Methods for hydrocarbon recovery

Patent metadata

Field	Value
Publication number	US-10619087-B2
Application number	US-201615372170-A
Country	US
Kind code	B2
Filing date	Dec 7, 2016
Priority date	Dec 8, 2015
Publication date	Apr 14, 2020
Grant date	Apr 14, 2020

Abstract

Provided herein are liquid polymer (LP) compositions comprising a synthetic (co)polymer (e.g., an acrylamide (co)polymer), as well as methods for preparing inverted polymer solutions by inverting these LP compositions in an aqueous fluid. The resulting inverted polymer solutions can have a concentration of a synthetic (co)polymer (e.g., an acrylamide (co)polymer) of from 50 to 15,000 ppm, and a filter ratio of 1.5 or less at 15 psi using a 1.2 μm filter. Also provided are methods of using these inverted polymer solutions in oil and gas operations, including enhanced oil recovery.

First claim

What is claimed is:

1. A method for preparing an inverted polymer solution comprising
providing a liquid polymer (LP) composition comprising:
one or more hydrophobic liquids having a boiling point of at least 100° C.;
at least 39% by weight of one or more synthetic (co)polymers;
one or more emulsifier surfactants; and
one or more inverting surfactants;

inverting the LP composition in an aqueous fluid to provide an inverted polymer solution having a concentration of synthetic (co)polymer of from 50 to 15,000 ppm;
wherein the inverted polymer solution has a filter ratio of 1.5 or less at 15 psi using a 1.2 μm filter; and
wherein the inverted polymer solution is used in a hydraulic fracturing operation, as a drag reducer that reduces friction during transportation of a fluid in a pipeline, or any combination thereof.

2. The method of claim 1 , wherein the inverted polymer solution has a filter ratio of from 1.1 to 1.3 at 15 psi using the 1.2 μm filter.

3. The method of claim 1 , wherein the inversion of the LP composition forms the inverted polymer solution in 30 minutes or less.

4. The method of claim 1 , wherein the inversion of the LP composition comprises a continuous process.

5. The method of claim 1 , wherein the inversion of the LP composition comprises a single step, and wherein the single step comprises diluting the LP composition in the aqueous fluid in an in-line mixer having a mixer inlet and a mixer outlet to provide the inverted polymer solution.

6. The method of claim 5 , wherein the difference in pressure between the mixer inlet and the mixer outlet is from 15 psi to 400 psi.

7. The method of claim 5 , wherein the in-line mixer is positioned on the surface, subsurface, subsea, or downhole.

8. The method of claim 1 , wherein the inversion of the LP composition comprises multiple steps.

9. The method of claim 8 , wherein the inversion of the LP composition comprises;
as a first step, inverting the LP composition in the aqueous fluid in a first in-line mixer having a first mixer inlet and a first mixer outlet to provide a concentrated polymer composition having a concentration of synthetic (co)polymer of up to 15,000 ppm; and
as a second step, diluting the concentrated polymer composition in the aqueous fluid in a second in-line mixer having a second mixer inlet and a second mixer outlet to provide the inverted polymer solution.

10. The method of claim 9 , wherein the difference in pressure between the first mixer inlet and the first mixer outlet is from 15 psi to 400 psi.

11. The method of claim 9 , wherein the first in-line mixer is positioned on the surface, subsurface, subsea, or downhole.

12. The method of claim 9 , wherein the difference in pressure between the second mixer inlet and the second mixer outlet is from 15 psi to 400 psi.

13. The method of claim 9 , wherein the second in-line mixer is positioned on the surface, subsurface, subsea, or downhole.

14. The method of claim 1 , wherein the aqueous fluid comprises soft brine or hard brine.

15. The method of claim 1 , wherein the aqueous fluid comprises produced reservoir brine, reservoir brine, sea water, fresh water, produced water, water, saltwater, brine, synthetic brine, synthetic seawater brine, or any combination thereof.

16. The method of claim 1 , wherein the aqueous fluid further comprises a surfactant, an alkalinity agent, a co-solvent, a chelating agent, or any combination thereof.

17. The method of claim 1 , wherein the inversion of the LP composition comprises parallel single steps, parallel multiple steps, or any combination thereof.

18. The method of claim 17 , wherein the parallel single steps, parallel multiple steps, or any combination thereof include using at least one in-line mixer for diluting the LP composition in the aqueous fluid, the in-line mixer having a mixer inlet and a mixer outlet to provide the inverted polymer solution.

19. The method of claim 18 , wherein the difference in pressure between the mixer inlet and the mixer outlet is from 15 psi to 400 psi.

20. The method of claim 18 , wherein the in-line mixer is positioned on the surface, subsurface, subsea, or downhole.

21. The method of claim 1 , wherein the one or more synthetic (co)polymers comprise one or more acrylamide (co)polymers.

22. The method of claim 1 , wherein the inverted polymer solution is used as a hydraulic fracturing fluid.

23. The method of claim 1 , wherein the inverted polymer solution is included in a hydraulic fracturing fluid.

24. The method of claim 1 , wherein the inverted polymer solution is used as a drag reducer that reduces friction during transportation of a fluid in a pipeline.

25. The method of claim 1 , wherein the inverted polymer solution is included in a drag reducer, wherein the drag reducer reduces friction during transportation of a fluid in a pipeline.

26. A method for preparing an inverted polymer solution comprising
providing a liquid polymer (LP) composition in the form of an inverse emulsion comprising:
one or more hydrophobic liquids having a boiling point of at least 100° C.;
up to 35% by weight of one or more synthetic (co)polymers;
one or more emulsifier surfactants; and
one or more inverting surfactants;

inverting the LP composition in an aqueous fluid to provide an inverted polymer solution having a concentration of synthetic (co)polymer of from 50 to 15,000 ppm;
wherein the inverted polymer solution has a filter ratio of 1.5 or less at 15 psi using a 1.2 μm filter; and
wherein the inverted polymer solution is used in a hydraulic fracturing operation, as a drag reducer that reduces friction during transportation of a fluid in a pipeline, or any combination thereof.

27. A method for hydraulic fracturing, comprising:
(a) providing a subsurface reservoir containing hydrocarbons there within;
(b) providing a wellbore in fluid communication with the subsurface reservoir;
(c) providing a liquid polymer (LP) composition comprising:
one or more hydrophobic liquids having a boiling point of at least 100° C.;
at least 39% by weight of one or more synthetic (co)polymers;
one or more emulsifier surfactants; and
one or more inverting surfactants; and

(d) inverting the LP composition in an aqueous fluid to provide an inverted polymer solution having a concentration of synthetic (co)polymer of from 50 to 15,000 ppm; wherein the inverted polymer solution has a filter ratio of 1.5 or less at 15 psi using a 1.2 μm filter
(e) injecting the inverted polymer solution through the wellbore into the subsurface reservoir,
wherein the inverted polymer solution is used in a hydraulic fracturing operation, as a drag reducer that reduces friction during transportation of a fluid in a pipeline, or any combination thereof.

Assignees

• Chevron Usa Inc

Inventors

• Kim Do Hoon
• Alexis Dennis Arun
• Dwarakanath Varadarajan
• Espinosa David
• Malik Taimur
• Jackson Logan
• Lynch Tom
• Robinson Ronald
• Fournier Frances
• Yang Hong
• Aujla Sukhjit

Classifications

• C09K8/588 Primary

  characterised by the use of specific polymers {(polymeric surfactants C09K8/584)} · CPC title

• C09K8/584

  characterised by the use of specific surfactants · CPC title

• E21B43/20

  Displacing by water · CPC title

• C09K8/68

  containing organic compounds · CPC title

• C09K8/882

  obtained by reactions only involving carbon-to-carbon unsaturated bonds · CPC title