DK178809B1 - Proces til udvinding af carbonhydrid - Google Patents

Proces til udvinding af carbonhydrid Download PDF

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Publication number
DK178809B1
DK178809B1 DKPA200900353A DKPA200900353A DK178809B1 DK 178809 B1 DK178809 B1 DK 178809B1 DK PA200900353 A DKPA200900353 A DK PA200900353A DK PA200900353 A DKPA200900353 A DK PA200900353A DK 178809 B1 DK178809 B1 DK 178809B1
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DK
Denmark
Prior art keywords
displacement fluid
water
aqueous displacement
content
multivalent cation
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Application number
DKPA200900353A
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English (en)
Inventor
Gary Russell Jerauld
Arnaud Lager
Patrick Lee Mcguire
Kevin Webb
Ian Ralph Collins
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Bp Exploration Operating
Bp Corp North America Inc
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Publication date
Application filed by Bp Exploration Operating, Bp Corp North America Inc filed Critical Bp Exploration Operating
Publication of DK200900353A publication Critical patent/DK200900353A/da
Priority to DKPA201570687A priority Critical patent/DK179973B1/da
Application granted granted Critical
Publication of DK178809B1 publication Critical patent/DK178809B1/da

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    • 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
    • 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
    • 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
    • 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
    • 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
    • Y10S507/904Process of making fluids or additives therefor
    • 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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  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mining & Mineral Resources (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Environmental & Geological Engineering (AREA)
  • Fluid Mechanics (AREA)
  • Materials Engineering (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

Carbonhydrider udvindes fra underjordiske formationer ved vandfyldning. Fremgangsmåden omfatter, at en vandig fortrængningsvæske via en injektionsbrønd føres gennem en porøs og permeabel sandstensformation til frigivelse af olie og udvinding af den frigivne olie fra en produktionsbrønd beliggende med afstand til injektionsbrønden, hvor (a) sandstensformationen omfatter mindst ét mineral med et negativt zeta-potentiale under formationsbetingelserne; (b) olie og connatvand er til stede i formationens porer; og (c) fraktionen af indholdet af divalent kation i den vandige fortræng ningsvæske i forhold til indholdet af divalent kation i connatvandet er mindre end 1.

Claims (22)

1. Fremgangsmåde til forøgelse af udvindingen af råolie fra et reservoir indeholdende mindst én porøs og permeabel underjordisk formation, hvor formationen indeholder sandstensklippe og mindst ét mineral, der har et negativt zeta-potentiale under reservoirbetingelserne, og hvor råolie og connatvand er til stede i formationens porer, hvilken fremgangsmåde omfatter: (A) injektion i formationen af en væskelomme af en vandig fortrængningsvæske, der fortrænger råolie fra overfladen af formationens porer, hvor porevolumenet (PV) af væskelommen af den vandige fortrængningsvæske er mindst 0,3 og mindre end 1, og den vandige fortrængningsvæske har et totalt indhold af opløste faste stoffer (TDS) i intervallet fra 200 til 10.000 ppm, og fraktionen af det totale indhold af multivalent kation i den vandige fortrængningsvæske i forhold til det totale indhold af multivalent kation i connatvandet er mindre end 1; og (B) efterfølgende injektion i formationen af et drivvand med højere indhold af multivalent kation og/eller højere totalt indhold af opløste faste stoffer end den vandige fortrængningsvæske.
2. Fremgangsmåde ifølge krav 1, ved hvilken fraktionen af det totale indhold af multivalent kation i den vandige fortrængningsvæske i forhold til det totale indhold af multivalent kation i connatvandet er mindst 0,01.
3. Fremgangsmåde ifølge krav 2, ved hvilken fraktionen af det totale indhold af multivalent kation i connatvandet er mindst 0,05.
4. Fremgangsmåde ifølge ethvert af de foregående krav, ved hvilken porevolumenet af den vandige fortrængningsvæske er mindst 0,4 PV.
5. Fremgangsmåde ifølge ethvert af de foregående krav, ved hvilken porevolumenet af den vandige fortrængningsvæske er mindre end 0,9 PV.
6. Fremgangsmåde ifølge krav 5, ved hvilken porevolumenet af den vandige fortrængningsvæske er mindre end 0,8 PV.
7. Fremgangsmåde ifølge krav 6, ved hvilken porevolumenet af den vandige fortrængningsvæske er mindre end 0,6 PV.
8. Fremgangsmåde ifølge krav 7, ved hvilken porevolumenet af den vandige fortrængningsvæske er mindre end 0,5 PV.
9. Fremgangsmåde ifølge krav 1 eller 2, ved hvilken den vandige fortrængningsvæske har et porevolumen i intervallet fra 0,3 til 0,6.
10. Fremgangsmåde ifølge krav 9, ved hvilken den vandige fortrængningsvæske har et porevolumen i intervallet fra 0,3 til 0,45.
11. Fremgangsmåde ifølge ethvert af de foregående krav, ved hvilken den vandige fortrængningsvæske injiceres i formationen under sekundær udvinding eller tertiær udvinding.
12. Fremgangsmåde ifølge ethvert af de foregående krav, ved hvilken den vandige fortrængningsvæske ledes gennem formationen fra en injektionsbrønd til fortrængning af råolie fra overfladen af formationens porer, og den fortrængte råolie udvindes fra en produktionsbrønd beliggende med afstand fra injektionsbrønden.
13. Fremgangsmåde ifølge ethvert af de foregående krav, ved hvilken drivvandet er valgt fra havvand og/eller produktionsvand.
14. Fremgangsmåde ifølge ethvert af de foregående krav, ved hvilken den vandige fortrængningsvæske er valgt ved: (i) bestemmelse af indholdet af multivalent kation i connatvandet; og (ii) udvælgelse af en vandig fortrængningsvæske med et totalt indhold af opløste faste stoffer (TDS) i intervallet fra 200 til 10.000 ppm og med et sådant indhold af multivalent kation, at fraktionen af det totale indhold af multivalent kation i injektionsvandet i forhold til det totale indhold af multivalent kation i connatvandet er mindre end 1, hvor den vandige fortrængningsvæske er (i) enten et ubehandlet vand med det ønskede TDS-indhold og det ønskede totale indhold af multivalent kation eller (ii) et behandlet vand, der er blevet indstillet således, at det har det ønskede TDS-indhold og det ønskede totale indhold af multivalent kation.
15. Fremgangsmåde ifølge ethvert af de foregående krav, ved hvilken zeta-potentialet af mineralet er fra -0,1 til -50 mV under reservoirbetingelserne.
16. Fremgangsmåde ifølge ethvert af de foregående krav, ved hvilken mineralet er til stede i formationen i en mængde i intervallet fra 1 til 30 vægt-%.
17. Fremgangsmåde ifølge ethvert af de foregående krav, ved hvilken fraktionen af det totale indhold af multivalent kation i den vandige fortrængningsvæske i forhold til det totale indhold af multivalent kation i connatvandet er mindre end 0,8.
18. Fremgangsmåde ifølge krav 17, ved hvilken fraktionen af det totale indhold af multivalent kation i den vandige fortrængningsvæske i forhold til det totale indhold af multivalent kation i connatvandet er mindre end 0,6.
19. Fremgangsmåde ifølge krav 18, ved hvilken fraktionen af det totale indhold af multivalent kation i den vandige fortrængningsvæske i forhold til det totale indhold af multivalent kation i connatvandet er mindre end 0,5.
20. Fremgangsmåde ifølge ethvert af de foregående krav, ved hvilken den vandige fortrængningsvæske er et ubehandlet ferskvand eller et ubehandlet grundvand.
21. Fremgangsmåde ifølge ethvert af de foregående krav, ved hvilken den vandige fortrængningsvæske er dannet ved formindskelse af indholdet af multivalent kation i et kildevand, hvor kildevandet har et TDS i det ønskede interval fra 200 til 10.000 ppm.
22. Fremgangsmåde ifølge ethvert af de foregående krav, ved hvilken den vandige fortrængningsvæske er dannet ud fra et kildevand med højt saltindhold med højt indhold af multivalent kation under anvendelse af omvendt osmose, fremadrettet osmose eller kombinationer deraf.
DKPA200900353A 2006-09-08 2009-03-13 Proces til udvinding af carbonhydrid DK178809B1 (da)

Priority Applications (1)

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DKPA201570687A DK179973B1 (da) 2006-09-08 2015-10-22 Hydrocarbon recovery process

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US84300006P 2006-09-08 2006-09-08
PCT/GB2007/003337 WO2008029124A1 (en) 2006-09-08 2007-09-05 Hydrocarbon recovery process

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US (2) US7987907B2 (da)
CN (2) CN101535443B (da)
AR (1) AR062716A1 (da)
AU (1) AU2007293281B2 (da)
BR (1) BRPI0716508B1 (da)
CA (1) CA2662295C (da)
DK (2) DK178809B1 (da)
EA (1) EA015208B1 (da)
EG (1) EG26795A (da)
GB (2) GB2455016B (da)
MX (1) MX2009002513A (da)
NO (1) NO343975B1 (da)
WO (1) WO2008029124A1 (da)

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