Brine purification process

Patent metadata

Field	Value
Publication number	US-11014832-B2
Application number	US-201515531812-A
Country	US
Kind code	B2
Filing date	Dec 4, 2015
Priority date	Dec 5, 2014
Publication date	May 25, 2021
Grant date	May 25, 2021

Abstract

The present invention provides a method for reducing the concentration of aluminum and nickel cations in a brine comprising aluminum and nickel cations. The treated brine can be used as a feedstock to membrane cell chlor-alkali process.

First claim

What is claimed is:

1. A method for reducing the concentration of aluminum and nickel cations in a brine comprising aluminum and nickel cations, the steps of the method comprising:
a) Determining the pH of the brine and, when the pH of the brine is in excess of 6 or below 2, adjusting the pH of the brine to a pH from 2 through 6; and
b) Contacting the brine of a) with a mixture of at least two cationic exchange resins, wherein the first cationic exchange resin comprises an aminophosphonic acid functional group and the second cationic exchange resin comprises an iminodiacetic acid functional group at a linear liquid velocity from 10 through 100 m/hr, and at a temperature of from 10 through 90° C., to produce a treated brine which contains less aluminum and nickel cations than prior to contacting the brine of a) with the mixture of at least two cationic exchange resins;

wherein the brine does not contain a chelating or complexing agent, and
wherein prior to the contact with the mixture of the at least two cationic exchange resins the brine has a concentration of from about 300 ppb to about 5 ppm aluminum and from about 3 ppb to about 100 ppb nickel, and wherein the concentration of aluminum and nickel is reduced to less than about 50 ppb aluminum and to less than about 1 ppb nickel after contact with the mixture of the at least two cationic exchange resins.

2. The method of claim 1 wherein the mixture comprises two cationic exchange resins and the ratio of the first cationic exchange resin to the second cationic exchange resin in the mixture is from 10:90 to 90:10.

3. The method of claim 1 , wherein the mixture comprises two cationic exchange resins and the ratio of the first cationic exchange resin to the second cationic exchange resin in the mixture is from 20:80 to 80:20.

4. The method of claim 1 , wherein the mixture comprises two cationic exchange resins and the ratio of the first cationic exchange resin to the second cationic exchange resin in the mixture is from 40:60 to 60:40.

5. The method of claim 1 , further comprising the regeneration of the mixture of resins by a treatment comprising a base of between 1 and 10% solution and by treatment comprising an acid of between 1 and 12% solution.

6. The method of claim 1 , wherein the brine is treated to reduce the quantity of calcium, barium, strontium and/or magnesium in the brine prior to step a).

7. The method of claim 1 , wherein the pH of the brine is in step a) is from 3 through 4.

8. The method of claim 1 , wherein the temperature is from 50 to 70° C.

9. The method of claim 8 wherein the temperature is from 55 to 65° C.

10. The method of claim 5 , wherein the base is 2 to 6% solution.

11. The method of claim 5 , wherein the acid is from 2 to 10% solution.

12. The Method of claim 1 , wherein the brine is reduced to less than about 20 ppb aluminum and to less than about 0.5 ppb nickel after contact with the mixture of at least two cationic exchange resins.

13. The Method of claim 1 , wherein the brine is reduced to less than about 2 ppb aluminum and to less than about 0.5 ppb nickel after contact with the mixture of at least two cationic exchange resins.

14. A method for reducing the concentration of aluminum and nickel cations in a brine comprising aluminum and nickel cations to provide a brine feedstock used in a membrane cell chlor-alkali process, the steps of the method comprising:
a) Determining the pH of the brine and, when the pH of the brine is in excess of 6 or below 2, adjusting the pH of the brine to a pH from 2 through 6;
b) Contacting the brine of a) with a mixture of at least two cationic exchange resins, wherein the first cationic exchange resin comprises an aminophosphonic acid functional group and the second cationic exchange resin comprises an iminodiacetic acid functional group at a liquid velocity from 10 through 100 m/hr, and at a temperature of from 10 through 90° C., to produce a treated brine which contains less aluminum and nickel cations than prior to contacting the brine of a) with the mixture of at least two cationic exchange resins; and
c) Using the brine of b) as a feedstock in a membrane cell chlor-alkali process; wherein the brine does not contain a chelating or complexing agent, and
wherein prior to the contact with the mixture of the at least two cationic exchange resins the brine has a concentration of from about 300 ppb to about 5 ppm aluminum and from about 3 ppb to about 100 ppb nickel, and wherein the concentration of aluminum and nickel is reduced to less than about 50 ppb aluminum and to less than about 1 ppb nickel after contact with the mixture of the at least two cationic exchange resins.

15. The method of claim 14 wherein the mixture comprises two cationic exchange resins and the ratio of the first cationic exchange resin to the second cationic exchange resin in the mixture is from 10:90 to 90:10.

16. The method of claim 14 , wherein the mixture comprises two cationic exchange resins and the ratio of the first cationic exchange resin to the second cationic exchange resin in the mixture is from 20:80 to 80:20.

17. The method of claim 14 , wherein the mixture comprises two cationic exchange resins and the ratio of the first cationic exchange resin to the second cationic exchange resin in the mixture is from 40:60 to 60:40.

18. The method of claim 14 , further comprising the regeneration of the mixture of resins by a treatment comprising a base of between 1 and 10% solution and by a treatment comprising an acid of between 1 and 12% solution.

19. The method of claim 14 , wherein the brine is treated to reduce the quantity of calcium, barium, strontium and/or magnesium in the brine prior to step a).

20. The method of claim 14 , wherein the pH of the brine is in step a) is from 3 through 4.

21. The method of claim 14 , wherein the temperature is from 50 to 70° C.

22. The method of claim 21 wherein the temperature is from 55 to 65° C.

23. The method of claim 18 , wherein the base is 2 to 6% solution.

24. The method of claim 18 , wherein the acid is from 2 to 10% solution.

Assignees

• Blue Cube Ip Llc

Inventors

• Zhou Jianqing
• Garbade Kurt
• Sabater-Prieto Sergio
• Offermann Martin

Classifications

• C01D3/14

  Purification · CPC title

• C02F2209/02

  Temperature · CPC title

• Y02W10/37

  using solar energy · CPC title

• C02F2101/20

  Heavy metals or heavy metal compounds · CPC title

• C01D3/145

  by solid ion-exchangers or solid chelating agents · CPC title