IP Library Granted Patent US 11,299,663
Granted Patent B2
US 11,299,663 · App. 16/892,784 · Granted Apr 12, 2022

Method for modifying well injection profile and enhanced oil recovery

Inventors: Ali Abdullah Al-Taq (Dhahran, SA); Zuhair AlYousif (Dhahran, SA); Othman Alswaie (Dammam, SA)
Assignee: SAUDI ARABIAN OIL COMPANY
C09K8/594E21B43/164E21B43/166E21B43/24
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Quick Facts
Patent No.
US 11,299,663
App. No.
16/892,784
Granted
Apr 12, 2022
Kind
B2
Abstract

A method for treating a hydrocarbon-containing formation includes injecting an aqueous solution that contains an alkali nitrite, an ammonium halide, and a foaming agent into the formation, injecting supercritical carbon dioxide into the formation, allowing a portion of the carbon dioxide to dissolve in the aqueous solutions, causing the alkali nitrite and ammonium halide to react and generate nitrogen gas, and allowing a foam to form by the interaction of the nitrogen gas with the foaming agent.

Claims (40)

1. A method for treating a hydrocarbon-containing formation, comprising:

pre-flushing the hydrocarbon-containing formation with a flushing solution comprising a foaming agent to form a pre-flushed hydrocarbon-containing formation;

injecting an aqueous solution that contains an alkali nitrite, an ammonium halide, and the foaming agent into the pre-flushed hydrocarbon-containing formation; and

injecting a supercritical carbon dioxide into the pre-flushed hydrocarbon-containing formation;

where a portion of the supercritical carbon dioxide dissolves into the aqueous solution causing the alkali nitrite and the ammonium halide to react and generate a nitrogen gas; and

where a foam forms by the interaction of the nitrogen gas with the foaming agent.

2. The method of claim 1 , wherein the aqueous solution and the supercritical carbon dioxide are co-injected.

3. The method of claim 1 , further comprising displacing hydrocarbons from the pre-flushed hydrocarbon-containing formation by forcing the portion of the supercritical carbon dioxide and the aqueous solution through the pre-flushed hydrocarbon-containing formation.

4. The method of claim 3 , further comprising recovering the hydrocarbons that are displaced.

5. The method of claim 3 , wherein the pre-flushed hydrocarbon-containing formation comprises a zone of high permeability and a zone of low permeability.

6. The method of claim 5 , wherein the at least a portion of the supercritical carbon dioxide and the aqueous solution are forced through the zone of low permeability.

7. The method of claim 1 , wherein the aqueous solution comprises a mixture of a first aqueous solution and a second aqueous solution.

8. The method of claim 7 , wherein the first aqueous solution contains the ammonium halide in a concentration of the range of 0.5 to 13 M.

9. The method of claim 7 , wherein the second aqueous solution contains the alkali nitrite in a concentration of the range of 1 to 15 M.

10. The method of claim 7 , wherein one or more of the first aqueous solution and the second aqueous solutions contains the foaming agent.

11. The method of claim 1 , wherein a molar ratio of the ammonium halide to the alkali nitrite that are injected into the formation is of the range of 1:1 to 1:3.

12. The method of claim 2 , wherein the supercritical carbon dioxide has a quality in the range of 10 to 90%.

13. The method of claim 1 , wherein the reaction between the alkali nitrite and the ammonium halide is triggered by a pH of the aqueous solutions decreasing to 5 or less.

14. The method of claim 13 , wherein the pH decrease is caused by the portion of the supercritical carbon dioxide dissolving into the aqueous solution.

15. The method of claim 1 , wherein the reaction between the alkali nitrite and the ammonium halide is triggered by a temperature of the aqueous solutions increasing to 60° C. or more.

16. The method of claim 15 , wherein the temperature increase is caused by the portion of the supercritical carbon dioxide dissolving into the aqueous solution.

17. The method of claim 1 , wherein the foam has an apparent viscosity in a range of about 1 to 50 cP.

18. The method of claim 1 , wherein the foam has a quality in a range of about 50 to 99%.

19. A method for enhanced oil recovery, comprising:

pre-flushing the hydrocarbon-containing formation with a flushing solution comprising the foaming agent to form a pre-flushed hydrocarbon-containing formation;

injecting a solution comprising an alkali nitrite, an ammonium halide, and the foaming agent into a high permeability zone of the pre-flushed hydrocarbon-containing formation;

decreasing a pH of the solution by injecting a supercritical carbon dioxide into the high permeability zone of the pre-flushed hydrocarbon-containing formation such that the alkali nitrite and the ammonium halide react to generate a nitrogen gas that forms a foam with the foaming agent in the high permeability zone and such that wormholes form in a low permeability zone of the pre-flushed hydrocarbon-containing formation such that hydrocarbons in the low permeability zone of the pre-flushed hydrocarbon-bearing formation are stimulated; and

producing hydrocarbons from the pre-flushed hydrocarbon-containing formation.

20. The method of claim 19 , wherein the solution comprises a mixture of a first aqueous solution and a second aqueous solution.

21. The method of claim 20 , wherein the first aqueous solution contains the ammonium halide in a concentration of a range of 0.5 to 13 M.

22. The method of claim 20 , wherein the second aqueous solution contains the alkali nitrite in a concentration of a range of 1 to 15 M.

23. The method of claim 20 , wherein one or more of the first aqueous solution and the second aqueous solutions contains the foaming agent.

24. A method for treating a hydrocarbon-containing formation, comprising:

pre-flushing the hydrocarbon-containing formation with a flushing solution comprising the foaming agent to form a pre-flushed hydrocarbon-containing formation;

injecting an aqueous solution that contains an alkali nitrite, an ammonium halide, and the foaming agent into the pre-flushed hydrocarbon-containing formation, wherein the aqueous solution comprises a mixture of a first aqueous solution containing the ammonium halide in a concentration of a range of 0.5 to 13 M and a second aqueous solution containing the alkali nitrite in a concentration of a range of 1 to 15 M, and a molar ratio of the ammonium halide to the alkali nitrite of a range of 1:1 to 1:3;

injecting a supercritical carbon dioxide into the pre-flushed hydrocarbon-containing formation such that a portion of the supercritical carbon dioxide dissolves in the aqueous solution and causes the alkali nitrite and the ammonium halide to react and generate a nitrogen gas,

wherein the reaction between the alkali nitrite and the ammonium halide is triggered by a pH of the aqueous solutions decreasing to 5 or less; and such that a foam having a viscosity in a range of about 1 to 50 cP to forms by an interaction of the nitrogen gas with the foaming agent.

25. The method of claim 24 , wherein one or more of the first aqueous solution and the second aqueous solutions contains the foaming agent.

26. The method of claim 24 , wherein a pH decrease is caused by the portion of the supercritical carbon dioxide dissolving into the aqueous solution.

27. The method of claim 24 , wherein the foam has a quality in a range of about 50 to 99%.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 4, 2020
From: AL-TAQ, ALI ABDULLAH; ALYOUSIF, ZUHAIR; ALSWAIE, OTHMAN
To: SAUDI ARABIAN OIL COMPANY
Reel/Frame 052842/0546 →
Continuity (1)
Related Publication 20210380869A1 · Dec 9, 2021
Cited By (1)
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