Treatment of produced water with seeded evaporator

US10221670B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10221670-B2
Application numberUS-201314428138-A
CountryUS
Kind codeB2
Filing dateAug 19, 2013
Priority dateSep 13, 2012
Publication dateMar 5, 2019
Grant dateMar 5, 2019

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

Produced water, for example from a steam assisted gravity drainage (SAGD) or cyclic steam stimulation (CSS) heavy oil recovery operation, is treated to recover water that is re-used to create steam. The produced water is treated in one or more thermal treatment devices such as an evaporator and a crystallizer. The thermal treatment device is seeded, for example with a calcium or magnesium salt. The thermal treatment device produces a blowdown or slurry comprising super-saturated solids and organic compounds. A solvent is added to the blowdown or slurry. The solids precipitate and are separated from the blowdown or slurry. The solvent may be recovered for re-use in treating more blowdown or slurry.

First claim

Opening claim text (preview).

What is claimed is: 1. A process for extracting oil, the process comprising the steps of: a) producing steam; b) injecting the steam into a formation comprising oil; c) withdrawing a mixture of water and oil from the formation; d) separating produced water from the mixture of water and oil; e) treating the produced water at least in a seeded evaporator to produce a distillate and a blowdown; f) using the distillate to produce additional steam for injection into the formation; g) mixing a solvent with the blowdown; h) after step g), separating precipitated solids comprising one or more salts from the blowdown; and i) recovering at least some of the solvent from the mixture with the blowdown, and mixing recovered solvent with additional blowdown from the seeded evaporator. 2. The process of claim 1 , wherein the oil is heavy oil or bitumen. 3. The process of claim 1 , wherein steps a), b), and c) are part of a steam assisted gravity drainage (SAGD) or cyclic steam stimulation (CSS) operation. 4. The process claim 1 , wherein step e) comprises treating the produced water with the seeded evaporator to produce an evaporator blowdown and treating the evaporator blowdown in a crystallizer to produce the blowdown. 5. The process of claim 1 , wherein the solvent comprises Diisopropylamine (DIPA). 6. The process of claim 1 , wherein the precipitated solids further comprise silica. 7. The process of claim 1 , further comprising a step of removing the blowdown from the process after the steps of recovering solvent and separating precipitated solids. 8. The process of claim 1 , further comprising treating organic compounds in the blowdown and returning treated blowdown to the process at or upstream of step e). 9. A method for treating a mixture having water, one or more salts in solution and one or more organic compounds, the method comprising the steps of, a) treating the mixture in an evaporator to produce a concentrate; b) adding a source of ions to the concentrate in the evaporator to form a seeded concentrate; c) mixing the seeded concentrate with a solvent; d) removing precipitates of the one or more salts and one or more organic compounds from the seeded concentrate; and e) recovering at least some of the solvent from the mixture of concentrate and solvent. 10. The method of claim 9 , further comprising a step of mixing recovered solvent with additional concentrate. 11. The method of claim 9 , wherein the water comprises produced water. 12. The method of claim 11 , wherein the produced water is extracted from a heavy oil containing formation after injecting steam into the formation. 13. The method of claim 9 , wherein the concentrate comprises blowdown from two or more thermal treatment devices that include the evaporator. 14. The method of claim 13 , wherein the thermal treatment devices comprise the evaporator and a crystallizer. 15. The method of claim 9 , further comprising a step of treating at least some of the seeded concentrate after step d) to oxidize or remove organic compounds and returning the treated seeded concentrate to step a). 16. An apparatus for treating produced water, the apparatus comprising: a) a seeded evaporator to treat the produced water and produce a blowdown stream; b) a solvent mixing vessel, the solvent mixing vessel in communication with the blowdown stream; c) a solvent feeding system in communication with the solvent mixing vessel; d) a solid-liquid separation device; and e) a solvent recovery system downstream of the solvent mixing vessel. 17. The apparatus of claim 16 , wherein the solid-liquid separation device is incorporated with, or downstream of, the solvent mixing vessel. 18. The apparatus of claim 16 , wherein the apparatus comprises two or more thermal treatment devices in series that includes the seeded evaporator. 19. The apparatus of claim 18 , wherein the two or more thermal treatment devices comprise the evaporator and a crystallizer. 20. The apparatus of claim 16 , further comprising a treatment system configured to oxidize or remove organic compounds downstream of the solvent recovery system. 21. A process for treating produced water from heavy oil extraction, the process comprising the steps of: a) de-oiling the produced water; b) treating the de-oiled produced water in a seeded evaporator to produce an evaporator blowdown; c) adding a solvent to the blowdown; d) separating solids from the blowdown; and e) after step d), recovering solvent from the blowdown. 22. The process of claim 21 , further comprising a step of treating the blowdown to remove or oxidize one or more organic compounds in the blowdown and returning treated blowdown to, or upstream of, step b).

Assignees

Inventors

Classifications

  • from quarries or from mining activities · CPC title

  • SAGD in combination with other methods · CPC title

  • E21B43/24Primary

    using heat, e.g. steam injection · CPC title

  • by flocculation or precipitation of suspended impurities {(C02F1/463 takes precedence)} · CPC title

  • Purification of waste water by evaporation · CPC title

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What does patent US10221670B2 cover?
Produced water, for example from a steam assisted gravity drainage (SAGD) or cyclic steam stimulation (CSS) heavy oil recovery operation, is treated to recover water that is re-used to create steam. The produced water is treated in one or more thermal treatment devices such as an evaporator and a crystallizer. The thermal treatment device is seeded, for example with a calcium or magnesium salt.…
Who is the assignee on this patent?
Bl Technologies Inc
What technology area does this patent fall under?
Primary CPC classification E21B43/24. Mapped technology areas include Fixed Constructions.
When was this patent published?
Publication date Tue Mar 05 2019 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 3 related publications on this page (citations in our corpus or others sharing the same primary CPC).