DK2882933T3 - Fremgangsmåde til produktion og fraseparering af olie - Google Patents

Fremgangsmåde til produktion og fraseparering af olie Download PDF

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Publication number
DK2882933T3
DK2882933T3 DK13828607.5T DK13828607T DK2882933T3 DK 2882933 T3 DK2882933 T3 DK 2882933T3 DK 13828607 T DK13828607 T DK 13828607T DK 2882933 T3 DK2882933 T3 DK 2882933T3
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water
oil
formation
ppm
produced
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DK13828607.5T
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English (en)
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Albert Joseph Hendrik Janssen
Bartholomeus Marinus Josephus Maria Suijkerbuijk
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Shell Int Research
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G33/00Dewatering or demulsification of hydrocarbon oils
    • C10G33/04Dewatering or demulsification of hydrocarbon oils with chemical means
    • EFIXED CONSTRUCTIONS
    • E21EARTH OR ROCK DRILLING; MINING
    • E21BEARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16Enhanced recovery methods for obtaining hydrocarbons
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G53/00Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more refining processes
    • C10G53/02Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more refining processes plural serial stages only
    • C10G53/04Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more refining processes plural serial stages only including at least one extraction step
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/02Well-drilling compositions
    • C09K8/03Specific additives for general use in well-drilling compositions
    • C09K8/035Organic additives
    • 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
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/04Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by extraction
    • C10G1/047Hot water or cold water extraction processes
    • EFIXED CONSTRUCTIONS
    • E21EARTH OR ROCK DRILLING; MINING
    • E21BEARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16Enhanced recovery methods for obtaining hydrocarbons
    • E21B43/20Displacing by water
    • EFIXED CONSTRUCTIONS
    • E21EARTH OR ROCK DRILLING; MINING
    • E21BEARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/34Arrangements for separating materials produced by the well
    • E21B43/35Arrangements for separating materials produced by the well specially adapted for separating solids
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10Feedstock materials
    • C10G2300/1033Oil well production fluids
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20Characteristics of the feedstock or the products
    • C10G2300/201Impurities
    • C10G2300/208Sediments, e.g. bottom sediment and water or BSW
    • EFIXED CONSTRUCTIONS
    • E21EARTH OR ROCK DRILLING; MINING
    • E21BEARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/34Arrangements for separating materials produced by the well
    • E21B43/40Separation associated with re-injection of separated materials
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S507/00Earth boring, well treating, and oil field chemistry
    • Y10S507/921Specified breaker component for emulsion or gel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S507/00Earth boring, well treating, and oil field chemistry
    • Y10S507/935Enhanced oil recovery
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S507/00Earth boring, well treating, and oil field chemistry
    • Y10S507/935Enhanced oil recovery
    • Y10S507/936Flooding the formation

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Mining & Mineral Resources (AREA)
  • Geology (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Environmental & Geological Engineering (AREA)
  • Fluid Mechanics (AREA)
  • Geochemistry & Mineralogy (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Wood Science & Technology (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Physical Water Treatments (AREA)

Claims (10)

1. Fremgangsmåde til produktion af olie, der omfatter passage af et saltholdigt kildevand med et samlet indhold af opløste faste stoffer ("TDS") på mere end 5.000 ppm gennem et ionfilter for at producere behandlet vand med reduceret saltindhold i forhold til kildevandet, mens mindst en del af kildevandet udelukkes fra passage gennem ionfilteret for at danne et retentat med øget saltindhold i forhold til kildevandet; anvendelse af mindst en del af det behandlede vand med reduceret saltindhold som mindst en del af et vandigt fluid med en ionstyrke på maksimalt 0,15 M og et samlet indhold af opløste faste stoffer på fra 200 ppm til 10.000 ppm, der indføres i en olieførende formation; produktion afolie og vand fra formationen efter indføring af det vandige fluid i formationen; blanding af en demulgator og en saltvandsopløsning med et samlet indhold af opløste faste stoffer på mere end 10.000 ppm med mindst en del af olien og vandet produceret fra formationen; og separering af olie fra blandingen af olie, vand, demulgator og saltvandsopløsning, hvor mindst en del af retentatet anvendes som mindst en del af saltvandsopløsningen.
2. Fremgangsmåde ifølge krav 1, hvor saltvandsopløsningen har et samlet indhold af opløste faste stoffer på mindst 15.000 ppm, eller mindst 20.000 ppm, eller mindst 25.000 ppm, eller mindst 30.000 ppm, eller mindst 40.000 ppm eller mindst 50.000 ppm.
3. Fremgangsmåde ifølge krav 1 eller 2, der endvidere omfatter trinnet med indføring af et drivfluid i formationen efter indføring af det vandige fluid med lavt saltindhold i formationen.
4. Fremgangsmåde ifølge et hvilket som helst af kravene 1-3, hvor den olieførende formation endvidere omfatter indelukket vand med en divalent ionkoncentration, hvor det vandige fluid med lavt saltindhold har en divalent ionkoncentration, og hvor den divalente ionkoncentration af det vandige fluid er mindre end den divalente ionkoncentration af det indelukkede vand.
5. Fremgangsmåde ifølge et hvilket som helst af kravene 1-4, hvor vandet produceret fra formationen omfatter vand, der er emulgeret med mindst en del af olien produceret fra formationen, og frit vand, der kan frasepareres olien produceret fra formationen uden demulgering, og olie, der er produceret fra formationen, omfatter olie, der er emulgeret med mindst en del af vandet produceret fra formationen og fri olie, der kan frasepareres vandet produceret fra formationen uden demulgering, hvilken fremgangsmåde endvidere omfatter trinnet med separering af det frie vand og den frie olie fra den emulgerede olie og det emulgerede vand før blanding af saltvandsopløsningen med olie og vand produceret fra formationen.
6. Fremgangsmåde ifølge et hvilket som helst af kravene 1-5, der endvidere omfatter følgende trin etablering af kontakt mellem et kildevand med et samlet indhold af opløste faste stoffer på mere end 10.000 ppm og et ionfilter; passage af en del af kildevandet gennem ionfilteret for at danne behandlet vand med reduceret saltindhold i forhold til kildevandet, mens mindst en del af kildevandet udelukkes fra passage gennem ionfilteret for at danne et retentat med øget saltindhold i forhold til kildevandet; anvendelse af det behandlede vand som mindst en del af det vandige fluid indført i formationen; anvendelse af retentatet som mindst en del af saltvandsopløsningen, der blandes med olien og vandet produceret fra formationen.
7. Fremgangsmåde ifølge et hvilket som helst af kravene 1-5, der endvidere omfatter følgende trin: etablering af kontakt mellem en del af et kildevand med et samlet indhold af opløste faste stoffer på mindst 10.000 ppm med et første ionfilter; passage af en del af kildevandet gennem det første ionfilter for at danne et første permeat med reduceret saltindhold i forhold til kildevandet, mens mindst en del af kildevandet, der har været bragt i kontakt med det første ionfilter, udelukkes fra passage gennem det første ionfilter for at danne et første retentat med øget saltindhold i forhold til kildevandet; etablering af kontakt mellem en del af kildevandet og et andet ionfilter; passage af en del af kildevandet gennem det andet ionfilter for at danne et andet permeat med reduceret saltindhold i forhold til kildevandet, mens mindst en del af kildevandet, der har været bragt i kontakt med det andet ionfilter, udelukkes fra passage gennem det andet ionfilter for at danne et andet retentat med øget saltindhold i forhold til kildevandet; anvendelse af det første permeat og det andet permeat som mindst en del af det vandige fluid indsprøjtet i formationen; anvendelse af det første retentat, det andet retentat eller en blanding af det første retentat og det andet retentat som mindst en del af saltvandsopløsningen, der blandes med olien og vandet produceret fra formationen.
8. Fremgangsmåde ifølge krav 7, hvor det første ionfilter er en nanofiltreringsmembran og det andet ionfilter er en omvendt osmosemembran.
9. Fremgangsmåde ifølge et hvilket som helst af kravene 1-8, hvor den olieførende formation er en underjordisk sandstensformation, der omfatter et mineral med et negativt zetapotentiale.
10. Fremgangsmåde ifølge et hvilket som helst af kravene 1-9, hvor den olieførende formation er en underjordisk carbonatformation bestående af mikrokrystallinsk kalksten, dolomit eller en blanding deraf.
DK13828607.5T 2012-08-09 2013-08-07 Fremgangsmåde til produktion og fraseparering af olie DK2882933T3 (da)

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US201261681232P 2012-08-09 2012-08-09
PCT/US2013/053896 WO2014025847A1 (en) 2012-08-09 2013-08-07 Process for producing and separating oil

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US (1) US9540574B2 (da)
EP (1) EP2882933B1 (da)
CN (1) CN104520532B (da)
BR (1) BR112015002736B1 (da)
DK (1) DK2882933T3 (da)
MY (1) MY178145A (da)
RU (1) RU2647524C2 (da)
WO (1) WO2014025847A1 (da)

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CN104520532B (zh) 2017-09-12
BR112015002736A2 (pt) 2017-07-04
MY178145A (en) 2020-10-05
BR112015002736B1 (pt) 2021-05-25
EP2882933A4 (en) 2016-04-27
WO2014025847A1 (en) 2014-02-13
CN104520532A (zh) 2015-04-15
RU2647524C2 (ru) 2018-03-16
EP2882933A1 (en) 2015-06-17
EP2882933B1 (en) 2018-11-28
US20140042058A1 (en) 2014-02-13
RU2015107988A (ru) 2016-09-27

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