Metal-mediated viscosity reduction of fluids gelled with viscoelastic surfactants
View Patent ↗Fluids viscosified with viscoelastic surfactants (VESs) may have their viscosities reduced (gels broken) by the direct or indirect action of a composition that contains at least one metal ion source and optionally at least one second source. An optional second source may be a chelating agent where at least one reducing agent source may be additionally optionally used. Another optional component with the metal ion source includes a second, different metal ion source. The breaking composition is believed to directly attack the VES itself, possibly by disaggregating or otherwise attacking the micellar structure of the VES-gelled fluid, and/or possibly by changing the chemical structure of the VES to give two or more products.
1. A method for breaking viscosity of aqueous fluids gelled with a viscoelastic surfactant (VES) comprising adding to an aqueous fluid gelled with at least one amidoamine oxide VES in an amount effective to increase the viscosity of the aqueous fluid, a composition in an amount effective to reduce the viscosity of the gelled aqueous fluid, where the composition comprises from about 0.01 to about 300 ppm, based on the total fluid of at least one transition metal ion source.
2. The method of claim 1 where the composition further comprises at least one chelating agent.
3. The method of claim 2 where the composition further comprises at least one reducing agent source.
4. The method of claim 3 where the reducing agent source is selected from the group consisting of erythorbates, dehydroascorbates, citrates, ascorbates, sulfites, thiols, and alkali metal, alkaline earth metal and ammonium salts thereof.
5. The method of claim 2 where the chelating agent is selected from the group consisting of carboxylic acids, aminocarboxylic acids, polyols, alkanolamines, and combinations thereof.
6. The method of claim 2 where the amount of chelating agent ranges from about 0.1 to about 50 pptg (about 0.012 to about 6 kg/m 3 ), based on the total fluid.
7. The method of claim 1 where the transition metal ion source is a transition metal salt or transition metal complex.
8. The method of claim 7 where the transition metal in the transition metal salt or transition metal complex is a transition metal selected from the group consisting of Groups VA, VIA, VIIA, VIIIA, IB, IIB, IIIB, and IVB of the Periodic Table (previous IUPAC American Group notation).
9. The method of claim 1 where the composition further comprises at least two transition metal ion sources.
10. The method of claim 1 where the composition reduces the viscosity of the gelled aqueous fluid by disaggregating or rearranging a micelle structure of the VES.
11. The method of claim 1 where the composition reduces the viscosity of the gelled aqueous fluid by chemically altering an effective amount of the VES required to increase the viscosity of the aqueous fluid.
12. A method for breaking viscosity of aqueous fluids gelled with a viscoelastic surfactant (VES) comprising adding to an aqueous fluid gelled with at least one amidoamine oside VES in an amount to increase the viscosity of the gelled aqueous fluid, where the composition comprises:
from about 0.01 to about 300 ppm, based on the total fluid of at least one transition metal ion source;
at least one chelating agent; and
at least one reducing agent source;
where the composition reduces the viscosity of the gelled aqueous fluid by a mechanism selected from the group consisting of disaggregating a micelle structure of the VES, rearranging a micelle structure of the VES, chemically altering an effective amount of the VES, and combinations thereof.
13. The method of claim 12 where the transition metal ion source is a transition metal salt or transition metal complex.
14. The method of claim 13 where the transition metal in the transition metal salt or transition metal complex is a transition metal selected from the group consisting of Groups VA, VIA, VIIA, VIIIA, IB, IIB, IIIB, and IVB of the Periodic Table (previous IUPAC American Group notation).
15. The method of claim 12 where the chelating agent is selected from the group consisting of carboxylic acids, aminocarboxylic acids, polyols, alkanolamines, and combinations thereof.
16. The method of claim 12 where the reducing agent source is an organic acid salt selected from the group consisting of erythorbates, dehydroascorbates, citrates, ascorbates, sulfites, thiols, and alkali metal, alkaline earth metal andammonium salts thereof.
17. The method of claim 12 where
the amount of reducing agent source ranges from about 5 to about 50 pptg (about 0.6 to about 6 kg/m 3 ), based on the total fluid; and
the amount of chelating agent ranges from about 0.1 to about 50 pptg (about 0.012 to about 6 kg/m 3 ),
based on the total fluid.
18. An aqueous fluid comprising:
water;
at least one amidoamine oxide viscoelastic surfactant (VES) in an amount effective to increase the viscosity of the aqueous fluid; and
a composition in an amount from about 0.01 to about 300 ppm, based on the total fluid, to reduce the viscosity of the gelled aqueous fluid, where the composition comprises at least one transition metal ion source.
19. The aqueous fluid of claim 18 where the composition further comprises at least one chelating agent.
20. The aqueous fluid of claim 19 where the composition further comprises at least one reducing agent source.
21. The aqueous fluid of claim 20 where the reducing agent source is selected from the group consisting of erythorbates, dehydroascorbates, citrates, ascorbates, sulfites, thiols, and alkali metal, alkaline earth metal and ammonium salts thereof.
22. The aqueous fluid of claim 19 where the chelating agent is selected from the group consisting of carboxylic acids, aminocarboxylic acids, polyols, alkanolamines, and combinations thereof.
23. The aqueous fluid of claim 19 where the amount of chelating agent ranges from about 0.1 to about 50 pptg (about 0.012 to about 6 kg/m 3 ), based on the total fluid.
24. The aqueous fluid of claim 18 where the composition further comprises at least two transition metal ion sources.
25. The aqueous fluid of claim 18 where the composition reduces the viscosity of the gelled aqueous fluid by disaggregating or rearranging a micelle structure of the VES.
26. The aqueous fluid of claim 18 where the composition reduces the viscosity of the gelled aqueous fluid by chemically altering an effective amount of the VES required to increase the viscosity of the aqueous fluid.
27. The aqueous fluid of claim 18 where the transition metal ion source is a transition metal salt or transition metal complex.
28. The aqueous fluid of claim 27 where the transition metal in the transition metal salt or transition metal complex is a transition metal selected from the group consisting of Groups VA, VIA, VIIA, VIIIA, IB, IIB, IIIB, and IVB of the Periodic Table (previous IUPAC American Group notation).
29. An aqueous fluid comprising:
water;
at least one amidoamine oxide viscoelastic surfactant (VES) in an amount effective to increase the viscosity of the aqueous fluid; and
a composition in an amount effective to reduce the viscosity of the gelled aqueous fluid, where the composition comprises:
from about 0.01 to about 300 ppm, based on the total fluid of at least one transition metal ion source;
at least one chelating agent; and
at least one reducing agent source;
where the composition reduces the viscosity of the gelled aqueous fluid by a mechanism selected from the group consisting of disaggregating a micelle structure of the VES, rearranging a micelle structure of the VES, chemically altering an effective amount of the VES, and combinations thereof.
30. The aqueous fluid of claim 29 where the transition metal ion source is a transition metal salt or transition metal complex.
31. The aqueous fluid of claim 29 where the transition metal in the transition metal salt or transition metal complex is a transition metal selected from the group consisting of Groups VA, VIA, VIIA, VIIIA, IB, IIB, IIIB, and IVB of the Periodic Table (previous IUPAC American Group notation).
32. The aqueous fluid of claim 29 where the chelating agent is selected from the group consisting of carboxylic acids, aminocarboxylic acids, polyols, alkanolamines, and combinations thereof.
33. The aqueous fluid of claim 29 where the reducing agent source is an organic acid salt selected from the group consisting of erythorbates, dehydroascorbates, citrates, ascorbates, sulfites, thiols, and alkali metal, alkaline earth metal and ammonium salts thereof.
34. The aqueous fluid of claim 29 where
the amount of reducing agent source ranges from about 5 to about 50 pptg (about 0.6 to about 6 kg/m 3 ), based on the total fluid; and
the amount of chelating agent ranges from about 0.1 to about 50 pptg (about 0.012 to about 6 kg/m 3 ),
based on the total fluid.