Solvent-induced separation of oilfield emulsions

Patent metadata

Field	Value
Publication number	US-10905972-B2
Application number	US-201515545251-A
Country	US
Kind code	B2
Filing date	Feb 27, 2015
Priority date	Feb 27, 2015
Publication date	Feb 2, 2021
Grant date	Feb 2, 2021

Abstract

Systems and methods for separation of oleaginous fluids, aqueous fluids, and solids from drilling or other oilfield emulsions by solvent extraction. A method for separation of oilfield emulsions comprising: providing an oilfield emulsion prepared for use in a wellbore and/or recovered from a wellbore; mixing the oilfield emulsion with at least a solvent to form at least a mixture; and separating the mixture to at least partially recover an oleaginous phase of the oilfield emulsion.

First claim

What is claimed is:

1. A method for separation of oilfield emulsions comprising:
flowing a drilling fluid from a wellbore and recovering the drilling fluid, wherein the drilling fluid comprises an oleaginous continuous phase, a discontinuous phase, and wellbore cuttings;
thereafter, mixing the drilling fluid with at least a solvent to form at least a mixture;
introducing the mixture into a separation column and contacting the mixture with liquid carbon dioxide;
withdrawing a lights overflow stream from the separation column, the lights overflow stream comprising at least a portion of the solvent, at least a portion of the carbon dioxide, at least a portion of the oleaginous continuous phase, and at least a portion of the discontinuous phase; and
separating the light overflow stream and at least partially recovering the oleaginous continuous phase of the drilling fluid.

2. The method of claim 1 wherein the oilfield emulsion comprises a solids-stabilized emulsion.

3. The method of claim 1 wherein the oleaginous continuous phase comprises at least one oleaginous liquid selected from the group consisting of a diesel oil, a crude oil, a paraffin oil, a mineral oil, an olefin, an ester, an amide, an amine, a polyolefin, a polydiorganosiloxane, a siloxane, an organosiloxane, an ether, an acetal, a dialkylcarbonate, a hydrocarbon, and combinations thereof, wherein the volume to volume ratio of the oleaginous continuous phase to the discontinuous phase is in the range of from 20:80 to 95:5.

4. The method of claim 1 wherein the solvent comprises a solvent or mixture of solvents whereby mixing the solvent with the oilfield emulsion breaks a solids-stabilized emulsion in the oilfield emulsion.

5. The method of claim 1 wherein the solvent comprises a paraffinic hydrocarbon having from four carbons to eight carbons.

6. The method of claim 1 wherein the separating the mixture comprises separating the mixture into at least a solids-laden fraction and an oleaginous-solvent fraction.

7. The method of claim 6 wherein the solids-laden fraction comprises barite, and wherein the method further comprising using the barite recovered from the oilfield emulsion in a drilling fluid.

8. The method of claim 6 further comprising separating the solvent oleaginous-fraction into at least a recovered solvent and an oleaginous-enriched phase.

9. The method of claim 1 further comprising, preparing the drilling fluid using at least a portion of the recovered oleaginous phase.

10. The method of claim 1 further comprising mixing the oilfield emulsion with carbon dioxide and recovering and recycling at least a substantial portion of the carbon dioxide and/or the solvent.

11. The method of claim 10 wherein the step of mixing the oilfield emulsion with carbon dioxide comprising counter-currently contacting the mixture of the oilfield emulsion and the solvent with the carbon dioxide.

12. The method of claim 1 further comprising mixing the oilfield emulsion with one or more of a brine, a surfactant, a demulsifying agent, fresh water, steam, a glycerol, a polyol, glycols, or combinations thereof.

13. A method for separation of oilfield emulsions comprising:
introducing an oilfield emulsion and a solvent into a mixing vessel and mixing the oilfield emulsion and the solvent in the mixing vessel to form a mixed fluid, wherein the oilfield emulsion comprises an oleaginous continuous phase, a discontinuous phase, and wellbore cutting solids;
introducing the mixed fluid into a separation column and counter currently contacting the mixed fluid with liquid carbon dioxide; and
withdrawing a lights overflow stream from the separation column, the lights overflow stream comprising at least a portion of the solvent, at least a portion of the carbon dioxide, at least a portion of the oleaginous continuous phase, and at least a portion of the discontinuous phase.

14. The method of claim 13 further comprising introducing the lights overflow stream into a CO 2 flash tank and generating a recovered carbon dioxide stream and a solvent-oleaginous stream.

15. The method of claim 14 further comprising compressing at least a portion of the recovered carbon dioxide stream to form at least a portion of the liquid carbon dioxide.

16. The method of claim 14 further comprising introducing the solvent-oleaginous stream into a solvent flash tank and generating an oleaginous-enriched stream and a recovered solvent stream comprising the solvent.

17. The method of claim 15 wherein the solvent comprises a paraffinic hydrocarbon having from four carbons to eight carbons, wherein the recovered solvent stream is in a gas phase, and wherein the method further comprises compressing the recovered solvent stream to form the solvent stream.

18. The method of claim 13 further comprising withdrawing an underflow stream comprising the wellbore cutting solids.

19. The method of claim 17 wherein the underflow stream comprises residual solvent and wherein the method further comprises recovering at least a portion of the residual solvent by drying and/or degassing the wellbore cutting solids.

Assignees

• Halliburton Energy Services Inc

Inventors

• Harvey Timothy Neal
• Mcdaniel Cato Russell
• Newman Katerina V

Classifications

• B01D17/047 Primary

  with separation aids · CPC title

• C01B32/50

  Carbon dioxide · CPC title

• E21B21/063

  by separating components · CPC title

• B01D17/00 Primary

  Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion (devices for separating or removing fatty or oily substances or similar floating material from water, waste water, or sewage C02F1/40; cleaning or keeping clear the surface of open water from oil or like materials E02B15/04; arrangements for separating lubricants from refrigerants F25B43/02) · CPC title

• E21B43/34 Primary

  Arrangements for separating materials produced by the well · CPC title