System for regenerating sodium hydroxide and sulfuric acid from waste water stream containing sodium and sulfate ions
A waste water treatment system including an electrolysis treatment system and three membrane concentration systems. The electrolysis treatment system includes a first chamber that receives waste water and produces treated waste water, a second chamber that receives first recycled water and produces dilute acid discharge, and a third chamber that receives second recycled water and produces dilute caustic discharge. An anion exchange membrane separates the first chamber from the second chamber. A cation exchange membrane separates the first chamber from the third chamber. The membrane concentration system receives the treated waste water and produces a concentrated aqueous sodium sulfate product and a pure water product. A first thermal concentration system receives the dilute acid discharge and produces first recycled water and a concentrated acid product. The second thermal concentration system receives the dilute caustic discharge and produces second recycled water and a concentrated aqueous sodium sulfate product.
1. A waste water treatment system comprising:
an electrolysis treatment system having:
a first chamber having an inlet to receive waste water and an outlet to produce treated waste water;
a second chamber having an inlet to receive first recycled water and an outlet to produce dilute acid discharge;
an anode contained in the second chamber;
a third chamber having an inlet to receive second recycled water and an outlet to produce dilute caustic discharge;
a cathode contained in the third chamber;
an anion exchange membrane (AEM) separating the first chamber from the second chamber; and
a cation exchange membrane (CEM) separating the first chamber from the third chamber;
a membrane concentration system having an inlet coupled to the outlet of the first chamber, a first outlet coupled to the inlet of the first chamber to produce a concentrated aqueous sodium sulfate product, and a second outlet to produce pure water product;
a first thermal concentration system having an inlet coupled to the outlet of the second chamber, a first outlet coupled to the inlet of the second chamber and producing the first recycled water, and a second outlet to produce a concentrated acid product; and
a second thermal concentration system having an inlet coupled to the outlet of the third chamber, a first outlet coupled to the inlet of the third chamber and producing the second recycled water, and a second outlet to produce a concentrated aqueous sodium sulfate product.
2. The waste water treatment system of claim 1 , wherein the waste water has a first ion content and the treated waste water has a second ion content that is less than the first ion content.
3. The waste water treatment system of claim 1 , wherein the first outlet of the membrane concentration system produces ionic saturated water.
4. The waste water treatment system of claim 3 , wherein the ionic saturated water comprises Na + /SO 4 2− saturated water.
5. The waste water treatment system of claim 1 , wherein the dilute acid discharge comprises less than 5 weight percent SO 4 2− .
6. The waste water treatment system of claim 1 , wherein the dilute caustic discharge comprises less than 5 weight percent Na + .
7. The waste water treatment system of claim 1 , wherein the concentrated acid product comprises between 15 wt % SO 4 2− and 50 wt % SO 4 2− .
8. The waste water treatment system of claim 1 , wherein the concentrated aqueous sodium sulfate product comprises between 15 wt % Na + and 50 wt % Na + .
9. The waste water treatment system of claim 1 , wherein at least one of the membrane concentration system, the first thermal concentration system, and the second thermal concentration system is an osmosis system.
10. The waste water treatment system of claim 1 , wherein at least one of the membrane concentration system, the first thermal concentration system, and the second thermal concentration system is a concentration driven system.
11. A method for treating waste water comprising:
by an electrolysis treatment system:
receiving waste water at an inlet of a first chamber;
receiving first recycled water at an inlet of a second chamber;
receiving second recycled water at an inlet of a third chamber;
migrating anions from the first chamber to the second chamber via an anion exchange membrane (AEM) separating the first chamber from the second chamber using an anode contained in the second chamber;
migrating cations from the first chamber to the third chamber via a cation exchange membrane (CEM) separating the first chamber from the third chamber using a cathode contained in the third chamber;
producing treated waste water at an outlet of the first chamber;
producing dilute acid discharge at an outlet of the second chamber; and
producing dilute caustic discharge at an outlet of the third chamber;
by a membrane concentration system:
receiving the treated waste water from the outlet of the first chamber;
producing saturated waste water;
returning the saturated waste water to the inlet of the first chamber; and
producing a pure water product;
by a first thermal concentration system:
receiving the dilute acid discharge from the outlet of the second chamber;
producing a concentrated acid product;
producing the first recycled water; and
returning the first recycled water to the inlet of the second chamber; and
by a second thermal concentration system:
receiving the dilute caustic discharge from the outlet of the third chamber;
producing a concentrated aqueous sodium sulfate product;
producing the second recycled water; and
returning the second recycled water to the inlet of the third chamber.
12. The method of claim 11 , wherein the waste water has a first ion content and the treated waste water has a second ion content that is less than the first ion content.
13. The method of claim 11 , wherein the membrane concentration system produces ionic saturated water.
14. The method of claim 13 , wherein the ionic saturated water comprises Na + /SO 4 2− saturated water.
15. The method of claim 11 , wherein the dilute acid discharge comprises less than 5 weight percent SO 4 2− .
16. The method of claim 11 , wherein the dilute caustic discharge comprises less than 5 weight percent Na + .
17. The method of claim 11 , wherein the concentrated acid product comprises between 15 wt % SO 4 2− and 50 wt % SO 4 2− .
18. The method of claim 11 , wherein the concentrated aqueous sodium sulfate product comprises between 15 wt % Na + and 50 wt % Na + .
19. The method of claim 11 , wherein at least one of the membrane concentration system, the first thermal concentration system, and the second thermal concentration system is an osmosis system.
20. The method of claim 11 , wherein at least one of the membrane concentration system, the first thermal concentration system, and the second thermal concentration system is a concentration driven system.