Process for producing sodium hydroxide and ammonium sulfate from sodium sulfate

• US 5,098,532 A
• Filed: 05/24/1991
• Issued: 03/24/1992
• Est. Priority Date: 05/24/1991
• Status: Expired due to Term

• Current Assignee: 773006 Alberta Limited
• Original Assignee: Ormiston Mining and Smelting Co., Ltd.
• Inventors: Genders, David, Thompson, Jack S.
• Primary Examiner(s): Niebling, John
• Assistant Examiner(s): RYSER, DAVID
• Application Number:
  US07/705,235
• Time in Patent Office: 305 Days
• Field of Search: 204/98, 204/104, 204/93, 204/182.4, 204/129
• US Class Current: 205/351
• CPC Class Codes: C25B 1/00 Electrolytic production of inorganic compounds or non-metals
• CPC Class Codes: C25B 1/16 Hydroxides by simultaneous production of alkali metal hydroxides and chlorine, oxyacids or salts of chlorine C25B1/34

Abstract

A process for producing sodium hydroxide and ammonium sulfate by electrolysing an aqueous solution of sodium sulfate is disclosed. The process is carried out in a three-compartment electrolytic cell having a central compartment separated from an anode and a cathode compartment by, respectively, anion selective and cation selective ion exchange membrane. The solution of sodium sulfate is circulated through the central compartment, while solutions of sodium hydroxide and ammonium sulfate are circulated, respectively, through the cathode and the anode compartment. During the process, ammonia is added to the anolyte to at least partially neutralize sulfuric acid produced in the anode compartment and reduce the back migration of protons from the anolyte into the central compartment. As a result, high purity ammonium sulfate of commercial value higher than that of sulfuric acid is produced with high current efficiency and in concentrations higher than those achievable for sulfuric acid.

Claims

1. A process for producing sodium hydroxide, which process comprises electrolysing an aqueous solution of sodium sulfate in an electrolytic cell having at least one anode compartment and at least one cathode compartment, said anode compartment containing an anolyte and having an anode located therein, said cathode compartment containing a catholyte and having a cathode located therein, said anode compartment and said cathode compartment being separated from the sodium sulfate solution by an anion selective ion exchange membrane and a cation selective ion exchange membrane, respectively, wherein during the process ammonia is added to the anolyte to at least partially neutralize sulfuric acid produced in the anode compartment.

3. A process according to claim 1 or 2, wherein sulfuric acid is neutralized to maintain the anolyte at a pH of less than about 7.

4. A process according to claim 3, wherein sulfuric acid is neutralized to maintain the anolyte at a pH of less than about 2.

5. A process according to claim 1 or 2, wherein the liquid ammonia is added to the anolyte.

6. A process according to claim 1 or 2, wherein gaseous ammonia is added to the anolyte.

7. A process according to claim 1 or 2, wherein the starting concentration of the sodium sulfate solution is from about 0.1M to about the solubility limit.

8. A process according to claim 7, wherein the starting concentration of the sodium sulfate solution is from about 1M to about 3.5M.

9. A process according to claim 8, wherein the starting concentration of the sodium sulfate solution is from about 2M to about 3M.

10. A process according to claim 1 or 2, wherein the catholyte is an aqueous solution of sodium hydroxide having the starting concentration of from about 0.01M to about 9M.

11. A process according to claim 10, wherein the starting concentration of sodium hydroxide solution is about 3M.

12. A process according to claim 1 or 2, wherein the anolyte is an aqueous solution of ammonium sulfate having the starting concentration of from about 0.01M to about 3.5M.

13. A process according to claim 1 or 2, wherein the cation selective ion exchange is made of an organic polymer having sulphonate or carboxylate groups attached thereto.

14. A process according to claim 1 or 2, wherein the cation selective ion exchange membrane is a stable perfluorinated cation exchange membrane.

15. A process according to claim 1 or 2, wherein the cation selective ion exchange membrane is NAFION 902 or FLEMION FCA membrane.

16. A process according to claim 1 or 2, wherein the anion selective ion exchange membrane is made of an organic polymer having amino functionality attached thereto.

17. A process according to claim 1 or 2, wherein the anion selective ion exchange membrane is NEOSEPTA AMH membrane.

18. A process according to claim 1 or 2, wherein a low hydrogen overpotential cathode is used.

19. A process according to claim 18, wherein the cathode is made of a material selected from the group consisting of nickel, stainless steels and spinels.

20. A process according to claim 1 or 2, wherein a low oxygen overpotential anode is used.

21. A process according to claim 20, wherein the anode is a nobel metal oxide anode or DSA-O₂ anode.

22. A process according to claim 1 or 2, wherein the process is carried out in a batch mode.

23. A process according to claim 1 or 2, wherein the process is carried out in a continuous mode.

2. A process for producing sodium hydroxide and ammonium sulfate, which method comprises:

passing a solution of sodium sulfate through a central compartment of a three-compartment electrolytic cell having a cathode compartment and an anode compartment separated from the central compartment by a cation selective ion exchange membrane and an anion selective ion exchange membrane, respectively;

passing a catholyte through the cathode compartment and an anolyte through the anode compartment;

passing a direct electric current between an anode and a cathode located in the anode compartment and the cathode compartment, respectively, thus producing sodium hydroxide in the cathode compartment and sulfuric acid in the anode compartment;

at least partially neutralizing sulfuric acid produced in the anode compartment by adding ammonia to the anolyte.

24. A process for producing sodium hydroxide, which process comprises electrolysing an aqueous solution of sodium sulfate in an electrolytic cell having at least one anode compartment and at least one cathode compartment, said anode compartment containing an anolyte and having an anode located therein, said cathode compartment containing a catholyte and having a cathode located therein, said anode compartment and said cathode compartment being separated from the sodium sulfate solution by an anion selective ion exchange membrane and a cation selective ion exchange membrane, respectively, wherein during the process ammonia is added to the anolyte to at least partially neutralize sulfuric acid produced in the anode compartment, and wherein the cation selective ion exchange membrane is a stable perfluorinated cation exchange membrane, the anion selective ion exchange membrane is made of an organic polymer having amino functionality attached thereto, the cathode is a nickel cathode and the anode is a DSA-O₂ anode and sulfuric acid is neutralized to maintain the anolyte at a pH of from about 0.5 to about 3.5.