IP Library Granted Patent US 10,920,121
Granted Patent B1
US 10,920,121 · App. 16/822,645 · Granted Feb 16, 2021

Methods of reducing lost circulation in a wellbore using Saudi Arabian volcanic ash

Inventors: Khawlah A. Alanqari (Al-Khubar, SA); Abdullah S. Al-Yami (Dhahran, SA)
Assignee: Saudi Arabian Oil Company
C09K8/032E21B21/003E21B33/138
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Quick Facts
Patent No.
US 10,920,121
App. No.
16/822,645
Granted
Feb 16, 2021
Kind
B1
Abstract

A method of reducing lost circulation includes introducing an activation solution comprising an aqueous solution, Na 2 SiO 3 , and NaOH into the wellbore and introducing Saudi Arabian volcanic ash into the wellbore. The Saudi Arabian volcanic ash comprises SO 3 , CaO, SiO 2 , Al 2 O 3 , Fe 2 O 3 , MgO, and K 2 O. The method further includes allowing the Saudi Arabian volcanic ash to contact the activation solution in the wellbore, thereby forming a geopolymer barrier between the wellbore and a subsurface formation to reduce lost circulation in the wellbore.

Claims (28)

1. A method of reducing lost circulation in a wellbore comprising:

introducing an activation solution comprising an aqueous solution, from 25 to 50 wt. % Na 2 SiO 3 , and from 15 to 35 wt. % NaOH into the wellbore;

introducing Saudi Arabian volcanic ash into the wellbore, in which the Saudi Arabian volcanic ash is free of TiO 2 and comprises SO 3 , CaO, SiO 2 , Al 2 O 3 , Fe 2 O 3 , MgO, and K 2 O; and

allowing the Saudi Arabian volcanic ash to contact the activation solution in the wellbore, thereby forming a geopolymer barrier between the wellbore and a subsurface formation to reduce lost circulation in the wellbore.

2. The method of claim 1 , in which the Na 2 SiO 3 has a ratio of Na 2 O to SiO 2 of from 0.250:1 to 0.350:1.

3. The method of claim 1 , in which the activation solution comprises SiO 2 in an amount of from 2 to 4 times the amount of Al 2 O 3 present in the Saudi Arabian volcanic ash.

4. The method of claim 1 , in which the activation solution comprises a pH of from 11.6 to 13.0.

5. The method of claim 1 , in which the Saudi Arabian volcanic ash has a particle size of from 20 to 30 μm.

6. The method of claim 1 , in which the Saudi Arabian volcanic ash comprises from 40 wt. % to 50 wt. % SiO 2 and from 10 wt. % to 20 wt. % Al 2 O 3 .

7. The method of claim 1 , in which the Saudi Arabian volcanic ash comprises:

from 0.05 wt. % to 0.2 wt. % SO 3 ;

from 5 wt. % to 10 wt. % CaO;

from 40 wt. % to 50 wt. % SiO 2 ;

from 10 wt. % to 20 wt. % Al 2 O 3 ;

from 10 wt. % to 15 wt. % Fe 2 O 3 ;

from 5 wt. % to 10 wt. % MgO; and

from 0.5 wt. % to 5 wt. % K 2 O.

8. The method of claim 1 , in which the aqueous solution comprises deionized water, tap water, fresh water, salt water, natural or synthetic brine, municipal water, formation water, produced water, well water, filtered water, distilled water, sea water, or combinations of these.

9. The method of claim 1 , in which introducing Saudi Arabian volcanic ash into the wellbore comprises introducing an ash solution comprising an aqueous solution and Saudi Arabian volcanic ash, in which the aqueous solution comprises deionized water, tap water, fresh water, salt water, natural or synthetic brine, municipal water, formation water, produced water, well water, filtered water, distilled water, sea water, or combinations of these.

10. The method of claim 9 , in which the ash solution comprises from 30 to 60 wt. % Saudi Arabian volcanic ash.

11. The method of claim 9 , in which the ash solution further comprises a cement precursor material comprising one or more components selected from the group consisting of calcium hydroxide, silicates, belite (Ca 2 SiO 5 ), alite (Ca 3 SiO 4 ), tricalcium aluminate (Ca 3 Al 2 O 6 ), tetracalcium aluminoferrite (Ca 4 Al 2 Fe 2 O 10 ), brownmillerite (4CaO.Al 2 O 3 .Fe 2 O 3 ), gypsum (CaSO 4 .2H 2 O), sodium oxide, potassium oxide, lime (calcium oxide), hexavalent chromium, trivalent chromium, calcium aluminate, and combinations thereof.

12. The method of claim 9 , in which the ash solution further comprises one or more additives selected from the group consisting of dispersants, fluid loss control agents, retarders, expansion additives, antifoaming agents, stabilizers, accelerators, extenders, weighting agents, lost circulation control agents, surfactants, gypsum, hematite, manganese tetroxide, silica flour, and silica sand.

13. The method of claim 1 , in which the geopolymer barrier has a compressive strength of from 1300 to 1500 psi.

14. The method of claim 1 , in which the geopolymer barrier has a ratio of Na 2 SiO 3 combined with NaOH to Al 2 O 3 ranges from 0.5:1.0 to 9.0:1.0.

15. The method of claim 1 , in which the geopolymer barrier comprises a sodium aluminosilicate hydrate.

16. The method of claim 15 , in which the sodium aluminosilicate hydrate comprises a formula of:

Na n [(—SiO 2 ) z —AlO 2 ] n .y H 2 O, where n represents a degree of polymerization ranging 1 to 50 and z represents an amount of silicate ranging from 2 to 10.

17. The method of claim 15 , in which the sodium aluminosilicate hydrate has a structure of:

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 18, 2020
From: ALANQARI, KHAWLAH A.; AL-YAMI, ABDULLAH S.
To: SAUDI ARABIAN OIL COMPANY
Reel/Frame 052154/0522 →
Cited By (7)
US 12,570,889 US 12,617,998 US 12,624,274 US 12,709,705 US 12,715,811 US 12,735,621 US 12,735,622