Self-breaking retarded acid emulsion

• US 4,140,640 A
• Filed: 07/06/1977
• Issued: 02/20/1979
• Est. Priority Date: 07/06/1977
• Status: Expired due to Term

• Current Assignee: Dowell Schlumberger Incorporated (Schlumberger NV)
• Original Assignee: The Dow Chemical Company (Dow, Inc.)
• Inventors: Scherubel, Gary A.
• Primary Examiner(s): Guynn, Herbert B.
• Application Number:
  US05/813,367
• Time in Patent Office: 594 Days
• Field of Search: 252/8.55 C, 252/8.55 R, 166/307
• US Class Current: 507/244
• CPC Class Codes: C09K 8/72 Eroding chemicals, e.g. acids
• CPC Class Codes: Y10S 507/934 with inhibitor

Abstract

A subterranean formation is acidized with an emulsion comprising an aqueous acidizing solution, an oil, an effective amount each of an alkyl C₈ to C₁₈ primary fatty amine and at least one diethanolamide of at least one C₈ to C₁₈ fatty acid.

Claims

1. In a method of acidizing an acid-soluble subterranean formation by contacting said formation with a retarded aqueous acid solution-in-oil emulsion, said emulsion including an effective retarding amount of at least one alkyl C₈ to C₁₈ primary amine, the improvement which comprises:

including in said emulsion, an effective amount of at least one diethanolamide of at least one C₈ to C₁₈ fatty acid so that said emulsion breaks upon the substantial depletion of the acidizing capacity of the emulsion after contact with the formation.

2. The method of claim 1 wherein the amine is dodecylamine or cocoamine and the amide is the diethanolamide of oleic acid.

3. The method of claim 1 wherein the acid solution is aqueous HCl.

4. The method of claim 3 wherein the concentration of the HCl in the acid solution is greater than 25 percent by weight of the acid solution phase of the emulsion.

5. The method of claim 4 wherein the amine is dodecylamine or cocoamine and the amide is the diethanolamide of oleic acid.

6. A method for stimulating the production of fluids from a subterranean formation, at least part of which is soluble in acid at the temperature of the formation, which comprises contacting said formation with a retarded acidizing emulsion comprising an aqueous acidizing solution dispersed in oil, said emulsion containing by weight of said emulsion, from about 0.01 to about 10 percent a primary C₈ to C₁₈ alkyl amine and from about 0.85 to about 2 parts of at least one diethanolamide of at least one C₈ to C₁₈ fatty acid, per part by weight of said primary amine.

7. The method of claim 6 wherein said amine comprises about 0.05-0.5 percent by weight of said emulsion.

8. The method of claim 7 wherein said amine is cocoamine or dodecylamine.

9. The method of claim 6 wherein from about 1 to about 1.6 parts by weight of said diethanolamide is employed per part by weight of said primary amine.

10. The method of claim 9 wherein the diethanolamide is the diethanolamide of at least one C₁₈ fatty acid.

11. The method of claim 10 wherein the primary amine is cocoamine or dodecylamine, and said amine comprises from about 0.05 to about 0.5 weight percent of said emulsion.

12. The method of claim 6 wherein the acidizing solution is an HCl solution.

13. The method of claim 12 wherein the acidizing solution is greater than 15 weight percent HCl.

14. The method of claim 13 wherein the acidizing solution is greater than 25 weight percent HCl.

15. The method of claim 6 wherein the emulsion comprises about 5 to about 95 percent by volume liquid hydrocarbon.

16. The method of claim 15 wherein the emulsion comprises about 10-50 volume percent liquid hydrocarbon.

17. The method of claim 16 wherein the emulsion comprises about 25-35 volume percent liquid hydrocarbon.

18. The method of claim 6 wherein the emulsion consists substantially of:

about 25-35 volume percent kerosene;

about 75-65 volume percent aqueous HCl having a concentration greater than 15 weight percent HCl;

about 0.05-0.5 weight percent cocoamine or dodecylamine; and

about 1-1.6 parts by weight of the diethanolamide of oleic acid per part of said amine.

19. The method of claim 18 wherein the concentration of HCl is greater than 25 weight percent.

20. The method of claim 18 wherein the temperature of the formation is about 150°

-250°

F.

21. The method of claim 6 wherein the temperature of the formation is at least about 150°

F.

22. The method of claim 6 wherein the emulsion is injected into the formation at a rate and pressure sufficient to fracture said formation.

23. In a composition for acidizing a subterranean formation, said composition being of the aqueous acidizing solution-in-oil emulsion type containing an effective amount of an alkyl C₈ to C₁₈ primary amine to reduce the normal reaction rate of said emulsion, the improvement which comprises:

in said emulsion, an effective amount of at least one diethanolamide of at least one C₈ to C₁₈ fatty acid so that said emulsion substantially completely breaks when the acidizing capacity of the emulsion becomes substantially spent as a result of reaction with such a formation.

24. The composition of claim 23 wherein the amine is dodecylamine or cocoamine and the amide is the diethanolamide of oleic acid.

25. The composition of claim 23 wherein the acid solution is aqueous HCl.

26. The composition of claim 25 wherein the concentration of the HCl in the acid solution is greater than 25 percent by weight of the acid solution phase of the emulsion.

27. The composition of claim 26 wherein the amine is dodecylamine or cocoamine and the amide is the diethanolamide of oleic acid.

28. A retarded acidizing emulsion suitable for use in methods for increasing the permeability of at least partially acid soluble subterranean formations, comprising:

an aqueous acidizing solution dispersed in oil, said emulsion containing by weight of said emulsion, from about 0.01 to about 10 percent a primary C₈ to C₁₈ alkyl amine and from about 0.85 to about 2 parts of at least one diethanolamide of at least one C₈ to C₁₈ fatty acid, per part by weight of said primary amine.

29. The emulsion of claim 28 wherein said amine comprises about 0.05-0.5 percent by weight of said emulsion.

30. The emulsion of claim 29 wherein said amine is cocoamine or dodecylamine.

31. The emulsion of claim 28 wherein from about 1 to about 1.6 parts by weight of said diethanolamide is employed per part by weight of said primary amine.

32. The emulsion of claim 31 wherein the diethanolamide is the diethanolamide of at least one C₁₈ fatty acid.

33. The emulsion of claim 32 wherein the primary amine is cocoamine or dodecylamine, and said amine comprises from about 0.05 to about 0.5 weight percent of said emulsion.

34. The emulsion of claim 28 wherein the acidizing solution is an HCl solution.

35. The emulsion of claim 34 wherein the acidizing solution is greater than 15 weight percent HCl.

36. The emulsion of claim 35 wherein the acidizing solution is greater than 25 weight percent HCl.

37. The emulsion of claim 28 wherein the emulsion comprises about 5 to about 95 percent by volume liquid hydrocarbon.

38. The emulsion of claim 37 wherein the emulsion comprises about 10-50 volume percent liquid hydrocarbon.

39. The emulsion of claim 38 wherein the emulsion comprises about 25-35 volume percent liquid hydrocarbon.

40. The emulsion of claim 28 wherein the emulsion consists substantially of:

about 25-35 volume percent kerosene;

about 75-65 volume aqueous HCl having a concentration greater than 15 weight percent HCl;

about 0.05-0.5 weight percent cocoamine or dodecylamine; and

about 1-1.6 parts by weight of the diethanolamide of oleic acid per part of said amine.

41. The emulsion of claim 40 wherein the concentration of HCl is greater than 25 weight percent.