Methods for hydrocarbon recovery

Patent metadata

Field	Value
Publication number	US-12371606-B2
Application number	US-202418437955-A
Country	US
Kind code	B2
Filing date	Feb 9, 2024
Priority date	Dec 8, 2015
Publication date	Jul 29, 2025
Grant date	Jul 29, 2025

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 water soluble (co) polymers;
one or more hydrophobic liquids;
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 water soluble (co) polymer of from 50 to 15,000 ppm; and
performing an injectivity test on the inverted polymer solution in which the inverted polymer solution exhibits a relative permeability of approximately 1 after 28 pore volumes of the inverted polymer solution is injected into the Bentheimer sandstone core at a flow rate of 0.5 mL/min at a temperature of 31° C., wherein the inverted polymer solution is used in an enhanced oil recovery (EOR) operation.

2. The method of claim 1 , wherein the liquid polymer (LP) composition comprises at least 39% by weight of the one or more water soluble (co) polymers.

3. The method of claim 1 , wherein the liquid polymer (LP) composition comprises an inverse emulsion comprising up to 38% by weight of the one or more water soluble (co) polymers.

4. The method of claim 1 , wherein the one or more water soluble (co) polymers comprise a synthetic (co) polymer.

5. The method of claim 4 , wherein the synthetic (co) polymer comprises polyacrylamide, a partially hydrolyzed polyacrylamide, acrylamide tertiary butyl sulfonic acid, 2-acrylamido-2-methylpropane sulfonic acid, a blend thereof, or a copolymer thereof.

6. The method of claim 4 , wherein the one or more synthetic (co) polymers have a molecular weight of from 15,000,000 g/mol to 30,000,000 g/mol.

7. The method of claim 4 , wherein the one or more synthetic (co) polymers have a molecular weight of from 15,000,000 g/mol to 25,000,000 g/mol.

8. The method of claim 1 , wherein the inverted polymer solution has a filter ratio of 1.5 or less at 15 psi using a 1.2 μm filter.

9. The method of claim 8 , 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.

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

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

12. The method of claim 1 , wherein the inversion of the LP composition comprises a single step.

13. The method of claim 12 , 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.

14. The method of claim 13 , wherein a difference in pressure between the mixer inlet and the mixer outlet is from 15 psi to 400 psi.

15. The method of claim 13 , wherein the in-line mixer comprises a static mixer.

16. The method of claim 13 , wherein the in-line mixer comprises a dynamic mixer.

17. The method of claim 16 , wherein the dynamic mixer comprises an impeller mixer, a turbine mixer, a rotor-stator mixer, a colloid mill, pump, or a pressure homogenizer.

18. The method of claim 16 , wherein the dynamic mixer comprises an electrical submersible pump, hydraulic submersible pump or a progressive cavity pump.

19. The method of claim 1 , wherein the in-line mixer is positioned on the surface, subsurface, subsea, or downhole.

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

21. 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.

22. The method of claim 1 , wherein the aqueous fluid comprises from 15,000 ppm to 100,000 ppm total dissolved solids (tds).

23. 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.

24. The method of claim 1 , wherein when two pore volumes of the inverted polymer solution is injected into a Bentheimer sandstone core at a flow rate of 0.5 mL/min at a temperature of 31° C., a pressure drop for the inverted polymer solution reaches a steady state.

25. The method of claim 1 , wherein the liquid polymer (LP) composition comprises an inverse emulsion comprising up to 35% by weight of the one or more water soluble (co) polymers.

26. The method of claim 1 , wherein the one or more hydrophobic liquids have a boiling point of at least 100° C.

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

• E21B43/20

  Displacing by water · CPC title

• C09K8/584

  characterised by the use of specific surfactants · CPC title

• C09K8/588 Primary

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