Methods for hydrocarbon recovery

Patent metadata

Field	Value
Publication number	US-10822539-B2
Application number	US-201916709872-A
Country	US
Kind code	B2
Filing date	Dec 10, 2019
Priority date	Dec 8, 2015
Publication date	Nov 3, 2020
Grant date	Nov 3, 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 mixing a liquid polymer solution, the method comprising:
(a) providing a liquid polymer (LP) composition comprising:
one or more hydrophobic liquids;
one or more emulsifier surfactants;
one or more inverting surfactants; and
a water soluble (co)polymer; and

(b) mixing the LP composition in an in-line mixer with an aqueous fluid in a single step to generate an inverted polymer solution having a concentration of the (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 pm filter.

2. The method of claim 1 , further comprising injecting the inverted polymer solution into the hydrocarbon reservoir.

3. The method of claim 2 , wherein the inverted polymer solution is used in an enhanced oil recovery (EOR) operation.

4. The method of claim 2 , wherein the inverted polymer solution is used in a hydraulic fracturing operation.

5. 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.

6. The method of claim 1 , wherein the in-line mixer comprises a mixer inlet and a mixer outlet and the pressure difference between the mixer inlet and the mixer outlet is from 15 psi to 400 psi.

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

8. The method of claim 1 , wherein the water soluble (co)polymer comprises a synthetic (co)polymer.

9. The method of claim 8 , 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.

10. The method of claim 1 , wherein the one or more inverting surfactants comprise a surfactant defined by Formula I
R 1 —O—(CH(R 2 )—CH 2 —O) n H (I) Formula I

wherein
R 1 is a C 8 -C 22 -hydrocarbon group;
n is an integer greater than or equal to 4; and
R 2 is, independently for each occurrence, H, methyl or ethyl, with the proviso that at least 50% of the R 2 groups are H.

11. A system for mixing a liquid polymer solution, the system comprising:
(a) a tank for storing a liquid polymer (LP) composition comprising:
one or more hydrophobic liquids;
one or more emulsifier surfactants;
one or more inverting surfactants; and
a water soluble (co)polymer; and

(b) a pump that injects a stream of the LP composition into a line carrying an aqueous fluid stream; and
(c) an inline mixer having a mixer inlet and a mixer outlet, the mixer inlet being in fluid communication with the line to receive the aqueous fluid stream and the stream of the LP composition, wherein the inline mixer mixes the LP composition with the aqueous fluid in a single step to generate an inverted polymer solution having a concentration of the (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 pm filter.

12. The system of claim 11 , wherein the inline mixer is a dynamic mixer.

13. The system of claim 12 , wherein the dynamic mixer comprises an impeller mixer, a turbine mixer, a rotor-stator mixer, a colloid mill, pump, or a pressure homogenizer.

14. The system of claim 12 , wherein the dynamic mixer comprises an electrical submersible pump, a hydraulic submersible pump, or a progressive cavity pump.

15. The system of claim 11 , wherein the inline mixer is a static mixer.

16. The system of claim 11 , wherein the pressure difference between the mixer inlet and the mixer outlet is from 15 psi to 400 psi.

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

18. The system of claim 11 , wherein the water soluble (co)polymer comprises a synthetic (co)polymer.

19. The system of claim 18 , 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.

20. The system of claim 11 , wherein the one or more inverting surfactants comprise a surfactant defined by Formula I
R 1 —O—(CH(R 2 )—CH 2 —O) n H (I) Formula I

wherein
R 1 is a C 8 -C 22 -hydrocarbon group;
n is an integer greater than or equal to 4; and
R 2 is, independently for each occurrence, H, methyl or ethyl, with the proviso that at least 50% of the R 2 groups are H.

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

• E21B43/26

  by forming crevices or fractures · CPC title

• C09K8/584

  characterised by the use of specific surfactants · CPC title

• E21B43/20

  Displacing by water · CPC title

• C09K8/588 Primary

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

• C09K8/882

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