Reclamation of brines with metal contamination using lime

Patent metadata

Field	Value
Publication number	US-10876388-B2
Application number	US-201515547752-A
Country	US
Kind code	B2
Filing date	Mar 7, 2015
Priority date	Mar 7, 2015
Publication date	Dec 29, 2020
Grant date	Dec 29, 2020

Abstract

A method of removing a soluble metal ion from a contaminated brine fluid comprising: adding lime to the contaminated brine fluid, wherein the lime causes the soluble metal ion to become insoluble in the contaminated brine fluid; and passing the contaminated brine fluid through a filter media, wherein the step of passing is performed after the step of adding, and wherein after the brine fluid is passed through the filter media, a brine fluid having a reduced concentration of the metal ion is produced. Another method of removing a soluble metal ion from a contaminated brine fluid comprises: passing the contaminated brine fluid through a filter media, wherein the filter media comprises the lime.

First claim

What is claimed is:

1. A method of removing a soluble metal ion from a contaminated brine fluid comprising:
adding lime to the contaminated brine fluid, wherein the lime causes the soluble metal ion to become insoluble in the contaminated brine fluid without addition of an oxidizer; and
passing the contaminated brine fluid through a filter media, wherein the filter media comprises lime, wherein the step of passing is performed after the step of adding, and wherein after the contaminated brine fluid is passed through the filter media, a brine fluid having a reduced concentration of the metal ion is produced; wherein the contaminated brine fluid is passed through the filter media using a pressure filter assembly; and wherein the pressure filter assembly is a continuous filter assembly, and the length of time for filtration is in the range of about 12 hours to about 4 days.

2. The method according to claim 1 , wherein the soluble metal ion is iron, zinc, or combinations thereof.

3. The method according to claim 1 , wherein the contaminated brine fluid comprises a salt, and wherein the salt is selected from the group consisting of sodium chloride, calcium chloride, calcium bromide, potassium chloride, potassium bromide, magnesium chloride, sodium bromide, cesium formate, cesium acetate, and any combination thereof.

4. The method according to claim 1 , wherein the contaminated brine fluid comprises a base fluid, and wherein the base fluid comprises water.

5. The method according to claim 1 , wherein the contaminated brine fluid has a density in a range of 8 to 20 pounds per gallon prior to the step of passing.

6. The method according to claim 5 , wherein the brine fluid that has passed through the filter media has a density that is within 10% of the density of the contaminated brine fluid prior to the step of passing.

7. The method according to claim 1 , wherein the brine fluid becomes contaminated with the soluble metal ion prior to, during, or after use in an oil or gas operation.

8. The method according to claim 1 , wherein the lime is selected from the group consisting of calcium oxide, calcium hydroxide, calcium carbonate, and combinations thereof.

9. The method according to claim 1 , wherein the lime is added to the contaminated brine fluid in a concentration in the range of 3 to 35 pounds per barrel of the contaminated brine fluid.

10. The method according to claim 1 , wherein the filter media further comprises a filter aid.

11. The method according to claim 10 , wherein the filter aid is selected from the group consisting of diatomaceous earth, glass fibers, glass wool, silica gel, alumina, paper, activated charcoal, and combinations thereof.

12. The method according to claim 1 , wherein the concentration of the metal ion is reduced to a value of less than or equal to 2% by weight of the brine fluid.

13. The method according to claim 1 , further comprising introducing the brine fluid into a wellbore, wherein the wellbore penetrates a subterranean formation, and wherein the step of introducing is performed after the step of passing.

14. The method according to claim 13 , wherein the brine fluid is used in a drilling fluid, completion fluid, workover fluid, injection fluid, or stimulation fluid.

15. The method according to claim 13 , wherein the step of introducing is performed using a pump.

16. A method of removing a soluble metal ion from a contaminated brine fluid comprising:
passing the contaminated brine fluid through a filter media, wherein the filter media comprises lime, wherein the lime causes the soluble metal ion to become insoluble in the contaminated brine fluid without addition of an oxidizer, and wherein after the contaminated brine fluid is passed through the filter media, a brine fluid having a reduced concentration of the metal ion is produced, wherein the contaminated brine fluid is passed through the filter media using a pressure filter assembly, and wherein the pressure filter assembly is a continuous filter assembly, and the length of time for filtration is in the range of about 12 hours to about 4 days.

17. The method according to claim 16 , wherein the lime is selected from the group consisting of calcium oxide, calcium hydroxide, calcium carbonate, and combinations thereof.

18. The method according to claim 16 , wherein the filter media further comprises a filter aid, and wherein the filter aid is selected from the group consisting of diatomaceous earth, glass fibers, glass wool, silica gel, alumina, paper, activated charcoal, and combinations thereof.

19. The method according to claim 16 , wherein the concentration of the metal ion is reduced to a value of less than or equal to 2% by weight of the brine fluid.

20. The method according to claim 16 , wherein the soluble metal ion is iron, zinc, or combinations thereof.

Assignees

• Halliburton Energy Services Inc

Inventors

• Davis Chesnee L
• Deville Jay P
• Miller Matthew L

Classifications

• C09K8/66

  Compositions based on water or polar solvents (C09K8/64 takes precedence) · CPC title

• C09K8/04

  Aqueous well-drilling compositions · CPC title

• E21B21/068

  using chemical treatment · CPC title

• E21B21/063

  by separating components · CPC title

• E21B43/34 Primary

  Arrangements for separating materials produced by the well · CPC title