Siloxane surfactant additives for oil and gas applications

Patent metadata

Field	Value
Publication number	US-11149189-B2
Application number	US-201615146278-A
Country	US
Kind code	B2
Filing date	May 4, 2016
Priority date	Mar 14, 2013
Publication date	Oct 19, 2021
Grant date	Oct 19, 2021

Abstract

A well treatment additive includes a siloxane surfactant, a solvent and an aqueous phase. The solvent is preferably a terpene hydrocarbon. Also disclosed is a method for using the well treatment additive to form and enhance the properties of terpene solvent based additives useful for the treatment of oil and gas wells. Methods of using the novel well treatment additives include using the additives in a variety of well treatment processes including, but not limited to, acidizing operations, hydraulic fracturing operations, well remediation operations and water removal operations.

First claim

It is claimed:

1. A method of treating a near-wellbore region of a subterranean formation in a well comprising:
providing an additive, wherein the additive is a microemulsion and comprises:
a siloxane surfactant, wherein the siloxane surfactant is present in an amount between about 10 wt % and about 15 wt % versus the total additive and has a formula selected from the following formulas:
(M′R 1 )D a (M′R 1 ) (formula 2), (M′R 1 )D a (M′R 2 ) (formula 3), (M′R 1 )D a (D′R 1 ) b (M′R 1 ) (formula 4), T z (T′R 1 ) c (formula 5), (M′R 1 ) t M u Q v (formula 6), [(D′R 1 )D k ] (formula 7);
wherein “R 1 ” represents an organic radical comprising —(CH 2 ) n —(OCH 2 CH 2 ) x —(OCH(CH 3 )CH 2 ) y —OR 3 , in which “n” is between 3 and about 11, “x” is between 3 and about 30, “y” is between 0 and about 30, and “R 3 ” is selected from the group consisting of —H, -Me, and —OC(O)CH 3 ;
wherein “M” represents Me 3 SiO 1/2 , “D” represents -Me 2 SiO—, “T” represents -MeSiO 3/2 —, “Q” represents —SiO 2 —, “M′R 1 ” represents Me 2 (R 1 )SiO 1/2 —, “M′R 2 ” represents Me 2 (R 2 )SiO 1/2 —, “D′R 1 ” represents -Me(R 1 )SiO—, “T′R 1 ” represents —R 1 SiO 3/2 , and “Me” represents CH 3 ;
wherein for formula 2, “a” is 4-50;
wherein for formula 3, “a” is 0-25 and “R 2 ” is an alkane radical of 1-8 carbon atoms;
wherein for formula 4, “a” is 0-200 and “b” is 1-20;
wherein for formula 5, the ratio of “c”:“z” is 1:7 to 2:6 and the total molecular weight of the siloxane surfactant is less than 7000 Daltons;
wherein for formula 6, the ratio of (“t”+“u”):“v” is from 0.4:1 to 2:1 and the ratio of “t”:“u” is from 1.4 to 1.1, and the total molecular weight of the siloxane surfactant is less than 7000 Daltons; and
wherein for formula 7, “k” is 4-5;

a hydrocarbon surfactant selected from the group consisting of dialkyl sulfosuccinates, ethylene oxide propylene oxide copolymers, sulfonates, carboxylates, amine oxides, primary alkylamines, dialkyl secondary amines, ethoxylated fatty amines, and combinations thereof;
a co-solvent;
a terpene solvent, and
an aqueous phase;

diluting the additive with a carrier fluid to form a diluted additive;
introducing the diluted additive into the well;
allowing the diluted additive to contact the subterranean formation; and
leaving the diluted additive in the well to increase water displacement from the subterranean formation by both oil and gas.

2. The method of claim 1 , wherein the diluted additive is pumped into the well in combination with a proppant during a hydraulic fracturing operation.

3. The method of claim 1 , wherein the diluted additive is pumped into the well at a high rate water pack with a friction reducer.

4. The method of claim 1 , wherein the diluted additive is pumped into the well in combination with a selected acid during an acidizing treatment.

5. The method of claim 1 , wherein the terpene solvent is present in the additive in an amount between about 5 wt % and about 40 wt % versus the total additive.

6. The method of claim 1 , wherein the co-solvent comprises alkyl alcohols containing from 1 to 4 carbon atoms, oligo-oxyalkylenes containing from 1 up to 3 units of ethylene oxide, and oligo-oxyalkylenes containing from 1 up to 3 units of propylene oxide.

7. The method of claim 1 , wherein the siloxane surfactant is a siloxane polyalkylene oxide copolymer.

8. The method of claim 1 , wherein the terpene solvent is present in the additive in an amount between about 10 wt % and about 15 wt % versus the total additive.

9. The method of claim 1 , wherein:
the hydrocarbon surfactant is present in an amount between about 10 wt % and about 35 wt % versus the total additive; and
the terpene solvent is present in an amount between about 5 wt % and about 40 wt % versus the total additive.

10. The method of claim 2 , wherein:
the hydrocarbon surfactant is present in an amount between about 10 wt % and about 35 wt % versus the total additive; and
the terpene solvent is present in an amount between about 5 wt % and about 40 wt % versus the total additive.

11. The method of claim 7 , wherein:
the hydrocarbon surfactant is present in an amount between about 10 wt % and about 35 wt % versus the total additive; and
the terpene solvent is present in an amount between about 5 wt % and about 40 wt % versus the total additive.

Assignees

• Flotek Chemistry Llc

Inventors

• Penny Glenn S
• Dismuke Keith Ingram
• Fox Richard Nelson
• Zelenev Andrei
• Hill Randal M

Classifications

• C09K2208/28

  Friction or drag reducing additives · CPC title

• C09K8/604 Primary

  Polymeric surfactants · CPC title

• C09K8/72

  Eroding chemicals, e.g. acids · CPC title

• C09K8/86

  containing organic compounds · CPC title

• C09K8/885

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