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NO149557B - PROCEDURE FOR OIL EXTRACTION FROM UNDERGROUND OIL SOURCES AND SURFACTIVE AGENTS FOR USE IN EXECUTION OF THE PROCEDURE - Google Patents

PROCEDURE FOR OIL EXTRACTION FROM UNDERGROUND OIL SOURCES AND SURFACTIVE AGENTS FOR USE IN EXECUTION OF THE PROCEDURE Download PDF

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NO149557B
NO149557B NO791889A NO791889A NO149557B NO 149557 B NO149557 B NO 149557B NO 791889 A NO791889 A NO 791889A NO 791889 A NO791889 A NO 791889A NO 149557 B NO149557 B NO 149557B
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carbon atoms
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weight
fluorine
surfactant
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NO791889L (en
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Thomas W Cooke
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Ciba Geigy Ag
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/02Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
    • C08G65/32Polymers modified by chemical after-treatment
    • C08G65/329Polymers modified by chemical after-treatment with organic compounds
    • C08G65/331Polymers modified by chemical after-treatment with organic compounds containing oxygen
    • C08G65/332Polymers modified by chemical after-treatment with organic compounds containing oxygen containing carboxyl groups, or halides, or esters thereof
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B23MACHINE TOOLS; METAL-WORKING NOT OTHERWISE PROVIDED FOR
    • B23KSOLDERING OR UNSOLDERING; WELDING; CLADDING OR PLATING BY SOLDERING OR WELDING; CUTTING BY APPLYING HEAT LOCALLY, e.g. FLAME CUTTING; WORKING BY LASER BEAM
    • B23K35/00Rods, electrodes, materials, or media, for use in soldering, welding, or cutting
    • B23K35/22Rods, electrodes, materials, or media, for use in soldering, welding, or cutting characterised by the composition or nature of the material
    • B23K35/36Selection of non-metallic compositions, e.g. coatings, fluxes; Selection of soldering or welding materials, conjoint with selection of non-metallic compositions, both selections being of interest
    • B23K35/3612Selection of non-metallic compositions, e.g. coatings, fluxes; Selection of soldering or welding materials, conjoint with selection of non-metallic compositions, both selections being of interest with organic compounds as principal constituents
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/68Polyesters containing atoms other than carbon, hydrogen and oxygen
    • C08G63/688Polyesters containing atoms other than carbon, hydrogen and oxygen containing sulfur
    • C08G63/6884Polyesters containing atoms other than carbon, hydrogen and oxygen containing sulfur derived from polycarboxylic acids and polyhydroxy compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/02Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
    • C08G65/32Polymers modified by chemical after-treatment
    • C08G65/329Polymers modified by chemical after-treatment with organic compounds
    • C08G65/334Polymers modified by chemical after-treatment with organic compounds containing sulfur
    • C08G65/3342Polymers modified by chemical after-treatment with organic compounds containing sulfur having sulfur bound to carbon and hydrogen
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/02Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
    • C08G65/32Polymers modified by chemical after-treatment
    • C08G65/338Polymers modified by chemical after-treatment with inorganic and organic compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G77/00Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
    • C08G77/04Polysiloxanes
    • C08G77/38Polysiloxanes modified by chemical after-treatment
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    • 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
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/60Compositions for stimulating production by acting on the underground formation
    • C09K8/602Compositions for stimulating production by acting on the underground formation containing surfactants

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
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  • General Life Sciences & Earth Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Mechanical Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
  • Fats And Perfumes (AREA)
  • Removal Of Floating Material (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Detergent Compositions (AREA)

Description

Ved utvinning av olje fra oljebærende kilder er When extracting oil from oil-bearing sources is

det vanligvis mulig å utvinne bare en liten del av den opp-rinnelige olje på stedet ved de såkalte primære utvinnings-metoder som bare utnytter det naturlige trykk som er til- it is usually possible to extract only a small part of the liquefiable oil on site by the so-called primary extraction methods which only utilize the natural pressure that is available

stede i kilden. For å øke utvinningen over det som økono- present in the source. In order to increase recovery above what is economically

misk er utvunnet ved anvendelse av slike naturkrefter er det blitt utviklet flere utvinningsteknikker. En av de mest vanlig anvendte videreutviklede utvinningsteknikker omfatter bruk av vannflømming. Vannet injiseres vanligvis inn i kil- misc is extracted using such natural forces, several extraction techniques have been developed. One of the most commonly used advanced extraction techniques involves the use of waterflooding. The water is usually injected into the wedge-

den for å presse råolje mot produksjonsstedet. Mengden av olje som utvinnes ved vannflømming avhenger av slike faktor- it to push crude oil towards the production site. The amount of oil recovered by waterflooding depends on such factors-

er som grenseflatespenning mellom vann og råolje, de rela- is like the interfacial tension between water and crude oil, the rela-

tive hastigheter av råolje og vann og fuktighetskarakteri-stikker av fjellene som holder oljen i kilden. tive velocities of crude oil and water and moisture characteristics of the rocks that hold the oil in the source.

For å øke effektiviteten av vannflømmingsteknik- To increase the efficiency of waterflooding tech-

ken settes overflateaktive stoffer til vannet. Det overflateaktive stoff nedsetter overflatespenningen av den van- when surfactants are added to the water. The surfactant lowers the surface tension of the water

dige væske og grenseflatespenningen mellom den vandige væske og petroleum og øker vannfukte-egenskapene derav, og derved reduseres kapillarkreftene i de underjordiske formasjoner som skal behandles. Dette hjelper til å frigjøre oljen fra underjordiske sand- og fjellformasjoner. Vanligvis er det benyttet vandige sammensetninger som inneholder petroleumsulfonater, fordelaktig i kombinasjon med kontrollerte meng- dige liquid and the interfacial tension between the aqueous liquid and petroleum and increases the water-wetting properties thereof, thereby reducing the capillary forces in the underground formations to be treated. This helps to release the oil from underground sand and rock formations. Generally, aqueous compositions containing petroleum sulphonates have been used, advantageously in combination with controlled amounts of

der av NaCl. Også natriumkarbonat og/eller natriumtripolyfosfat kan settes til slike sammensetninger som et tilset-ningsmiddel for å beskytte petroleumsulfonat-overflateaktive stoff fra tap som skyldes utfellingsreaksjoner med divalente kationer. Videre er det foreslått bruk av fortykningsmidler for å øke vannflømmingens glidningseffekt. En vannflømmings-teknikk innbefatter bruk av et preflushed eller kondisjonert slam for å nedsette mengden av divalente kationer (f.eks. Ca 2 +, Mg 7 +) som ville utfelle eller absorbere det overflateaktive stoff, et overflateaktivt middel inneholdende slam for å there of NaCl. Also, sodium carbonate and/or sodium tripolyphosphate can be added to such compositions as an additive to protect petroleum sulfonate surfactant from loss due to precipitation reactions with divalent cations. Furthermore, the use of thickeners has been proposed to increase the sliding effect of waterflooding. A waterflooding technique involves using a preflushed or conditioned sludge to reduce the amount of divalent cations (eg, Ca 2 + , Mg 7 + ) that would precipitate or absorb the surfactant, a surfactant containing sludge to

løsne og presse ut oljen fra sand og fjell, og et hastighets-bufferslam som kan benyttes for å stå imot det overflateak- loosen and squeeze out the oil from sand and rock, and a speed-buffer mud that can be used to resist the surface ac-

tive system. Preflush eller kondisjoneringsslammet er fritt tive system. Preflush or the conditioning mud is free

for kationer som ville påvirke overflateaktiviteten og kan inneholde helt eller delvis oppløsninger av natriumkarbonat og natriumtripolyfosfat og lignende. Eventuelt kan NaCl-lake deretter injiseres for å optimere saltkonsentrasjonen for optimal utpresningsevne. Natriumionene erstatter altså kalsium- og magnesiumioner. Sterk syre kan benyttes for å bryte opp karbonatfjellformasjon. Etter injisering med den vandige overflateaktive oppløsning injiseres hastighetsbuffer-slammet. Hastighetsbufferen inneholder vanligvis en vannopp-løselig polymer som polyakrylamid eller en biopolymer (f.eks. naturlig gummi). for cations that would affect the surface activity and may contain complete or partial solutions of sodium carbonate and sodium tripolyphosphate and the like. Optionally, NaCl brine can then be injected to optimize the salt concentration for optimal extrudability. The sodium ions therefore replace calcium and magnesium ions. Strong acid can be used to break up carbonate rock formations. After injection with the aqueous surfactant solution, the rate buffer sludge is injected. The rate buffer usually contains a water-soluble polymer such as polyacrylamide or a biopolymer (eg natural rubber).

Etter injeksjonen av hastighetsbuffer eller kon-trollslammet injiseres et drivfluidum for å erstatte de tid-ligere injiserte fluider gjennom sand- eller fjellformasjonen. Naturen av drivfluidet er ikke kritisk og kan eksempelvis være lokalt tilgjengelig vann. Drivfluidet bør imidlertid ikke være uforenelig med den underjordiske formasjon. I en utførelse av ovennevnte teknikk, hvor det benyttes et preflush-slam, overflateaktivt slam og hastighetsbuffer-slam, After the injection of the velocity buffer or the control mud, a driving fluid is injected to replace the previously injected fluids through the sand or rock formation. The nature of the drive fluid is not critical and can for example be locally available water. However, the driving fluid should not be incompatible with the underground formation. In an embodiment of the above technique, where a preflush sludge, surfactant sludge and velocity buffer sludge are used,

er det overflateaktive slam i form av en vandig mikroemulsjon av olje i kombinasjon med petroleumsulfonater, ko-overflateaktive midler som alkoholer dg elektrolytter. is the surfactant sludge in the form of an aqueous microemulsion of oil in combination with petroleum sulphonates, co-surfactants such as alcohols and electrolytes.

Ifølge oppfinnelsen er det tilveiebragt en fremgangsmåte for behandling av underjordiske formasjoner for å stimulere strømmen av olje derifra og overflateaktive midler for bruk i slik behandling. According to the invention, there is provided a method for treating underground formations to stimulate the flow of oil therefrom and surfactants for use in such treatment.

Oppfinnelsen vedrører en fremgangsmåte for oljeutvinning fra underjordiske oljekilder ved injeksjon av et vandig overflateaktivt middel for å frigjøre olje fra kilden, idet fremgangsmåten er karakterisert ved at det anvendes et middel som inneholder en overflateaktiv forbindelse med formel The invention relates to a method for extracting oil from underground oil sources by injecting an aqueous surface-active agent to release oil from the source, the method being characterized by the use of an agent containing a surface-active compound with the formula

hvor R, er en hydrofob-oleofob fluoralifatisk gruppe med 4-24 karbonatomer, Z betyr en divalent forbindelsesgruppe, where R, is a hydrophobic-oleophobic fluoroaliphatic group with 4-24 carbon atoms, Z means a divalent connecting group,

A er et divalent hydrofilt organisk radikal, Q er en divalent forbindelsesgruppe, er et hydrofobt-oleofilt alifatisk radikal med 6-24 karbonatomer eller aralifatisk radikal med minst 9 karbonatomer, og m og n er uavhengig av hverandre 0 eller 1, idet den fluorholdigé overflateaktive forbindelse har en oppløselighet i vann ved 30°C på minst 0,01 vekt-%, .utøver en overflatespenning på mindre enn 30 dyn/cm ved 0,1 vekt-% aktiv forbindelse i avionisert vann og utøver en grenseflatespenning på mindre enn 12 dyn/cm ved 0,1 vekt-% aktive forbindelser i avionisert vann, målt i forhold til cykloheksan og eventuelt i tillegg inneholder ikke-fluorerte anioniske, blandinger av anioniske og ikke-ioniske eller kationiske overflateaktive forbindelser. A is a divalent hydrophilic organic radical, Q is a divalent connecting group, is a hydrophobic-oleophilic aliphatic radical with 6-24 carbon atoms or araliphatic radical with at least 9 carbon atoms, and m and n are independently 0 or 1, the fluorine-containing surfactant compound has a solubility in water at 30°C of at least 0.01% by weight, exerts a surface tension of less than 30 dyne/cm at 0.1% by weight active compound in deionized water and exerts an interfacial tension of less than 12 dyn/cm at 0.1% by weight active compounds in deionized water, measured in relation to cyclohexane and optionally additionally contains non-fluorinated anionic, mixtures of anionic and nonionic or cationic surfactant compounds.

Eventuelt inneholder det vandige overflateaktive middel ytterligere overflateaktive midler, f.eks. av ikke-fluor-ert type, som er anioniske, blandinger av anioniske og ikke-ioniske eller kationiske. Oppløseligheten av ønskelige overflateaktive midler i avionisert vann kan være mindre enn den anvendte konsentrasjon (0,1 vekt-% i avionisert vann) ved mål-ing av overflate- og grenseflatetensjoner. I slike tilfel-ler utføres målingene i et mettet heterogent vandig system inneholdende 0,1% av det fluoralifatiske overflateaktive middel i avionisert vann. Optionally, the aqueous surfactant contains further surfactants, e.g. of non-fluorinated type, which are anionic, mixtures of anionic and nonionic or cationic. The solubility of desirable surfactants in deionized water may be less than the concentration used (0.1% by weight in deionized water) when measuring surface and interfacial tensions. In such cases, the measurements are carried out in a saturated heterogeneous aqueous system containing 0.1% of the fluoroaliphatic surfactant in deionized water.

Fortrinnsvis utøver det fluoralifatiske overflateaktive middel en overflatetensjon på 0,1% aktiv i avionisert vann på ca. 16-28 dyn/cm og en grenseflatespenning på mindre enn 12 dyn/cm, f.eks. på ca. 4-10 dyn/cm i avionisert vann målt mot cykloheksan. Preferably, the fluoroaliphatic surfactant exerts a surface tension of 0.1% active in deionized water of approx. 16-28 dyne/cm and an interfacial tension of less than 12 dyne/cm, e.g. of approx. 4-10 dyne/cm in deionized water measured against cyclohexane.

De fluoralifatiske overflateaktive midler inneholder vanligvis minst 2-50 vekt-% fluor og fortrinnsvis 5-35 vekt-% fluor. The fluoroaliphatic surfactants usually contain at least 2-50% by weight fluorine and preferably 5-35% by weight fluorine.

R^-radikale er fortrinnsvis et rettlinjet eller forgrenet perfluoralifatisk radikal som inneholder 4-24 karbonatomer og kan være avbrutt med oksygen. R^-radical is preferably a straight or branched perfluoroaliphatic radical which contains 4-24 carbon atoms and may be interrupted by oxygen.

I en foretrukket utførelsesform er Rf-gruppen rettlinjet eller forgrenet perfluoralkyl med 4-20 karbonatomer, rettlinjet eller forgrenet perfluoralkenyl med 4-20 karbon- - atomer, eller rettlinjet eller forgrenet perfluoralkyl-polyfluoralkoksy-perfluoralkylen med opp til 24 karbonatomer . In a preferred embodiment, the Rf group is linear or branched perfluoroalkyl with 4-20 carbon atoms, linear or branched perfluoroalkenyl with 4-20 carbon atoms, or linear or branched perfluoroalkyl-polyfluoroalkyl-perfluoroalkylene with up to 24 carbon atoms.

Egnede R^-grupper er de med følgende formel: Suitable R^ groups are those with the following formula:

hvori n er 4 - 20 hvori n er 4 - 20 og -<1> hvori m er 1-3, p er 2-4, q er 0-6 og r er 1-10, med den forholdsregel atm+p+q+rer minst 4. Egnede Rf-grupper med formel (2) er CF^ICF,,)^ hvor x betyr 3 - 19 og blandinger herav, såvel som de av typen wherein n is 4 - 20 wherein n is 4 - 20 and -<1> wherein m is 1-3, p is 2-4, q is 0-6 and r is 1-10, with the precaution atm+p+q +rer at least 4. Suitable Rf groups with formula (2) are CF^ICF,,)^ where x means 3 - 19 and mixtures thereof, as well as those of the type

og blandinger herav. and mixtures thereof.

Egnede R^-grupper med formel (3) er de av typen CF3(CF2)Q_g-CF=CF(CF2)1-9 og blandinger herav, såvel som forgrenede analoge som Suitable R^ groups with formula (3) are those of the type CF3(CF2)Q_g-CF=CF(CF2)1-9 and mixtures thereof, as well as branched analogues such as

Representative R^-grupper med formel (4) er de av typen og blandinger herav. Representative R^ groups of formula (4) are those of the type and mixtures thereof.

Rj-radikale kan også inneholder substituenter foruten fluor, som klor og hydrogen. Imidlertid bør ikke mer enn 2 0% av slike substituenter være forskjellig fra fluor for at radikalet skal utøve sin hydrofobisk-olefobe karakter. Rj radicals can also contain substituents besides fluorine, such as chlorine and hydrogen. However, no more than 20% of such substituents should be different from fluorine for the radical to exert its hydrophobic-olephobic character.

Egnede R^-radikaler som inneholder slike andre substituenter omfatter følgende: Suitable R₂ radicals containing such other substituents include the following:

hvor a er 0 til 8, og b er 0 til 8, forutsatt at (a+b) ligger mellom 2 og 16. where a is 0 to 8, and b is 0 to 8, provided that (a+b) is between 2 and 16.

Naturen av den divalente forbindelsesgreuppe Z, når den er tilstede, er ikke kritisk så lenge som den utøver den vesentlige funksjon av kovalent binding av den fluoralifatiske gruppe, R^, til hydrofile organiske radikal A. The nature of the divalent linking group Z, when present, is not critical as long as it performs the essential function of covalently linking the fluoroaliphatic group, R^, to the hydrophilic organic radical A.

Således kan Z eksempelvis velges blant følgende: Thus, Z can, for example, be selected from among the following:

~C1~C6 alkylen-' ~C1~C6 alkylene-'

-fenylen-, -phenylene-,

-(C^-Cg-alkylen)- R^(C^-Cg-alkylen)-, -(C 1 -C 8 -alkylene)- R^(C 1 -C 8 -alkylene)-,

- (C-j^-Cg-alkylen) ) , - (C-j^-Cg-alkylene) ) ,

- R^-- (C^-Cg-alkylen)-, - R^-- (C^-Cg-alkylene)-,

~R1~(Ci~c6~alkylen-Ri) ~R1~(Ci~c6~alkylene-Ri)

~<R>l"'~<R>l"'

-R1~fenylen-(C^-Cg-alkylen-R^)-, -R1~phenylene-(C^-Cg-alkylene-R^)-,

-R^-fenylen-, eller -R^-phenylene-, or

-fenylen-R| -phenylene-R|

hvor i hvert tilfelle nevnte alkylen og fenylen er uavhengig usubstituert eller substituert med hydroksy, halogen, nitro, karboksy, C-L-Cg-alkoksy, C-|_-Cg-alkanoyl, C^-Cg-karbalkoksy, G-^-Cg-alkanoyloksy eller C-i^-Cg-alkanoylamino. Alkylen-radikalet kan være rett- wherein in each case said alkylene and phenylene are independently unsubstituted or substituted by hydroxy, halogen, nitro, carboxy, C-L-Cg-alkoxy, C-|_-Cg-alkanoyl, C^-Cg-carbalkoxy, G-^-Cg- alkanoyloxy or C 1 -C 8 -alkanoylamino. The alkylene radical can be straight-

linjet eller forgrenet. lined or branched.

R-^ og R^ betyr uavhengig R-^ and R^ mean independent

, -NR2CO-, -CONR2- , -NR2CO-, -CONR2-

R2 betyr hydrogen, C^-Cg-alkyl eller C-^- C^- alkyl, substituert med: C-^-Cg-alkoksy, halogen, hydroksy, karboksy, C^-Cg-karbalkoksy, C-j^-Cg-alkanoyloksy eller C^-Cg-alkanoylamino. R 2 means hydrogen, C 1 -C 8 -alkyl or C 1 -C 8 -alkyl, substituted with: C 1 -C 8 -alkyloxy, halogen, hydroxy, carboxy, C 1 -C 8 -carbaloxy, C 1 -C 8 -alkanoyloxy or C 1 -C 8 -alkanoylamino.

I tillegg kan Z inneholde et cykloalifatisk eller heterocyklisk radikal. In addition, Z may contain a cycloaliphatic or heterocyclic radical.

Således kan R-^ eksempelvis i tillegg bety Thus, R-^ can, for example, additionally mean

hvor R, betyr -0Ro, -OM hvor M er definert nedenfor, eller -NHR-; where R, means -ORo, -OM where M is defined below, or -NHR-;

R R

R. betyr -0- eller |2 R. means -0- or |2

-N- , og -N- , and

R5 betyr hydrogen, halogen, C-j^-Cg-alkyl eller C^-Cg-alkoksy, eller R-^ betyr: R 5 means hydrogen, halogen, C 1 -C 8 alkyl or C 1 -C 8 alkoxy, or R 5 means:

Egnede hydrofile radikaler A er eksempelvis det hydrofile divalente radikal med følgende formel: Suitable hydrophilic radicals A are, for example, the hydrophilic divalent radical with the following formula:

hvori Rg betyr hydrogen, eller en blanding av hydrogen og metyl, med den forutsetning at slik R, er overveiende hydrogen; hvor R7 betyr hydrogen, lavere alkyl eller hydroksyetyl; hvori Ry betyr hydrogen eller hydroksyetyl; hvor t betyr 1 til 3 og Rg betyr lavere alkyl, hydroksy-laverealkyl eller iCH2CH20)gH; hvor t betyr 1 til 3 og T er -S03M, -COOM, -P03M, -OS03M eller -OP03M2, og M betyr hydrogen, ammonium eller et alkalimetallkation; eller wherein R 8 means hydrogen, or a mixture of hydrogen and methyl, with the proviso that such R 8 is predominantly hydrogen; where R 7 means hydrogen, lower alkyl or hydroxyethyl; wherein Ry is hydrogen or hydroxyethyl; where t means 1 to 3 and Rg means lower alkyl, hydroxy-lower alkyl or iCH2CH2O)gH; wherein t is 1 to 3 and T is -SO 3 M, -COOM, -PO 3 M, -OSO 3 M or -OPO 3 M 2 , and M is hydrogen, ammonium or an alkali metal cation; or

hvori Rg, R^q og R^ uavhengig betyr hydrogen; C^-C4-alkyl eller C2~C4 alkyl substituert med hydroksy, C^-C^-alkoksy eller hydroksy-C2-C4~alkoksy; og en av Rg og R1Q kan i tillegg bety benzyl; u betyr 0 eller 1; wherein Rg, R^q and R^ are independently hydrogen; C 1 -C 4 -alkyl or C 2 -C 4 -alkyl substituted with hydroxy, C 1 -C 4 -alkyloxy or hydroxy-C 2 -C 4 -alkyl; and one of Rg and R1Q can additionally be benzyl; u means 0 or 1;

R^ betyr i tillegg C^-Cg-alkylen substituert med sulfo eller karboksy; X betyr acetat, halogen, metosulfat eller hydroksylanion hvor u betyr 1 og R^ er forskjellig fra nevnte C-j^-Cg-alkylen, og t betyr 1 til 3. R 1 additionally means C 1 -C 8 alkylene substituted by sulfo or carboxy; X means acetate, halogen, methosulphate or hydroxyl anion where u means 1 and R^ is different from said C-j^-Cg alkylene, and t means 1 to 3.

I hver av de ovennevnte formler hvor det er nevnt, betyr s 2 til 60, fortrinnsvis 5 til 25. In each of the above formulas where mentioned, s means 2 to 60, preferably 5 to 25.

Blandinger av ovennevnte hydrofile radikaler kan Mixtures of the above hydrophilic radicals can

være tilstede. be present.

Også egnet er hydrofile divalenterradikaler hvori minst en del av den hydrofile karakter skyldes en avhengig gruppe som et divalent radikal med formel: Also suitable are hydrophilic divalent radicals in which at least part of the hydrophilic character is due to a dependent group such as a divalent radical of formula:

hvor n-^ og n, uavhengig av hverandre betyr 0 til 2 0 og n2 og n^ uavhengig betyr 1 til 2 0; hvori n5 betyr uavhengig 2 til 20 og n^ uavhengig 1 til 10,eller where n-^ and n independently mean 0 to 2 0 and n 2 and n^ independently mean 1 to 2 0; wherein n5 means independently 2 to 20 and n^ independently 1 to 10, or

hvor R14 betyr hydrogen, C1~C4 alkyl, eller (OCH2CH2)n OH; where R14 means hydrogen, C1~C4 alkyl, or (OCH2CH2)n OH;

^9 ^ 2 ketyr uavhengig av hverandre 0 til 4, y 3 betyr 1 til 8, og n2 og n4 er uavhengige av hverandre 1 til 20. ^9 ^ 2 independently denotes 0 to 4, y 3 denotes 1 to 8, and n2 and n4 independently denote 1 to 20.

Q er en divalent forbindelsesgruppe og på samme måte som Z er ikke kritisk så lenge som den utøver den vesentlige funksjon av kovalent binding av det hydrofile organiske radikal A til den hydrofobe-oleofile gruppe RHC- Q is a divalent connecting group and, in the same way as Z, is not critical as long as it performs the essential function of covalently binding the hydrophilic organic radical A to the hydrophobic-oleophilic group RHC-

Således forbindelsesgruppen Q er uavhengig valgt fra de grupper som er angitt for Z, med den forutsetning at når R^ eller Rj er direkte bundet til A, og A ender i en oksy eller amino ligand, og Ri i denne stilling er forskjellig fra: Thus the connecting group Q is independently selected from the groups indicated for Z, with the proviso that when R^ or Rj is directly bound to A, and A ends in an oxy or amino ligand, and Ri in this position is different from:

, -s-, , -oso2-, -oso3~, , -s-, , -oso2-, -oso3~,

eller -0-. or -0-.

R^ er en hydrofob-oleofil, alifatiske eller aralifatisk monovalent gruppe. R 1 is a hydrophobic-oleophilic, aliphatic or araliphatic monovalent group.

Egnede R^-grupper innbefatter hydrofil-oleofil høyere alkyl eller alkenyl eller 6-24 karbonatomer, som er usubstituert eller substituert med: klor, brom, alkoksy med opptil 18 karbonatomer, nitro, alkanoyl med opptil 18 karbonatomer, alkylmercapto med opptil 18 karbonatomer, amino, C^-C^g-alkylamino eller di-C^-C^g-alkylamino. Suitable R^ groups include hydrophilic-oleophilic higher alkyl or alkenyl or 6-24 carbon atoms, which are unsubstituted or substituted with: chlorine, bromine, alkoxy of up to 18 carbon atoms, nitro, alkanoyl of up to 18 carbon atoms, alkylmercapto of up to 18 carbon atoms, amino, C 1 -C 8 -alkylamino or di-C 1 -C 8 -alkylamino.

Fortrinnsvis er nevnte alkyl eller alkenyl med minst 8 karbonatomer. Alkyl og<:>alkenyl-gruppene kan være rettlinjet eller forgrenet. Blandinger herav kan benyttes. Said alkyl or alkenyl is preferably with at least 8 carbon atoms. The alkyl and<:>alkenyl groups may be straight or branched. Mixtures of these can be used.

I tillegg kan R^-gruppen være en gruppe, med formel: In addition, the R^ group can be a group, with formula:

hvori R5 betyr C1-C6-alkyl, n? betyr 5-20, og Rg betyr hydrogen eller alkyl med opptil 24 karbonatomer. wherein R 5 means C 1 -C 6 alkyl, n? means 5-20, and Rg means hydrogen or alkyl of up to 24 carbon atoms.

Videre kan R^-gruppen være en hydrofob-oleofil aralifatisk radikal med minst 9 karbonatomer. Furthermore, the R 1 group can be a hydrophobic-oleophilic araliphatic radical with at least 9 carbon atoms.

Egnede slike grupper innbefatter de med formel: Suitable such groups include those of formula:

hvori ng betyr 0 til 1; wherein ng means 0 to 1;

R-^cj betyr alkyl med opptil 20 karbonatomer, alkoksy med opptil 2 0 karbonatomer, alkanoyl med opptil 2 0 karbonatomer, mono- eller dialkylamino med opptil 20 karbonatomer, alkylmercapto med opptil 20 karbonatomer, alkanoyloksy med opptil 20 karbonatomer, eller karbalkoksy med opptil 20 karbonatomer; R-^cj means alkyl of up to 20 carbon atoms, alkoxy of up to 20 carbon atoms, alkanoyl of up to 20 carbon atoms, mono- or dialkylamino of up to 20 carbon atoms, alkylmercapto of up to 20 carbon atoms, alkanoyloxy of up to 20 carbon atoms, or caralkyloxy of up to 20 carbon atoms;

R-^g betyr hydrogen, halogen, nitro eller R-^-R-^g means hydrogen, halogen, nitro or R-^-

Også egnet er hydrofob-oleofile grupper med formel: Also suitable are hydrophobic-oleophilic groups with the formula:

hvor ng, R^^ og R-^ har ovennevnte betydning. where ng, R^^ and R-^ have the above meaning.

I tillegg kan gruppen ~Qn-R|jc hvori n betyr 1 bety en gruppe med formel In addition, the group ~Qn-R|jc in which n means 1 can mean a group of formula

hvori R^- j og R^g uavhengig av hverandre betyr høyere alkylgrupper wherein R^-j and R^g independently of each other mean higher alkyl groups

med 6 til 24 karbonatomer, eller gruppen —K^2~cg_alkylen^—°"with 6 to 24 carbon atoms, or the group —K^2~cg_alkylene^—°"

hvori R^g og Rjq er høyere alkyl med 6 til 24 karbonatomer. wherein R^g and Rjq are higher alkyl of 6 to 24 carbon atoms.

Foretrukne forbindelser er de som er vesentlig ikke ioniske, dvs. fri for sterkt sure grupper, som -SO^H og -PO-^H og fri for sterkt basiske kvaternære ammonium-grupper. Preferred compounds are those which are substantially non-ionic, i.e. free of strongly acidic groups, such as -SO^H and -PO-^H and free of strongly basic quaternary ammonium groups.

Blant slike foretrukne vesentlig ikke ioniske overflateaktive midler.spesielt lysende er de som både utøver en overflatetensjon ved 0,1% aktivitet i avionisert vann og ca. 16 til 28 dyn/cm, tilveiebringer en oppløselighet i vann på minst 0,01vekt%, utøver en grenseflatespenning på mindre enn 12 dyn/cm ved 0,lvekt% aktive i avionisert vann målt mot cyklohexan og hvori det tilsvarende hydrokarbon overf lateaktive midlet R^-Q^-A-OH, har en tilsynelatende HLB (hydrofil-lipofil balanse) i området på ca. Among such preferred substantially non-ionic surfactants, particularly luminous are those which both exert a surface tension at 0.1% activity in deionized water and approx. 16 to 28 dynes/cm, provides a solubility in water of at least 0.01% by weight, exerts an interfacial tension of less than 12 dynes/cm at 0.1% by weight active in deionized water measured against cyclohexane and wherein the corresponding hydrocarbon surfactant R ^-Q^-A-OH, has an apparent HLB (hydrophilic-lipophilic balance) in the range of approx.

5 til 24, og fortrinnsvis i området fra 12 til 18. 5 to 24, and preferably in the area from 12 to 18.

HLB av et vesentlig ikke-ionisk hydrokarbon overflateaktivt middel er en velkjent indikasjon på prosentvekten av den hydrofile del av det ikke-ioniske hydrokarbon overflateaktive mole-kyl. Eksempelvis Ind. and Eng. Chem,Anal.Ed.Vol. 18, side 500(1946). The HLB of a substantially nonionic hydrocarbon surfactant is a well-known indication of the percentage weight of the hydrophilic portion of the nonionic hydrocarbon surfactant molecule. For example, Ind. and Eng. Chem, Anal. Ed. Vol. 18, page 500(1946).

En spesielt foretrukket klasse av fluorkjemiske overflateaktive midler er de med formel: A particularly preferred class of fluorochemical surfactants are those of the formula:

hvor R^ rettlinjet eller'forgrenet betyr perfluoralkyl med 4 til 2 0 spesielt 4 til 12 karbonatomer, R^ betyr alkyl med 6 til 24, fortrinnsvis 12 til 18 karbonatomer eller hvor R- 21 betyr alkyl med 3 til 20, fortrinnsvis 6 til 12 karbonatomer og R22 betyr hydrogen, halogen (klor, brom, fluor), nitro eller R2^» m betyr 0 eller 1, s betyr 5 til 30, Z betyr -COO-, -S03-, -O-, -C1-C4-alkylen-COO-, -C^-C^-alkylen-SC^, where R^ straight or branched means perfluoroalkyl with 4 to 20 especially 4 to 12 carbon atoms, R^ means alkyl with 6 to 24, preferably 12 to 18 carbon atoms or where R- 21 means alkyl with 3 to 20, preferably 6 to 12 carbon atoms and R22 means hydrogen, halogen (chloro, bromine, fluorine), nitro or R2^» m means 0 or 1, s means 5 to 30, Z means -COO-, -SO3-, -O-, -C1-C4 -alkylene-COO-, -C^-C^-alkylene-SC^,

Foretrukket er de forbindelser med formel (5), hvor Rf °^ s ^ar ^e an9itte betydninger og m og n betyr null. Preferred are the compounds with formula (5), where Rf °^ s ^ar ^e given meanings and m and n mean zero.

Foretrukket er også de forbindelser med formel (5), Preferred are also the compounds with formula (5),

hvori Z betyr -C-^-C^-alkylen-S wherein Z means -C-C-C-Alkylene-S

som med formel: eller hvori Z betyr med formel: as by formula: or where Z means by formula:

hvori Rf, RHC og s har ovennevnte betydning. wherein Rf, RHC and s have the above meaning.

De fluorkjemiske overflateaktive stoffer som benyttes ifølge oppfinnelsen kan fremstilles ifølge kjente fremgangsmåter. Således kan f.eks. de fluorkjemiske overflateaktive midler fremstilles ved omsetning av kjente hydrokarbon-overflateaktive midler med formel: The fluorochemical surfactants used according to the invention can be produced according to known methods. Thus, e.g. the fluorochemical surfactants are produced by reacting known hydrocarbon surfactants with the formula:

med et fluoralifatisk syrehalogenid i et inert oppløsningsmiddel. with a fluoroaliphatic acid halide in an inert solvent.

Eksempelvis kan <CF>3(CF2)7S02F fremstilt ifølge US-patent nr. 2.759.019 omsettes med H(OCH2CH2)5_2QN(stearyl)2 i dietyleter som oppløsningsmiddel og pyridin eller trietylamin som syreakseptor for å gi den tilsvarende ester med formel: For example, <CF>3(CF2)7SO2F prepared according to US patent no. 2,759,019 can be reacted with H(OCH2CH2)5_2QN(stearyl)2 in diethyl ether as solvent and pyridine or triethylamine as acid acceptor to give the corresponding ester with formula:

Analogt kan n-C3F7OCF(CF3)COF som angitt i kanadisk patent nr. 725.740 omsettes med octylfenoksy-poly(etylenoksy)etanol med en gjennomsnittlig molekylvekt mellom 514 og 778 i nærvær av dietyleter og pyridin som syreakseptor for å gi den tilsvarende ester. Analogously, n-C3F7OCF(CF3)COF as stated in Canadian Patent No. 725,740 can be reacted with octylphenoxy-poly(ethyleneoxy)ethanol having an average molecular weight between 514 and 778 in the presence of diethyl ether and pyridine as acid acceptor to give the corresponding ester.

Alternativt kan a-perfluoralken med formel C n F2„ n—l, hvor n betyr 6-2 0 omsettes med et hydrokarbon overflateaktivt middel med formel: R„0-Q n-A-OH i nærvær av kaliumkarbonat i et inert oppløsningsmiddel, som metyl-etyl-keton eller aceton ved en temperatur på 20-70°C, Alternatively, the α-perfluoroalkene of formula C n F2„ n—l, where n means 6-2 0, can be reacted with a hydrocarbon surfactant of formula: R„0-Q n-A-OH in the presence of potassium carbonate in an inert solvent, such as methyl -ethyl ketone or acetone at a temperature of 20-70°C,

for å gi den tilsvarende fluoralifatiske eter. to give the corresponding fluoroaliphatic ether.

Eksempelvis kan et oleinsyre-etylen-oksyd-kondensat (molekylvekt på ca. 680) omsettes med tetrafluoretylen-pentamer i nærvær av kaliumkarbonat i aceton for å gi et produkt med formel C10F19°(CH2CH2°)10<C>OC15H29" Hvis det benyttes en blanding av cetyl/oleyl-etylen-oksyd-kondensat (molekylvekt på ca. 550) oppnås tilsvarende cetyl/oleyl-eter-produkt med formel For example, an oleic acid ethylene oxide condensate (molecular weight of about 680) can be reacted with tetrafluoroethylene pentamer in the presence of potassium carbonate in acetone to give a product of the formula C10F19°(CH2CH2°)10<C>OC15H29" If used a mixture of cetyl/oleyl ethylene oxide condensate (molecular weight of approx. 550) gives a corresponding cetyl/oleyl ether product with the formula

C10F19° (CH2CH20) 10C16H31/33 .• C10F19° (CH2CH20) 10C16H31/33 .•

Slike forbindelser og deres fremstilling omtales i britisk patent 1.371.054. Such compounds and their preparation are discussed in British patent 1,371,054.

Alternativt kan fluoralifatiske isocyanater og karbamin-syre-halogenider omsettes med hydrokarbon overflateaktive midler med formel R„ n- Q -A-OH eller R_„ -Q -A-NHR- for å gi de tilsvarende uretaner og urinstoff, resp. Reaksjonene utføres fortrinnsvis i nærvær av et inert medium ved temperaturer på 2 0 til 5 0°C. Hvor det fluoralifatiske karbaminsyrehalogenid er en reaksjonsdeltager, settes det fortrinnsvis til et tertiært amin som trietylamin eller pyridin for å påskynde reaksjonen og fjerne dannet hydrogenhalogenid. Alternatively, fluoroaliphatic isocyanates and carbamic acid halides can be reacted with hydrocarbon surfactants of the formula R„ n- Q -A-OH or R_„ -Q -A-NHR- to give the corresponding urethanes and urea, resp. The reactions are preferably carried out in the presence of an inert medium at temperatures of 20 to 50°C. Where the fluoroaliphatic carbamic acid halide is a reaction participant, it is preferably added to a tertiary amine such as triethylamine or pyridine to accelerate the reaction and remove the hydrogen halide formed.

Eksempelvis blir 1,1-dihydroperfluoroctyl-karbamyl-klorid, med formel C7<F>15CH2NHC0C1, fremstilt ifølge tysk patent 1.145.606, satt langsomt til etoksylert (15 mol) kokosfettsyre i dietyleter, i nærvær av trietylamin som en HCl-oppfanger, under omrøring. Det resulterende produkt har formel For example, 1,1-dihydroperfluorooctylcarbamyl chloride, with formula C7<F>15CH2NHC0C1, prepared according to German patent 1,145,606, is added slowly to ethoxylated (15 mol) coconut fatty acid in diethyl ether, in the presence of triethylamine as an HCl scavenger, while stirring. The resulting product has the formula

<C>7<F>15CH2NHCOO—*CH2CH2~°i5' C0<R>HC' hvor RHC er kokosfettsyre-hydro-karbonresiduet. <C>7<F>15CH2NHCOO—*CH2CH2~°i5' C0<R>HC' where RHC is the coconut fatty acid hydrocarbon residue.

På tilsvarende måte kan CF3(CF2)gNCO fremstilles overensstemmende med US-patent -nr. 2.617.817, omsettes med stearin eller laurinsyre-amid-etylenimin (4 til 6 mol) kondensat, som de eksempelvis omtalt i US-patent nr. 2.163.807 i et inert fortynningsmiddel for å danne et produkt med formel CF-. (CF-,) ,NHCO (NHCH0CH„) . , In a similar way, CF3(CF2)gNCO can be prepared in accordance with US patent no. 2,617,817, is reacted with stearin or lauric acid-amide-ethyleneimine (4 to 6 mol) condensate, such as those described for example in US Patent No. 2,163,807 in an inert diluent to form a product of formula CF-. (CF-,) ,NHCO (NHCH0CH„) . ,

J £■ o Z 2. 4 —D —NHCO-RHC, hvori RHC er hydrokarbonresidu av stearin eller laurinsyre. J £■ o Z 2. 4 —D —NHCO-RHC, wherein RHC is the hydrocarbon residue of stearic or lauric acid.

Produktet kan nøytraliseres med vandig HCl eller H2S04 for å- danne de tilsvarende salter, eller kan alkyleres med dimetyl-sulfat eller metylhalogenid, som metylbromid for å danne de tertiære eller kvaternære ammoniumderivater herav. Alternativt kari produktet The product can be neutralized with aqueous HCl or H2S04 to form the corresponding salts, or can be alkylated with dimethyl sulphate or methyl halide, such as methyl bromide to form the tertiary or quaternary ammonium derivatives thereof. Alternatively the curry product

omsettes med etylenoksyd, f.eks. i mengder på 4 til 15 mol pr. reacted with ethylene oxide, e.g. in quantities of 4 to 15 mol per

mol produkt for å danne de etoksylerte derivater herav i nærvær av en HCl-katalysator. moles of product to form the ethoxylated derivatives thereof in the presence of an HCl catalyst.

Analogt kan fosgen omsettes med ikke-ioniske hydro-karbonoverflatemidler med formel R^-Q^-A-OH for å danne det tilsvarende klorformat og syrekloridet omsettes med en fluoralifatisk alkohol eller amin for å danne det tilsvarende karbonat eller uretan, resp. Fortrinnsvis utføres reaksjonen i nærvær av et tertiært amin, som trietylamin, og et inert fortynnin<q>smiddel. Analogously, phosgene can be reacted with nonionic hydrocarbon surfactants of formula R^-Q^-A-OH to form the corresponding chloroformate and the acid chloride reacted with a fluoroaliphatic alcohol or amine to form the corresponding carbonate or urethane, resp. Preferably, the reaction is carried out in the presence of a tertiary amine, such as triethylamine, and an inert diluent.

Eksempelvis kan C12H25S (CH^t^O-)-^-^ omsettes med fosgen i nærvær av trietylamin for å gi det tilsvarende syreklorid C12<H>25<S>(CH2CH20^ioCOC1' SOm p^ sin side omsettes med en fluoralifatisk alkohol som (CF3)2CFO-CF2CF2-CH2CH2CONH(CH2)30H, omtalt i US-patent nr. 3.697.564 i nærvær av trietylamin i dietyleter for For example, C12H25S (CH^t^O-)-^-^ can be reacted with phosgene in the presence of triethylamine to give the corresponding acid chloride C12<H>25<S>(CH2CH20^ioCOC1' SOm p^ is in turn reacted with a fluoroaliphatic alcohol such as (CF3)2CFO-CF2CF2-CH2CH2CONH(CH2)30H, disclosed in US Patent No. 3,697,564 in the presence of triethylamine in diethyl ether for

å gi et produkt med formel to give a product with formula

(CF3)2CFO-CF2CF2CH2CH2CONH(CH2)3OCO(OCH2CH2-) s-ci2H25' (CF3)2CFO-CF2CF2CH2CH2CONH(CH2)3OCO(OCH2CH2-) s-ci2H25'

På samme måte kan C^gF^gOCgH^SC^Cl som omtalt i britisk patent 1.130.822 og 1.270.662 omsettes med polyoksyetylen (20)sorbitan-monolaurat i nærvær av trietylamin i et inert fortynningsmiddel for å danne den tilsvarende ester. Similarly, C^gF^gOCgH^SC^Cl as disclosed in British Patents 1,130,822 and 1,270,662 can be reacted with polyoxyethylene (20)sorbitan monolaurate in the presence of triethylamine in an inert diluent to form the corresponding ester.

Fortrinnsvis kan fluorkjemiske overflateaktive midler fremstilles ved omsetning av et hydrokarbon overflateaktivt middel med formel Ruo-Q -A-OH med en ekvimolar mengde av toluen diisocyanat for å danne 1:1 uretan-addukt herav, og omsetning av uretan-monoisocyanat med polyfluor alifatisk amin eller alkohol. Preferably, fluorochemical surfactants can be prepared by reacting a hydrocarbon surfactant of the formula Ruo-Q -A-OH with an equimolar amount of toluene diisocyanate to form a 1:1 urethane adduct thereof, and reacting the urethane monoisocyanate with polyfluoro aliphatic amine or alcohol.

Således kan nonylfenoksypolyetoksyetanol med et gjennomsnitt på 4 mol etylenoksyd omsettes med et mol toluen diisocyanat for å danne det tilsvarende 1:1 addukt, som på sin side omsettes med et perfluoralkylalkylamin med formel CgF^7(CH2)^NH2 som kan fremstilles overensstemmende med US-patent 3.257.407 for å danne det tilsvarende urinstoffderivat. Thus, nonylphenoxypolyethoxyethanol with an average of 4 moles of ethylene oxide can be reacted with one mole of toluene diisocyanate to form the corresponding 1:1 adduct, which in turn is reacted with a perfluoroalkylalkylamine of formula CgF^7(CH2)^NH2 which can be prepared in accordance with US -patent 3,257,407 to form the corresponding urea derivative.

Analogt kan mange fluorkjemiske overflateaktive forbindelser med formel R^-Z -A-OH omsettes med egnede alifatiske Analogously, many fluorochemical surface-active compounds of the formula R^-Z -A-OH can be reacted with suitable aliphatic

in in

eller aralifatiske syrehalogenider, isocyanater og lignende, for å danne egnede fluorkjemiske overflateaktive midler for bruk ifølge oppfinnelsen. or araliphatic acid halides, isocyanates and the like, to form suitable fluorochemical surfactants for use according to the invention.

Eksempelvis kan CgF17S02N(C2H5)-CH2CH2(OCH2CH2)1Q-0H For example, CgF17S02N(C2H5)-CH2CH2(OCH2CH2)1Q-0H

omtalt i US-patent 2.915.554 omsettes med dodecylbenzensulfonyl- discussed in US patent 2,915,554 is reacted with dodecylbenzenesulfonyl-

klorid i dietyleter i nærvær av trietylamin for å gi den tilsvarende sulfonatester. chloride in diethyl ether in the presence of triethylamine to give the corresponding sulfonate ester.

Anvendelige overflateaktive midler for bruk ifølge oppfinnelsen kan også fremstilles ved omsetning av et fluoralifatisk tiol med et etylenisk umettet dikarboksylsyreanhydrid og omsetning av det resulterende anhydridkondensat med en. ekvimolar mengde av hydrokarbon-overflateaktivt middel med formel R„_-Q -A-OH eller R„~-Q -A-NH- for å danne den resulterende halv-tid n nu n z Useful surfactants for use according to the invention can also be prepared by reacting a fluoroaliphatic thiol with an ethylenically unsaturated dicarboxylic acid anhydride and reacting the resulting anhydride condensate with a. equimolar amount of hydrocarbon surfactant of formula R„_-Q -A-OH or R„~-Q -A-NH- to form the resulting half-time n nu n z

ester eller halvamid, respektiv. Alternativt kan det etylenisk ume.ttede dikarboksylsyreanhydrid omsettes med en ekvimolar mengde av hydrokarbon overf lateaktivt middel med formel R^-Q -A-OH eller , Rjj^-Q -A-NH2, eksempelvis, og reaksjonsproduktet omsettes med et fluoralifatisk tiol. ester or half amide, respectively. Alternatively, the ethylenically unsaturated dicarboxylic acid anhydride can be reacted with an equimolar amount of hydrocarbon surfactant of formula R^-Q -A-OH or , Rjj^-Q -A-NH2, for example, and the reaction product is reacted with a fluoroaliphatic thiol.

Eksempelvis kan dodecylfenoksypolyetoksyetanol (inneholdende 9 mol etylenoksyd) omsettes med en ekvimolar mengde maleinsyre anhydrid i et inert fortynningsmiddel som sulfolan for å gi den tilsvarende halvester med formel: For example, dodecylphenoxypolyethoxyethanol (containing 9 moles of ethylene oxide) can be reacted with an equimolar amount of maleic anhydride in an inert diluent such as sulfolane to give the corresponding half-ester with formula:

Halvesteren kan omsettes med et fluoralifatisk tiol som C9F19<C>2<H>4<S>H, fremstilt ifølge US-patenter nr. 3.172.910 og 3.088.849. Reaksjonen utføres fortrinnsvis i vesentlig støkiome-triske mengder i vandig etanol i nærvær av mindre mengder natrium-hydroksyd og et tertiært amin, som piperidin, ved fra 20 til 75°C, f.eks. å danne et produkt med formel: fremstilt ifølge US-patent nr. 3.471.518 omsettes med forbindelsen med formel: The half ester can be reacted with a fluoroaliphatic thiol such as C9F19<C>2<H>4<S>H, prepared according to US Patent Nos. 3,172,910 and 3,088,849. The reaction is preferably carried out in substantially stoichiometric amounts in aqueous ethanol in the presence of minor amounts of sodium hydroxide and a tertiary amine, such as piperidine, at from 20 to 75°C, e.g. to form a product of formula: prepared according to US Patent No. 3,471,518 is reacted with the compound of formula:

omtalt i US-patent nr. 2.341.84 6 ved å tilbakeløpskoke ekvimolare mengder i dioksan for å danne den tilsvarende halvester. disclosed in US Patent No. 2,341,84 6 by refluxing equimolar amounts in dioxane to form the corresponding half ester.

På samme måte kan forbindelsen med formel: Likewise, the compound with formula:

hvor R^ er en blanding av C5~c^0Per^luoralkyl, fremstilt ved omsetning av norbornen anhydrid og R^ CB^CB^SH i nærvær av en liten mengde av azobutyronitril som katalysator, omsettes med 3-(n-dodecyl-amino)-propylamin i ekvimolare mengder ved en temperatur på 2 0 til 5 0°C i et inert fortynningsmiddel som toluen og dehydratisering av produktet ved azotropisk destillering av vann for å gi det tilsvarende imin som igjen kan etoksyleres med 10 mol etylenoksyd i et vandig surt medium for å gi et produkt med formel: 0 where R^ is a mixture of C5~c^0 Per^fluoroalkyl, prepared by reacting norbornene anhydride and R^ CB^CB^SH in the presence of a small amount of azobutyronitrile as a catalyst, reacted with 3-(n-dodecyl-amino )-propylamine in equimolar amounts at a temperature of 20 to 50°C in an inert diluent such as toluene and dehydration of the product by azeotropic distillation of water to give the corresponding imine which can again be ethoxylated with 10 moles of ethylene oxide in an aqueous acid medium to give a product of formula: 0

Noen av de fluorkjemiske overflateaktive midler som kan benyttes ifølge oppfinnelsen er kjente forbindelser. Some of the fluorochemical surfactants which can be used according to the invention are known compounds.

Egnede fluorkjemiske overflateaktive midler som angitt ovenfor og benyttet ifølge oppfinnelsen kan lett fremstilles fra kjente utgangsmaterialer ved vanlig teknikk, som de som er angitt ovenfor og som videre er vist i de følgende eksempler. Suitable fluorochemical surfactants as indicated above and used according to the invention can be easily prepared from known starting materials by ordinary techniques, such as those indicated above and which are further shown in the following examples.

Fortrinnsvis er de fluorkjemiske overflateaktive midler benyttet alene i et vandig system eller i en kombinasjon med et vanlig vannflømmingsoverflateaktivt middel. Slike overflateaktive midler for øket oljeutvinning er velkjent og innbefatter anioniske overflateaktive midler som petroleumsulfonater, synte-tiske alkyl-aryl-sulfonater og lignende, anioniske-ikke-ioniske overflateaktive systemer, som de som er angitt i US-patent nr. 3.811.504, 3.792.731 og 4.005.749 og kationiske overflateaktive systemer. Preferably, the fluorochemical surfactants are used alone in an aqueous system or in combination with a common water-flooding surfactant. Such surfactants for enhanced oil recovery are well known and include anionic surfactants such as petroleum sulfonates, synthetic alkyl-aryl sulfonates and similar anionic-nonionic surfactant systems, such as those disclosed in US Patent No. 3,811,504, 3,792,731 and 4,005,749 and cationic surfactant systems.

Blandinger av kationiske og anioniske overflateaktive midler bør vanligvis unngås, da de kan være uforenelige på grunn av interaksjon. Mixtures of cationic and anionic surfactants should generally be avoided as they may be incompatible due to interaction.

Den totale mengde av overflateaktivt middel basert på vandig medium kan variere innen vide grenser, f.eks. mellom 0,01 og 4 0 vekt%, vanligvis 0,05 til 20 vekt%. Når det benyttes en blanding av fluorkjemisk overflateaktivt middel ifølge oppfinnelsen og en vanlig: vannflømmings-overflateaktivt middel er det vanligvis til stede minst 1%, fortrinnsvis minst 4% av det fluorkjemiske overflateaktive middel, basert på mengden av ikke-fluorkjemisk overflateaktivt middel. The total amount of surfactant based on aqueous medium can vary within wide limits, e.g. between 0.01 and 40% by weight, usually 0.05 to 20% by weight. When a mixture of fluorochemical surfactant according to the invention and a conventional: waterflooding surfactant is used, there is usually present at least 1%, preferably at least 4% of the fluorochemical surfactant, based on the amount of non-fluorochemical surfactant.

Den vandige overflateaktive væske kan også fortrinnsvis inneholde egnede ko-overflateaktive midler som alifatisk eller alkyl-aryl-alkoholer med en molekylvekt på 4 0 til 22 0 i mengder opptil 10 volum% av oppløsningen. Et monovalent salt kan også være til stede i det vandige medium i mengder opp til . 5 vekt% basert på det vandige medium for saltholdighetskontroll. The aqueous surfactant liquid may also preferably contain suitable co-surfactants such as aliphatic or alkyl-aryl alcohols with a molecular weight of 40 to 220 in amounts up to 10% by volume of the solution. A monovalent salt can also be present in the aqueous medium in amounts up to . 5% by weight based on the aqueous medium for salinity control.

Forskjellige fortykningsmidler som guar-gummi eller polysakkarider og sakrifise stoffer som uorganiske polyfosfater eller alkalimetall-karbonater, kan også være tilstede. Various thickeners such as guar gum or polysaccharides and sacrificial substances such as inorganic polyphosphates or alkali metal carbonates may also be present.

I en utførelse kan overflateaktive væsker være i form av en vandig petroleumsolje-emulsjon inneholdende 0,5 til 4 0 vekt% olje basert på vekten av den vandige fase. In one embodiment, surfactant liquids may be in the form of an aqueous petroleum oil emulsion containing 0.5 to 40% by weight of oil based on the weight of the aqueous phase.

I en ytterligere utførelse av oppfinnelsen, omfatter den endelige del av den vandige overflateaktive væske, eller vandige petroleumsolje-emulsjon en lavere konsentrasjon av ikke-vandige ingredienser enn begynnelsesdelen injisert i kilden, hvorfra oljen utvinnes. Bruk av en slik konsentra-sjonsgradient reduserer således den totale mengde av nødven- In a further embodiment of the invention, the final portion of the aqueous surfactant liquid, or aqueous petroleum oil emulsion comprises a lower concentration of non-aqueous ingredients than the initial portion injected into the source, from which the oil is recovered. Use of such a concentration gradient thus reduces the total amount of emergency

dig overflateaktivt middel i oljeutvinningsprosedyren. surfactant in the oil extraction procedure.

Oppfinnelsen skal forklares nærmere ved hjelp av noen ikke-begrensende eksempler, hvor alle deler er vektdeler hvis intet annet er angitt. The invention shall be explained in more detail by means of some non-limiting examples, where all parts are parts by weight if nothing else is indicated.

Eksempel 1 Example 1

I en 500 ml kolbe utstyrt med termometer, rørverk og nitrogeninnløp has 84,2 g (0,075 mol) polyetoksylert cetyl-alkohol med et gjennomsnitt på 2 0 étoksyenheter og med formel: omrøres ved 5 0-5 5°C under nitrogen. Bor-trifluorid i form av dietyleter-komplekset (47,3% BF^) ble tilsatt i mengder på 0,4 g. Deretter ble 6,1 g epiklorhydrin (0,066 mol) satt langsomt til blandingen under opprettholdelse av temperaturen ved 5 0-6 0°C over en periode på ca. 10 minutter. Reaksjoneblandingen ble deretter omrørt ved en temperatur på 5 0-60°C for ytterligere 30 minutter. Det dannede produkt har formel: In a 500 ml flask equipped with a thermometer, piping and nitrogen inlet, 84.2 g (0.075 mol) of polyethoxylated cetyl alcohol with an average of 20 ethoxy units and with formula: is stirred at 50-55°C under nitrogen. Boron trifluoride in the form of the diethyl ether complex (47.3% BF^) was added in amounts of 0.4 g. Then 6.1 g of epichlorohydrin (0.066 mol) was slowly added to the mixture while maintaining the temperature at 5 0- 6 0°C over a period of approx. 10 minutes. The reaction mixture was then stirred at a temperature of 50-60°C for a further 30 minutes. The product formed has the formula:

Til detté reaksjonsprodukt ble det deretter satt 140,3 g vannfri isopropylalkohol og 27,9 g RfCH2CH2SH, hvor Rf er rettlinjet perfluoralkyl med følgende R^ fordeling: 0,9% C4Fg-, 32,9% C6F13-, 37,5% CgF^-, 22, 99% C-^F^-, og 5,3% ci2<F>25 (<g>jennomsnittlig molekylvekt omtrent 465) og blandingen omrøres ved ca. 5 0°C. Deretter tilsettes 5,4 g 5 0%-ig vandig NaOH (0,0672 mol) langsomt med en slik hastighet som opprettholder reaksjonsblandingen ved 50-60°C. Det dannes en hvit utfelling av NaCl. Blandingen ble omrørt i ytterligere én time ved 5 0-55°C og skiftet fra farveløs til svakt gul. Oppløs-ningen ble deretter filtrert for å fjerne biproduktet NaCl. Ved tørking ble det oppnådd 73,6 g av produktet (ca. 70% utbytte).. Produktet har formel: 140.3 g of anhydrous isopropyl alcohol and 27.9 g of RfCH2CH2SH were then added to this reaction product, where Rf is linear perfluoroalkyl with the following R^ distribution: 0.9% C4Fg-, 32.9% C6F13-, 37.5% CgF ^-, 22, 99% C-^F^-, and 5.3% ci2<F>25 (<g>average molecular weight approximately 465) and the mixture is stirred at approx. 50°C. Then 5.4 g of 50% aqueous NaOH (0.0672 mol) are added slowly at such a rate that maintains the reaction mixture at 50-60°C. A white precipitate of NaCl is formed. The mixture was stirred for an additional hour at 50-55°C and changed from colorless to slightly yellow. The solution was then filtered to remove the by-product NaCl. By drying, 73.6 g of the product was obtained (approx. 70% yield). The product has the formula:

Eksempel 2 Example 2

Idet det benyttes fremgangsmåten ifølge Eks. 1 ble polyetoksylart stearyl-amin med formel As the method according to Ex. 1 was polyethoxylated stearyl amine of formula

(hvor q + r er 15) (where q + r is 15)

i en mengde på 54,69 g (0,063 mol) omsatt med 5,09 g (0,055 mol) epiklorhydrin i nærvær av 0,3 g BF^; dietyleter-komplek og det resulterende reaksjonsprodukt omsatt med 23,25 g R^Cf^CI^SH ifølge Eks. 1 i nærvær av 4,48 g 50%-ig vandig NaOH i 98,85 g isopropanol. Reaksjonsproduktet ble omrørt i 2 timer før filtrering for å gi 151,47 g ravfarvet uklar oppløsning. Ved refiltrering ble det oppnådd 142,01 g klar ravfarvet oppløsning. Ved tørking ble det oppnådd 46,43 g av produktet med formel: in an amount of 54.69 g (0.063 mol) reacted with 5.09 g (0.055 mol) of epichlorohydrin in the presence of 0.3 g of BF^; diethyl ether complex and the resulting reaction product reacted with 23.25 g of R^Cf^CI^SH according to Ex. 1 in the presence of 4.48 g of 50% aqueous NaOH in 98.85 g of isopropanol. The reaction product was stirred for 2 hours before filtration to give 151.47 g of amber cloudy solution. By refiltration, 142.01 g of clear amber colored solution was obtained. Upon drying, 46.43 g of the product with formula was obtained:

E ksempel 3 Example 3

Under anvendelse av fremgangsmåten ifølge Eks. 1 ble 264,0 g etoksylert (15) p-nonyl-fenol med formel Using the method according to Ex. 1 was 264.0 g of ethoxylated (15) p-nonyl-phenol with formula

omsatt med 24,42 g epiklorhydrin i nærvær av 1,6 g BF^; dietyleter-komplekset og produktet herav ble deretter omsatt med 111,6 g R^CI^CI^SH, hvori Rf har fordelingen som i Eks. 1, i nærvær av reacted with 24.42 g of epichlorohydrin in the presence of 1.6 g of BF^; The diethyl ether complex and the product thereof were then reacted with 111.6 g of R^CI^CI^SH, in which Rf has the distribution as in Ex. 1, in the presence of

21,50 g 50% vandig natrium-hydroksyd og 460,4 g isopropylalkohol. 21.50 g of 50% aqueous sodium hydroxide and 460.4 g of isopropyl alcohol.

Det resulterende reaksjonsprodukt har formel: The resulting reaction product has the formula:

Eksempel 4 Example 4

Maleinsyreanhydrid, 2,55 g og 2,55 g sulfolan som oppløsningsmiddel, ble satt til 36,45 g av dinonyl-polyetoksylert (24) fenol med formel: og omrørt i 20 timer ved-60°C for å danne en reaksjonsblanding inneholdende en halvester med formel: Maleic anhydride, 2.55 g and 2.55 g of sulfolane as solvent were added to 36.45 g of dinonyl-polyethoxylated (24) phenol of the formula: and stirred for 20 hours at -60°C to form a reaction mixture containing a half esters with formula:

Til denne reaksjonsblanding ble det deretter satt 0,1 g trietylamin og 11,63 g RfCJ^CH^SH med R^-fordelingen ifølge Eks. 1 under et nitrogen og blandingen omrørt ved 6 0°C i ca. To this reaction mixture was then added 0.1 g of triethylamine and 11.63 g of RfCJ^CH^SH with the R^ distribution according to Ex. 1 under nitrogen and the mixture stirred at 60°C for approx.

7 timer. Produktet har formel: 7 hours. The product has the formula:

Eksempel 5 Example 5

For å måle effektiviteten av fluorkjemisk overflateaktivt middel i utdrevet olje fra en oljebærende underjordisk formasjon ved å øke effektiviteten av det vandige medium, ble det benyttet følgende screen-teknikk: E£2§§^Y£§: 20 g av sand-olje-blanding (10% A.S.T.M.-olje nr. 3 og 90% Ottawa-standardsand 20-30 mesh) plasseres i et 25 x 150 mm prøverør. Prøveoppløsningen (25 ml ved 0,1% aktiver av prøve i avionisert vann) legges forsiktig over sand-olje-blandingen. Systemet hensettes deretter uforstyrret i 18-20 timer. Enhver olje som perkolerer til overflaten, fjernes med en pipette og veies. Resultatet er angitt som % utvunnet (dvs. vekten av oljen utvunnet To measure the effectiveness of fluorochemical surfactant in expelled oil from an oil-bearing underground formation by increasing the effectiveness of the aqueous medium, the following screen technique was used: E£2§§^Y£§: 20 g of sand-oil- mixture (10% A.S.T.M. oil No. 3 and 90% Ottawa standard sand 20-30 mesh) is placed in a 25 x 150 mm test tube. The sample solution (25 ml at 0.1% active of sample in deionized water) is carefully placed over the sand-oil mixture. The system is then left undisturbed for 18-20 hours. Any oil that percolates to the surface is removed with a pipette and weighed. The result is given as % recovered (ie the weight of the oil recovered

sammenlignet med det teoretiske maksimum på 2,0 g olje i røret). compared to the theoretical maximum of 2.0 g of oil in the tube).

3 til 5 forsøk gjøres for hver prøve for gjennomsnittsverdi. 3 to 5 trials are done for each sample for average value.

I de følgende tabeller, forbindelsene ble siktet In the following tables, the compounds were charged

ved 0,10% aktivitet i avionisert vann, overflatetensjon og grense-flatespenninger ble målt mot cyklohexan. Hvis intet annet er angitt var R^-fordelingen i perfluoralkyl-overflateaktive midlene: 0,9% C4F9-, 32,9% C6F13-, 37,5% CgF^-, 22,9% C-^F^- og <5,3%><C>12<F>25. at 0.10% activity in deionized water, surface tension and interfacial tensions were measured against cyclohexane. Unless otherwise stated, the R^ distribution in the perfluoroalkyl surfactants was: 0.9% C4F9-, 32.9% C6F13-, 37.5% CgF^-, 22.9% C-^F^- and < 5.3%><C>12<F>25.

Eksempel 6 Example 6

I den følgende tabell er det gitt formuleringer av forskjellige hydrokarbon overflateaktive midler med representative fluorkjemiske overflateaktive midler og deres effektivitet i uttatt olje ifølge fremgangsmåten angitt i Eks. 5. I følgende tabell er hydrokarbon overflateaktivt middel A et kommersielt anionisk sulfat-overflateaktivt middel. (Conco EL-3 0); hydrokarbon-overflateaktivt middel B er et polyetoksylert nonylfenol-ikke-ionisk overflateaktivt middel ("Igepal CO-710"), og overflateaktivt middel C er petroleum-sulfonat anionisk overflateaktivt middel ("Tetronate L"). In the following table, there are given formulations of different hydrocarbon surfactants with representative fluorochemical surfactants and their effectiveness in withdrawn oil according to the method indicated in Ex. 5. In the following table, hydrocarbon surfactant A is a commercial anionic sulfate surfactant. (Conco EL-30); hydrocarbon surfactant B is a polyethoxylated nonylphenol nonionic surfactant ("Igepal CO-710"), and surfactant C is petroleum sulfonate anionic surfactant ("Tetronate L").

Resultatene av ovennevnte tabell viser fordelene The results of the above table show the benefits

som kan oppnås ved å benytte formuleringer av vanlige hydrokarbon-overflateaktive midler sammen med fluorkjemiske overflateaktive midler i tertiær oljeutvinning. which can be achieved by using formulations of conventional hydrocarbon surfactants together with fluorochemical surfactants in tertiary oil recovery.

Claims (10)

1. Fremgangsmåte for oljeutvinning fra underjordiske oljekilder ved injeksjon av et vandig overflateaktivt middel for å frigjøre oljen fra kilden, karakterisert ved at det anvendes et middel inneholdende en overflateaktiv forbindelse med formel hvor ^ er en hydrofob-oleofob fluoralifatisk gruppe med 4-24 karbonatomer, Z betyr en divalent forbindelsesgruppe, A er et divalent hydrofilt organisk radikal, Q er en divalent forbindelsesgruppe, R er et hydrofobt-oleoEilt alifatisk radikal med 6-24 karbonatomer eller aralifatisk radikal med minst 9 karbonatomer, og m og n er uavhengig av hverandre 0 eller 1, idet den fluorholdige overflateaktive forbindelse har en oppløselighet i vann ved 30°C på minst 0,01 vekt-%, utøver en overflatespenning på mindre enn 30 dyn/cm ved 0,1 vekt-% aktive forbindelser i avionisert vann og utøver en grenseflatespenning på mindre enn 12 dyn/cm ved 0,1 vekt-% aktive forbindelser i avionisert vann, målt i forhold til cykloheksan, og eventuelt i tillegg inneholder ikke-fluorerte anioniske, blandinger av anioniske og ikke-ioniske eller kationiske overf lateaktive forbindelser..1. Method for oil extraction from underground oil sources by injecting an aqueous surface-active agent to release the oil from the source, characterized in that an agent containing a surface-active compound of formula is used where ^ is a hydrophobic-oleophobic fluoroaliphatic group with 4-24 carbon atoms, Z means a divalent connecting group, A is a divalent hydrophilic organic radical, Q is a divalent connecting group, R is a hydrophobic-oleoyl aliphatic radical with 6-24 carbon atoms or araliphatic radical with at least 9 carbon atoms, and m and n are independently 0 or 1, the fluorine-containing surfactant compound has a solubility in water at 30°C of at least 0.01% by weight, exerts a surface tension of less than 30 dyne/cm at 0.1% by weight active compounds in deionized water and exerts an interfacial tension of less than 12 dyne/cm at 0.1% by weight of active compounds in deionized water, measured in relation to cyclohexane, and possibly additionally contains non-fluorinated anionic, mixtures of anionic and nonionic or cationic surface-active compounds. 2. Fremgangsmåte ifølge krav 1, karakterisert ved at det anvendes en fluorholdig overflateaktiv forbindelse som utøver en overflatespenning på 16 28 dyn/cm ved 0,1 vekt-% aktiveforbindélseri avionisert vann og en grenseflatespenning på mindre enn 12 dyn/cm ved 0,1 vekt-% aktive forbindelser i avionisert vann, målt i forhold til cykloheksan.2. Method according to claim 1, characterized in that a fluorine-containing surface-active compound is used which exerts a surface tension of 16 28 dyne/cm at 0.1% by weight active compound deionized water and an interfacial tension of less than 12 dyne/cm at 0.1 wt% active compounds in deionized water, measured relative to cyclohexane. 3. Fremgangsmåte ifølge krav 2, kara, kteri-s e r t ved at det anvendes en fluorholdig overflateaktiv. forbindelse som i det vesentlige er ikke-ionisk.3. Method according to claim 2, characterized in that a fluorine-containing surfactant is used. compound which is essentially non-ionic. 4. Fremgangsmåte ifølge krav 3,karakterisert ved at det anvendes en overflateaktiv forbindelse - HO-A-Q -R^ som har en hydrofil-lipofil balanse i området 4 - 24.4. Method according to claim 3, characterized in that a surface-active compound is used - HO-A-Q -R^ which has a hydrophilic-lipophilic balance in the range 4 - 24. 5. Fremgangsmåte ifølge krav 4, karakter i-, sert ved at det anvendes en overflateaktiv forbindelse HO-A-Q -Rjj£ som har en hydrof il-lipof il likevekt i området 12 - 18.5. Method according to claim 4, character i-, characterized in that a surface-active compound HO-A-Q-Rjj£ is used which has a hydrophilic-lipophilic equilibrium in the range 12 - 18. 6. Fremgangsmåte ifølge krav 4,karakterisert ved at det anvendes en fluorholdig overflateaktiv forbindelse med formel hvori Rf betyr rettlinjet eller forgrenet perfluoralkyl med 4-20 karbonatomer, R^ er alkyl med 6-24 karbonatomer eller en gruppe med formel hvori R ^ betyr alkyl med 3 - 20 karbonatomer og R22 betyr hydrogen, halogen, nitro eller I^i' m ketyr 0 eller 1, s betyr 5 - 25, Z betyr -COO-, -S03~, -0-, -C^-C^-alkylen-COO-, COOH -C1-C4-alkylen-S03 , -(^-C^-alkylen-S-C1H-CH^OO-<,> eller -C1-C4-alkylen-S-CH2CHCH20-, n betyr 0 eller 1 og Q betyr OH -CO eller -S02~.6. Method according to claim 4, characterized in that a fluorine-containing surfactant compound with formula is used in which Rf means straight or branched perfluoroalkyl of 4-20 carbon atoms, R^ is alkyl of 6-24 carbon atoms or a group of formula in which R ^ means alkyl with 3 - 20 carbon atoms and R 22 means hydrogen, halogen, nitro or I^i' m ketyr 0 or 1, s means 5 - 25, Z means -COO-, -SO3~, -0-, - C 2 -C 2 -alkylene-COO-, COOH -C1-C4-alkylene-SO3 , -(^-C^-alkylene-S-C1H-CH^OO-<,> or -C1-C4-alkylene-S-CH2CHCH20-, n means 0 or 1 and Q means OH -CO or -S02~. 7. Fremgangsmåte ifølge krav 6,karakterisert ved at det anvendes en overflateaktiv forbindelse hvor Rf er rettlinjet eller forgrenet perfluoralkyl med 4 - 20 karbonatomer, Rur, betyr alkyl med 6-24 karbonatomer eller en gruppe med formel m og n betyr 0 og s, R2^ og R22 nar den i krav 6 angitte betydning.7. Method according to claim 6, characterized in that a surface-active compound is used where Rf is linear or branched perfluoroalkyl with 4-20 carbon atoms, Rur means alkyl with 6-24 carbon atoms or a group with the formula m and n mean 0 and s, R2^ and R22 when the meaning stated in claim 6. 8. Fremgangsmåte ifølge krav 6, karakterisert ved at det anvendes en fluorholdig overflateaktiv forbindelse med formel hvori Rf, RHC og s har den i krav 6 angitte betydning.8. Method according to claim 6, characterized in that a fluorine-containing surfactant compound with formula is used in which Rf, RHC and s have the meaning specified in claim 6. 9. Vandig overflateaktivt middel for oljeutvinning fra underjordiske oljekilder, karakterisert ved at det inneholder 0,01 - 40 vekt-% av et fluorholdig overflateaktivt middel med formel hvor Rf er en hydrofob-oleofob fluoralifatisk gruppe med 4 - 24 karbonatomer, Z betyr en divalent forbindelsesgruppe, A er et divalent hydrofilt organisk radikal, Q er en divalent forbindelsesgruppe, RHC er et hydrofobt-oleofilt alifatisk radikal med 6-24 karbonatomer eller aralifatisk radikal med minst 9 karbonatomer, og m og n er uavhengig av hverandre 0 eller 1, idet den fluorholdige overflateaktive for bindelse har en oppløselighet i vann ved 30°C på minst 0,01 vekt-%, utøver en overflatespenning på mindre enn 30 dyn/cm ved 0,1 vekt-% aktive forbindelser i avionisert vann og utøver en grenseflatespenning på mindre enn 12 dyn/cm ved 0,1 vekt-% aktive forbindelser i avionisert vann, målt i forhold til cykloheksan og eventuelt et vanlig vannflømmings,.ikke-fluorholdig overflateaktivt middel.9. Aqueous surfactant for oil extraction from underground oil sources, characterized in that it contains 0.01 - 40% by weight of a fluorine-containing surfactant with formula where Rf is a hydrophobic-oleophobic fluoroaliphatic group with 4-24 carbon atoms, Z means a divalent connecting group, A is a divalent hydrophilic organic radical, Q is a divalent connecting group, RHC is a hydrophobic-oleophilic aliphatic radical with 6-24 carbon atoms or araliphatic radical with at least 9 carbon atoms, and m and n are independently 0 or 1, the fluorine-containing surfactant for bond has a solubility in water at 30°C of at least 0.01% by weight, exerts a surface tension of less than 30 dynes/cm at 0.1% by weight of active compounds in deionized water and exerts an interfacial tension of less than 12 dynes /cm at 0.1% by weight active compounds in deionized water, measured in relation to cyclohexane and possibly a common water-flooding, non-fluorine-containing surfactant. 10. Overflateaktivt middel ifølge krav 9, karakterisert ved at det inneholder minst 1 vekt-% av det fluorholdige overflateaktive middel, basert på vekten av ikke-fluorholdig overflateaktivt middel.10. Surfactant according to claim 9, characterized in that it contains at least 1% by weight of the fluorine-containing surfactant, based on the weight of non-fluorine-containing surfactant.
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