Di-alkyl chain surfactants as a main surfactant for enhancing oil recovery for tight oil formations

Patent metadata

Field	Value
Publication number	US-12565618-B2
Application number	US-202318125473-A
Country	US
Kind code	B2
Filing date	Mar 23, 2023
Priority date	Mar 20, 2020
Publication date	Mar 3, 2026
Grant date	Mar 3, 2026

Abstract

Some reservoirs have tight oil formations, such as the Changqing reservoir. The surfactant polymer flooding and low-tension gas flooding are two potential chemical flooding methods for use in tight oil formations. In these methods, an oil displacement agent, or surfactant, is added. Derivatives of nonionic surfactants with extended chains (by propylene oxide and ethylene oxide) from di-alkyl alcohols were developed and tested. A synergistic blend of surfactants was developed between the di-alkyl chain surfactants and a commercially available anionic surfactants that lowers interfacial tension and improves surfactant solubility in high salinity water and oil.

First claim

What is claimed is:

1 . A method of making a di-alkyl surfactant comprising:
reacting a di-alkyl primary alcohol with ethylene oxide and propylene oxide to form a nonionic surfactant; reacting the nonionic surfactant with a base to form a first composition; reacting the first composition with a chloride acid or a salt derivative of a chloride acid to form a second composition; reacting the second composition with a glycol ether to form a third composition; and adding water to the third composition to produce the di-alkyl surfactant.

2 . The method of claim 1 wherein the nonionic surfactant has a formulation of C m H 2m+1 CH(C n H 2n+1 )CH 2 O(PO) x (EO) y H wherein:
m can be 4, 6, 8, 10, 12, 14, 16, 18, 20, 22, or any combination thereof;
n can be 2, 4, 6, 8, 10, 12, 14, 16, 18, 20, or any combination thereof;
x can be from 0-50; and
y can be from 0-30.

3 . The method of claim 1 further comprising:
purging the nonionic surfactant with at least one of nitrogen or a vacuum during the reacting steps.

4 . The method of claim 1 further comprising:
using a condensation trap or a condensation receiver to collect water or organics for reuse.

5 . The method of claim 1 further comprising:
heating the nonionic surfactant to a temperature of less than about 50 degrees Celsius prior to reacting the nonionic surfactant with the base.

6 . The method of claim 1 wherein the base is one or more of potassium hydroxide, sodium hydroxide, sodium methoxide, sodium ethoxide, potassium methoxide, lithium hydroxide, or potassium tert-butoxide.

7 . The method of claim 1 wherein the base is added at a ratio of 1 to 2 moles for every 1 mole of the nonionic surfactant.

8 . The method of claim 1 wherein the reaction with the base occurs at between about 90 degrees Celsius to about 120 degrees Celsius.

9 . The method of claim 1 wherein the salt derivative of a chloride acid is one or more of sodium monochloroacetate or 3-chloro-2-hydroxy-1-propanesulfonic acid sodium salt.

10 . The method of claim 1 wherein the chloride acid is one or more of monochloroacetic acid, chlorosulfonic acid, or 3-chloro-2-hydroxy-1-propanesulfonic acid.

11 . The method of claim 1 wherein the chloride acid or the salt derivative of a chloride acid is added at a ratio of 1-1.9 moles for every 1 mole of the nonionic surfactant.

12 . The method of claim 1 wherein the reaction with the chloride acid or the salt derivative of a chloride acid occurs at about 70-100 degrees Celsius.

13 . The method of claim 1 further comprising:
reacting the chloride acid or the salt derivative of a chloride acid until the free chloride ion of the reaction is in the range of about 1.2-2.7%.

14 . The method of claim 1 wherein the glycol ether is one or more of tetrapropylene glycol monomethyl ether, tripropylene glycol monomethyl ether, tripropylene glycol monoethyl ether, tripropylene glycol dimethyl ether, tripropylene glycol diethyl ether, dipropylene glycol dimethyl ether, dipropylene glycol diethyl ether, dipropylene glycol monomethyl ether, or diethylene glycol monobutyl ether.

15 . The method of claim 1 wherein the glycol ether is added at a 0.5 to 2 mass ratio to the nonionic surfactant.

16 . The method of claim 1 wherein the glycol ether is reacted at about 50-90 degrees Celsius.

17 . The method of claim 1 wherein the water is added at a 0.5 to 2 mass ratio to the nonionic surfactant.

18 . The method of claim 1 wherein the di-alkyl surfactant forms a Type III microemulsion with interfacial tensions of less than 10 −3 mN/m.

19 . The method of claim 18 wherein the Type III microemulsion is formed in fluids with 30,000 to 120,000 ppm of total dissolved solids.

20 . The method of claim 1 wherein the di-alkyl surfactant is a clear, viscous liquid.

Assignees

• Cnpc Usa Corp
• Beijing Huamei Inc
• China Nat Petroleum Corp

Inventors

• Zhou Nancy Chun
• Liu Fuchen
• Lu Meng
• Vaughan Steven

Classifications

• C09K8/584 Primary

  characterised by the use of specific surfactants · CPC title

• C09K23/42 Primary

  Ethers, e.g. polyglycol ethers of alcohols or phenols · CPC title