High solids content slurry methods and systems

• US 8,511,381 B2
• Filed: 06/30/2010
• Issued: 08/20/2013
• Est. Priority Date: 06/30/2010
• Status: Expired due to Fees

• Current Assignee: Schlumberger Technology Corporation (Schlumberger NV)
• Original Assignee: Schlumberger Technology Corporation (Schlumberger NV)
• Inventors: Panga, Mohan K. R., Gadiyar, Balkrishna, Drochon, Bruno, Still, John W.
• Primary Examiner(s): SUCHFIELD, GEORGE A
• Application Number:
  US12/827,853
• Publication Number:
  US 20120000653A1
• Time in Patent Office: 1,147 Days
• Field of Search: None
• US Class Current: 166/278
• CPC Class Codes: C09K 8/80 Compositions for reinforcing fractures, e.g. compositions of proppants used to keep the fractures open
• CPC Class Codes: E21B 43/04 Gravelling of wells
• CPC Class Codes: E21B 43/267 reinforcing fractures by propping

Abstract

A system and method are disclosed for low damage gravel packing. The system comprises a well bore; a gravel packing slurry comprising a carrier fluid and a solids mixture, wherein the solids mixture comprises a plurality of volume-averaged particle size distribution (PSD) modes such that a packed volume fraction (PVF) exceeds 0.75, wherein the solids mixture comprises at least a proppant PSD mode and a fines PSD mode; a pump to circulate the slurry in the wellbore and form a proppant pack; and a dispersant source effective to facilitate fines flowback from the pack. The method comprises circulating the slurry through a wellbore to form a proppant pack; contacting fines in the pack with a dispersant; and passing fluid through the pack to remove fines from the pack. Dispersants disclosed as present in the slurry or in another treatment fluid include polyelectrolyte, polysulfonate, polycarboxylate, lignosulfonates, polymelamine sulfonates, polystyrene sulfonates, polynaphthalene sulfonates, polyacrylates having a weight average molecular weight less than 10,000 Daltons, anionic, cationic, amphoteric and zwitterionic surfactants, and nonionic surfactants.

Claims

1. A method, comprising:

combining a carrier fluid and a solids mixture to form a slurry, wherein the solids mixture comprises a plurality of volume-averaged particle size distribution (PSD) modes such that a packed volume fraction (PVF) exceeds 0.75, wherein the solids mixture comprises at least a proppant PSD mode and a fines PSD mode;

circulating the slurry through a well bore to form a proppant pack from depositing the solids mixture in one or both of a fracture in a formation and an annulus between a screen and the wellbore;

contacting fines in the pack with a dispersant;

passing fluid through the pack to remove fines from the pack.

2. The method of claim 1, wherein the dispersant is present in the slurry.

3. The method of claim 1, wherein contacting the fines with the dispersant comprises displacing the carrier fluid from the proppant pack with another fluid comprising the dispersant.

4. The method of claim 1, wherein contacting the fines with the dispersant comprises circulating a fluid comprising the dispersant in the well bore after forming the pack.

5. The method of claim 1, wherein contacting the fines with the dispersant comprises spotting a fluid comprising the dispersant in contact with the pack after forming the pack.

6. The method of claim 1, wherein the dispersant comprises a polyelectrolyte.

7. The method of claim 1, wherein the dispersant comprises polysulfonate, polycarboxylate or a combination thereof.

8. The method of claim 1, wherein the dispersant is selected from lignosulfonates, polymelamine sulfonates, polystyrene sulfonates, polynaphthalene sulfonates and combinations thereof.

9. The method of claim 1, wherein the dispersant comprises polynaphthalene sulfonate.

10. The method of claim 1, wherein the dispersant is selected from polyacrylates having a weight average molecular weight less than 10,000 Daltons.

11. The method of claim 1, wherein the dispersant is selected from anionic, cationic, amphoteric and zwitterionic surfactants.

12. The method of claim 1, wherein the carrier fluid comprises brine and the dispersant is selected from nonionic surfactants.

13. The method of claim 1, wherein a weight ratio of dispersant to fines is from about 1:

500 to about 10;

90.

14. The method of claim 1, wherein the fines comprise silica.

15. The method of claim 1, wherein the fines comprise calcium carbonate.

16. The method of claim 1, wherein the fines are agglomerated in the slurry.

17. The method of claim 1, wherein the slurry comprises a volume fraction of solids of from about 0.45 up to the PVF.

18. The method of claim 1, wherein the proppant PSD mode is from 100 to 2000 microns and the fines PSD mode is from 1 to 20 microns.

19. The method of claim 1, wherein the proppant PSD mode is from 18 to 900 times larger than the fines PSD mode.

20. The method of claim 1, wherein the slurry further comprises one or more intermediate PSD modes selected from the group consisting of PSD modes from 2 to 60 times smaller than the proppant PSD mode, PSD modes from 1.1 to 60 times larger than the fines PSD mode, and combinations thereof.

21. The method of claim 20, wherein at least one of the intermediate PSD modes is degradable, and further comprising degrading the at least one degradable intermediate PSD mode after forming the pack.

22. The method of claim 20, wherein the intermediate PSD modes include a relatively larger PSD mode and a relatively smaller intermediate PSD mode, wherein the larger intermediate PSD mode is from 2 to 15 times smaller than the proppant PSD mode and from 1.25 to 15 times larger than the smaller intermediate PSD mode, and wherein the smaller intermediate mode is from 1.1 to 15 times larger than the fines PSD mode.

23. The method of claim 22, further comprising a middle intermediate PSD mode from 1.5 to 4 times smaller than the larger intermediate PSD mode and 1.25 to 2.5 times larger than the smaller PSD mode.

24. The method of claim 22, wherein the relatively larger intermediate PSD mode is degradable, and further comprising degrading the larger intermediate PSD mode after forming the pack.

25. The method of claim 1, wherein at least 70 percent of the fines are removed from the pack.

26. The method of claim 1, further comprising producing reservoir fluid through the cleaned pack into the well bore.

27. The method of claim 1, comprising gravel packing wherein the slurry is circulated in the well bore at a rate less than about 800 L/min (5 BPM).

28. The method of claim 1, wherein the carrier fluid is a low viscosity fluid free of viscosifier or comprising viscosifier in an amount less than 2.4 g of viscosifier per liter of carrier fluid (20 lb/1000 gal).

29. A system, comprising:

a well bore in fluid communication with a subterranean formation;

a gravel packing slurry comprising a carrier fluid and a solids mixture, wherein the solids mixture comprises a plurality of volume-averaged particle size distribution (PSD) modes such that a packed volume fraction (PVF) exceeds 0.75, wherein the solids mixture comprises at least a proppant PSD mode and a fines PSD mode;

a pump to circulate the slurry in the well bore to deposit the solids mixture and form a proppant pack in one or both of a fracture in the formation and an annulus between a screen and the formation; and

a dispersant source effective to facilitate fines flowback from the pack.

30. The system of claim 29, wherein the dispersant is present in the slurry.

31. The system of claim 29, wherein the dispersant source comprises a dispersant circulation or spotting fluid.

32. The system of claim 29, wherein the dispersant comprises a polyelectrolyte.

33. The system of claim 29, wherein the dispersant comprises polysulfonate, polycarboxylate or a combination thereof.

34. The system of claim 29, wherein the dispersant is selected from lignosulfonates, polymelamine sulfonates, polystyrene sulfonates, polynaphthalene sulfonates and combinations thereof.

35. The system of claim 29, wherein the dispersant comprises polynaphthalene sulfonate.

36. The system of claim 29, wherein the dispersant is selected from polyacrylates having a weight average molecular weight less than 10,000 Daltons.

37. The system of claim 29, wherein the dispersant is selected from anionic, cationic, amphoteric and zwitterionic surfactants.

38. The system of claim 29, wherein the carrier fluid comprises brine and the dispersant is selected from nonionic surfactants.

39. The system of claim 29, wherein a weight ratio of dispersant to fines is from about 1:

500 to about 10;

90.

40. The system of claim 29, wherein the fines comprise silica.

41. The system of claim 29, wherein the fines comprise calcium carbonate.

42. The system of claim 29, wherein the fines are agglomerated in the slurry.

43. The system of claim 29, wherein the slurry comprises a volume fraction of solids of from about 0.45 up to the PVF.

44. The system of claim 29, wherein the proppant PSD mode is from 100 to 2000 microns and the 30 fines PSD mode is from 1 to 20 microns.

45. The system of claim 29, wherein the proppant PSD mode is from 18 to 900 times larger than the fines PSD mode.

46. The system of claim 29, wherein the slurry further comprises one or more intermediate PSD modes selected from the group consisting of:

PSD modes from 2 to 60 times smaller than the proppant PSD mode, PSD modes from 1.1 to 60 times larger than the fines PSD mode, and combinations thereof.

47. The system of claim 46, wherein at least one of the intermediate PSD modes is degradable.

48. The system of claim 46, wherein the intermediate PSD modes include a relatively larger intermediate PSD mode and a relatively smaller intermediate PSD mode, wherein the larger intermediate PSD mode is from 2 to 15 times smaller than the proppant PSD mode and from 1.25 to 15 times larger than the smaller intermediate PSD mode, and wherein the smaller intermediate mode is from 1.1 to 15 times larger than the fines PSD mode.

49. The system of claim 48, further comprising a middle intermediate PSD mode from 1.5 to 4 times smaller than the larger intermediate PSD mode and 1.25 to 2.5 times larger than the smaller PSD mode.

50. The system of claim 48, wherein the relatively larger intermediate PSD mode is degradable.

51. The system of claim 29, wherein the carrier fluid is a low viscosity fluid free of viscosifier or comprising viscosifier in an amount less than 2.4 g of viscosifier per liter of carrier fluid (20 lb/1000 gal).