IP Library Granted Patent US 12686809
Granted Patent B2
US 12686809 · App. 17/538,494 · Granted Jul 21, 2026

Methods and formulations for treating oil-containing porous media for oil recovery

Inventors: Mohammad Piri (Laramie, WY); Youssra Rahham (Laramie, WY); Lamia Goual (Laramie, WY); Maziar Arshadi (Laramie, WY); Morteza Akbarabadi (Laramie, WY)
Assignee: UNIVERSITY OF WYOMING
C09K8/584C09K23/017C09K23/18C09K23/42
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 12686809
App. No.
17/538,494
Granted
Jul 21, 2026
Kind
B2
Abstract

Embodiments of the present disclosure generally relate to methods and formulations for enhanced oil recovery. In an embodiment, a method for treating oil-containing porous media for oil recovery includes introducing oil-containing porous media with a surfactant formulation described herein. Methods can be utilized for, e.g., wettability reversal or oil recovery. Surfactant formulations are also described.

Claims (26)

1 . A method for treating oil-containing porous media for oil recovery, the method comprising:

introducing a surfactant formulation with a reservoir comprising oil-containing porous media, the oil-containing porous media being oil-wet prior to introducing with the surfactant formulation, the surfactant formulation comprising a surfactant A and a surfactant B:

wherein:

at least one surfactant A is present, and for each surfactant A present, each of R 1 , R 2 , and R 3 is methyl, R 4 is an alkyl group having 18 carbon atoms, and X is, independently, bromide or chloride; and

R5 of surfactant B is an alkyl group having 13 carbon atoms, and n of surfactant B is 18;

reversing a wettability of the oil-containing porous media from oil-wet towards water-wet by contacting the oil-containing porous media with the surfactant formulation; and

recovering oil from the oil-containing porous media.

2 . The method of claim 1 , wherein:

at least one surfactant A is present, and each surfactant A present is trimethyloctadecylammonium bromide or trimethyloctadecylammonium chloride.

3 . The method of claim 1 , wherein the method is performed in a tight oil reservoir, in a hydraulically fractured tight oil reservoir, or on a tight porous media.

4 . The method of claim 3 , wherein the method is performed in the hydraulically fractured tight oil reservoir, and the method further comprises, prior to the introducing operation:

creating fractures in rock formations in a tight oil reservoir; and

propping the fractures open by administering a proppant to form the hydraulically fractured tight oil reservoir.

5 . The method of claim 1 , wherein the oil-containing porous media is tight porous media.

6 . The method of claim 1 , wherein a volume ratio of surfactant B to surfactant A in the surfactant formulation is from about 50:50 to about 99:1.

7 . The method of claim 1 , wherein:

the surfactant formulation further comprises brine; and

the method further comprises lowering an interfacial tension between organic phase in the reservoir and aqueous phase present in the surfactant formulation by contacting the oil-containing porous media with the surfactant formulation.

8 . The method of claim 1 , wherein a volume ratio of surfactant B to surfactant A in the surfactant formulation is from about 70:30 to about 99:1.

9 . The method of claim 1 , wherein a total amount of surfactant A and surfactant B is from about 0.01 wt % to about 5 wt % based on a total weight of the surfactant formulation.

10 . The method of claim 1 , wherein:

the surfactant formulation further comprises brine; and

a total amount of surfactant A and surfactant B is from about 0.01 wt % to about 1 wt % based on a total weight of the surfactant formulation.

11 . The method of claim 10 , wherein the brine has a total dissolved solids content from about 100 ppm to about 5,000 ppm.

12 . The method of claim 10 , wherein the brine has a total dissolved solids content from about 10,000 ppm to about 100,000 ppm.

13 . The method of claim 10 , wherein the brine has a total dissolved solids content from about 50,000 ppm to about 1,000,000 ppm.