IP Library Granted Patent US 9,133,386
Granted Patent B2
US 9,133,386 · App. 13/712,539 · Granted Sep 15, 2015

Viscous settable fluid for lost circulation in subterranean formations

Inventors: Arunesh Kumar (London, GB); Sharath Savari (Kingwood, TX); Jason T. Scorsone (Houston, TX); Rajendra A. Kalgaonkar (Pune, IN)
Assignee: Hallburton Energy Services, Inc.
C09K8/512C04B28/14C04B28/26C09K8/467C09K8/487C09K8/5045E21B21/003C04B2103/10C04B2103/445C04B2111/00008C04B2111/00146C09K2208/10
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Quick Facts
Patent No.
US 9,133,386
App. No.
13/712,539
Granted
Sep 15, 2015
Kind
B2
Abstract

A method of treating a well the method including the steps of: (A) forming a fluid including: (i) a shear-thinning aqueous liquid phase; and (ii) an inorganic setting material; wherein the fluid is shear-thinning, pumpable, and settable; and (B) introducing the fluid into the well.

Claims (32)

1. A method of treating a well, the method comprising the steps of:

(A) forming a fluid comprising:

(i) a shear-thinning aqueous liquid phase, wherein the shear-thinning aqueous liquid phase comprises a nano-particulate dispersed therein;

(ii) an inorganic setting material; and

(iii) a water-soluble chemical activator selected from the group consisting of: (a) phytic acid, an alkali metal salt or ammonium salt thereof; (b) methylglycinediacetic acid, an alkali metal salt or ammonium salt thereof; (c) a water-soluble polyepoxysuccinic acid, an alkali metal salt or ammonium salt thereof; and (d) salicylic acid, ascorbic acid, tannic acid, and an alkali metal salt or ammonium salt of any of the foregoing;

wherein the fluid is shear-thinning, pumpable, and settable; and

(B) introducing the fluid into the well.

2. The method according to claim 1 , wherein the fluid forms a solid within at most 0.5 hours at a temperature as least as high as a design temperature for the method.

3. The method according to claim 1 , wherein the shear-thinning aqueous liquid phase comprises a viscosity-increasing agent, and a crosslinking agent.

4. The method according to claim 3 , wherein the viscosity-increasing agent is selected from the group consisting of: a water-soluble polysaccharide, a water-soluble polysaccharide derivative, and any combination thereof.

5. The method according to claim 4 , wherein the viscosity-increasing agent comprises a guar derivative.

6. The method according to claim 4 , wherein the cross-linking agent is a borate compound.

7. The method according to claim 3 , wherein the shear-thinning aqueous liquid phase has a pH greater than 8.

8. The method according to claim 3 , wherein the shear-thinning aqueous liquid phase comprises a water-soluble inorganic salt.

9. The method according to claim 1 , wherein the nano-particulate comprises a silica.

10. The method according to claim 9 , wherein the shear-thinning aqueous liquid phase has a pH greater than 8.

11. The method according to claim 9 , wherein the shear-thinning aqueous liquid phase comprises a water-soluble inorganic salt.

12. The method according to claim 9 , wherein the shear-thinning aqueous liquid phase has an ionic strength less than 0.75.

13. The method according to claim 1 , wherein the inorganic setting material comprises a non-hydraulic cement.

14. The method according to claim 1 , wherein the inorganic setting material is selected from the group consisting of: calcium sulfate, a water-soluble silicate, and any combination thereof.

15. The method according to claim 1 , additionally comprising a lost-circulation material.

16. The method according to claim 15 , wherein the lost-circulation material is selected from the group consisting of: marble, calcium carbonate, calcium magnesium carbonate, walnut shells, graphites, fibers, cellulosic materials, and any combination thereof.

17. The method according to claim 15 , wherein the lost-circulation material has a particulate size of at least 5 microns.

18. The method according to claim 1 , wherein the fluid does not include fibers.

19. The method according to claim 1 , wherein the fluid is introduced into a zone of the well from which there is greater than 100 barrels per hour lost circulation or no return.

20. The method according to claim 1 , wherein the fluid is introduced into the well during drilling without tripping out a drill string.

21. The method according to claim 1 , wherein the fluid is introduced through a drill string or bottom hole assembly.

22. The method according to claim 1 , wherein the fluid is introduced into the well without simultaneously introducing another fluid into the well.

23. The method according to claim 1 , wherein the shear-thinning aqueous liquid phase has at least 25% by weight of the nano-particulate dispersed therein.

24. The method according to claim 1 , wherein the inorganic setting material comprises a water-soluble silicate.

25. The method according to claim 1 , wherein the inorganic setting material comprises calcium sulfate.

26. method according to claim 1 , wherein the shear-thinning aqueous liquid phase has at least 7.5% by weight of the nano-particulate dispersed therein.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 12, 2012
From: KUMAR, ARUNESH; SAVARI, SHARATH; SCORSONE, JASON T; KALGAONKAR, RAJENDRA A
To: HALLIBURTON ENERGY SERVICES, INC.
Reel/Frame 029456/0194 →
Continuity (1)
Related Publication 20140158354A1 · Jun 12, 2014