Electrodialysis processes using an organic solvent for separating dissolved species
Provided are water treatment systems and methods of treating water that include separating dissolved salts from a feed stream using an organic solvent brine stream. For example, described are water treatment systems comprising: an electrodialysis device comprising an inlet feed stream, an inlet brine stream, an outlet product stream, and an outlet brine stream; and a precipitation tank comprising an inlet stream and an outlet stream, wherein the inlet stream of the precipitation tank comprises the outlet brine stream of the electrodialysis device, and the inlet brine stream of the electrodialysis device comprises the outlet stream of the precipitation tank, and wherein inlet brine stream and outlet brine stream comprises an organic solvent.
1. A water treatment system for separating dissolved salts from a feed stream comprising:
an inlet feed stream comprising dissolved salts;
an inlet brine stream comprising at least 60 wt. % ethanol and/or isopropanol;
an electrodialysis unit configured to remove the dissolved salts from the inlet feed stream and add the dissolved salt to the inlet brine stream to form an outlet brine stream;
a precipitation tank configured to precipitate the dissolved salts out of the outlet brine stream from the electrodialysis unit, wherein the precipitation tank comprises a flash valve configured to flash off a fraction of the solution of outlet brine stream as vapor;
a supernatant brine stream from the precipitation tank comprising at least 60 wt. % ethanol and/or isopropanol, wherein the supernatant brine stream is sent to the electrodialysis unit to be at least a portion of the inlet brine stream;
a distillation column configured to receive the vapor from the precipitation tank and generate a vapor stream comprising a higher concentration of ethanol and/or isopropanol than the vapor from the precipitation tank; and
a condenser configured to condense the vapor stream from the distillation column, wherein the condensed vapor stream is sent to the electrodialysis unit to be at least a portion of the inlet brine stream.
2. The water treatment system of claim 1 , wherein a salt concentration of a product stream of the electrodialysis unit is greater than a salt concentration of the outlet brine stream of the electrodialysis unit.
3. The water treatment system of claim 1 , wherein the inlet brine stream and the outlet brine stream of the electrodialysis unit comprise a water and organic solvent composition.
4. The water treatment system of claim 3 , wherein the water and organic solvent composition of the inlet brine stream comprises 2-20 wt. % water.
5. The water treatment system of claim 1 , wherein the salt concentration of a product stream of the electrodialysis unit is less than that of the inlet feed stream.
6. The water treatment system of claim 1 , wherein the salt concentration of a product stream of the electrodialysis unit is 50-80 wt. % that of the inlet feed stream.
7. The water treatment system of claim 1 , wherein the salt concentration of the inlet brine stream is less than that of the outlet brine stream.
8. The water treatment system of claim 1 , wherein the salt concentration of the inlet brine stream is 30-60 wt. % that of the outlet brine stream.
9. The water treatment system of claim 1 , wherein the salt concentration of the outlet brine stream is less than that of a product stream of the electrodialysis unit.
10. The water treatment system of claim 1 , wherein a salt concentration of the outlet brine stream is 30-70 wt. % that of a product stream of the electrodialysis unit.
11. The water treatment system of claim 1 , wherein the supernatant brine stream of the precipitation tank comprises a supernatant.
12. The water treatment system of claim 1 , comprising a screw conveyor configured to remove precipitated salts from the precipitation tank.
13. The water treatment system of claim 1 , comprising a solvent recovery step configured to replenish organic solvent in the inlet brine stream.
14. The water treatment system of claim 1 , wherein the inlet feed stream is controlled to a pH of 9 or less.
15. The water treatment system of claim 1 , wherein the inlet feed stream is controlled to a pH of 7 or less.
16. The water treatment system of claim 1 , wherein the dissolved salts comprise one or more of sodium chloride, lithium carbonate, boric acid, sodium sulfate, lithium hydroxide, sodium bicarbonate, or potassium chloride.