Aqueous fluid compositions and barite scale removal therewith

Patent metadata

Field	Value
Publication number	US-12227693-B2
Application number	US-202217930843-A
Country	US
Kind code	B2
Filing date	Sep 9, 2022
Priority date	Sep 9, 2022
Publication date	Feb 18, 2025
Grant date	Feb 18, 2025

Abstract

Barite (barium sulfate) scale may be problematic in subterranean formations, wellbores, pipelines, and other locations and may be difficult to remove in many instances. Aqueous fluid compositions effective for removing barite scale may comprise a concentrated mineral acid, a first salt comprising an iodide anion, and a second salt comprising an anion that forms an aqueous-soluble barium salt. One suitable aqueous fluid composition may comprise concentrated hydroiodic acid, an alkali metal iodide, and an alkali metal hypophosphite salt. The aqueous fluid compositions may be used in combination with a second treatment phase comprising a fluid composition comprising at least one acid gas capturing agent. The at least one acid gas capturing agent may comprise a first component reactive toward hydrogen sulfide and an optional second component reactive toward carbon dioxide.

First claim

The invention claimed is:

1. An aqueous fluid composition comprising:
a concentrated mineral acid comprising concentrated hydroiodic acid;
a first salt comprising an iodide anion; and
a second salt comprising an anion that forms an aqueous-soluble barium salt;
wherein a molar ratio of total iodide ions to second salt in the aqueous fluid composition is about 5 to about 10; and
wherein water from the concentrated mineral acid is the sole source of water in the aqueous fluid composition, other than trace moisture, or up to about 10 vol. % additional water from a source other than the concentrated mineral acid is present in the aqueous fluid composition.

2. The aqueous fluid composition of claim 1 , wherein the second salt is a reducing agent.

3. The aqueous fluid composition of claim 1 , wherein the second salt comprises a hypophosphite salt.

4. The aqueous fluid composition of claim 3 , wherein a molar ratio of hydroiodic acid to hypophosphite salt in the aqueous fluid composition is about 5 to about 10.

5. The aqueous fluid composition of claim 1 , wherein the first salt comprises an alkali metal iodide.

6. The aqueous fluid composition of claim 5 , wherein the second salt comprises an alkali metal hypophosphite.

7. The aqueous fluid composition of claim 6 , wherein a molar ratio of hydroiodic acid to alkali metal hypophosphite in the aqueous fluid composition is about 5 to about 10.

8. A scale dissolution system comprising:
a first treatment phase comprising the aqueous fluid composition of claim 1 ; and
a second treatment phase comprising a fluid composition comprising at least one acid gas capturing agent.

9. The scale dissolution system of claim 8 , wherein the second salt comprises a hypophosphite salt.

10. The scale dissolution system of claim 9 , wherein a molar ratio of hydroiodic acid to hypophosphite salt in the first treatment phase is about 5 to about 10.

11. The scale dissolution system of claim 8 , wherein the first salt comprises an alkali metal iodide and the second salt comprises an alkali metal hypophosphite.

12. The scale dissolution system of claim 8 , wherein the at least one acid gas capturing agent in the second treatment phase comprises at least a first component reactive toward hydrogen sulfide.

13. The scale dissolution system of claim 12 , wherein the at least one acid gas capturing agent in the second treatment phase further comprises a second component reactive toward carbon dioxide.

14. The scale dissolution system of claim 13 , wherein the second component comprises at least one amine.

15. The scale dissolution system of claim 12 , wherein the first component is reactive toward hydrogen sulfide through nucleophilic aromatic substitution.

16. The scale dissolution system of claim 15 , wherein the first component comprises p-bromotoluene.

17. A method comprising:
introducing the aqueous fluid composition of claim 1 to a location containing barite scale; and
contacting the barite scale with the aqueous fluid composition for a sufficient time to dissolve at least a portion of the barite scale.

18. The method of claim 17 , wherein the second salt comprises a hypophosphite salt.

19. The method of claim 18 , further comprising:
introducing a fluid composition comprising at least one acid gas capturing agent to the location; and
reacting the at least one acid gas capturing agent with at least a portion of at least one acid gas that is present at the location.

20. The method of claim 19 , wherein the at least one acid gas comprises hydrogen sulfide, carbon dioxide, or any combination thereof.

21. The method of claim 20 , wherein the at least one acid gas comprises at least hydrogen sulfide, and at least a portion of the hydrogen sulfide is formed upon contacting the barite scale with the aqueous fluid composition.

22. The method of claim 19 , wherein the at least one acid gas capturing agent in the fluid composition comprises a first component reactive toward hydrogen sulfide and optionally, a second component reactive toward carbon dioxide.

23. The method of claim 17 , wherein the location is a subterranean formation, a wellbore penetrating a subterranean formation, a pipeline, or any combination thereof.

Assignees

• Saudi Arabian Oil Co

Inventors

• Oduro Harry Daniel
• Haidary Saleh Abdulrahman

Classifications

• E21B37/06

  using chemical means for preventing or limiting {, e.g. eliminating,} the deposition of paraffins or like substances · CPC title

• C09K2208/20

  Hydrogen sulfide elimination · CPC title

• C09K8/54

  Compositions for in situ inhibition of corrosion in boreholes or wells · CPC title

• C09K8/528 Primary

  inorganic depositions, e.g. sulfates or carbonates · CPC title