow Corning Corporation Ester-functional silanes and the preparation and use thereof; and use of iminium compounds as phase transfer catalysts
GB2510526A (en) * 2011-12-21 2014-08-06 Shell Int Research Method and composition for inhibiting foam in a hydrocarbon mixture
US9416307B2 (en) 2011-12-21 2016-08-16 Shell Oil Company Method and composition for inhibiting wax in a hydrocarbon mixture
WO2013096216A1 (en) * 2011-12-21 2013-06-27 Shell Oil Company Method and composition for inhibiting foam in a hydrocarbon mixture
US9453173B2 (en) 2011-12-21 2016-09-27 Shell Oil Company Method and composition for inhibiting foam in a hydrocarbon mixture
US20140345190A1 (en) * 2011-12-21 2014-11-27 Shell Oil Company Method and composition for inhibiting foam in a hydrocarbon mixture
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US9150472B2 (en) 2011-12-21 2015-10-06 Shell Oil Company Method and composition for inhibiting asphaltene deposition in a hydrocarbon mixture
US9062266B2 (en) * 2012-02-10 2015-06-23 Basf Se Imidazolium salts as additives for fuels
US20130205654A1 (en) * 2012-02-10 2013-08-15 Maxim Peretolchin Imidazolium salts as additives for fuels
US8481474B1 (en) 2012-05-15 2013-07-09 Ecolab Usa Inc. Quaternized alkyl imidazoline ionic liquids used for enhanced food soil removal
US8716207B2 (en) 2012-06-05 2014-05-06 Ecolab Usa Inc. Solidification mechanism incorporating ionic liquids
WO2014042783A1 (en) * 2012-09-14 2014-03-20 Liquid Light, Inc. Multiphase electrochemical reduction of co2
EP2738234A1 (en) * 2012-11-29 2014-06-04 Shell Internationale Research Maatschappij B.V. Composition and process for demulsifying oil/water emulsions
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US20140171348A1 (en) * 2012-12-14 2014-06-19 Exxonmobil Research And Engineering Company Ionic liquids as lubricating oil base stocks, cobase stocks and multifunctional functional fluids
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US20160060500A1 (en) * 2013-04-09 2016-03-03 Slaheddine Kefi Composition and Methods for Completing Subterranean Wells
WO2014167375A1 (en) * 2013-04-09 2014-10-16 Services Petroliers Schlumberger Composition and methods for completing subterranean wells
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US10596561B2 (en) 2015-03-31 2020-03-24 Uop Llc Halometallate ionic liquid micro-emulsions
US10814317B2 (en) 2015-03-31 2020-10-27 Uop Llc Hydrocarbon processes using halometallate ionic liquid micro-emulsions
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