Concentrating aqueous solutions via hybridizing electrodialysis and other desalination techniques
An aqueous solution flows through a desalination system that separates the aqueous solution into purified water and concentrated brine. The concentrated brine is directed into an electrodialysis system that includes an anode and a cathode and at least two monovalent selective ion exchange membranes between the anode and the cathode. At least one of the monovalent selective ion exchange membranes separates at least one diluate channel from at least one concentrate channel in the electrodialysis system, and this membrane selectively allows at least one monovalent ion to pass through the membrane while blocking or inhibiting the transport therethrough of multi-valent ions. The concentrated brine flows through at least the concentrate channel while a voltage is applied to the anode and cathode; and additional aqueous solution flows through the diluate channel.
1. A method for concentrating aqueous solutions, comprising:
directing an aqueous solution through a desalination system that separates the aqueous solution into purified water and concentrated brine;
directing the concentrated brine into an electrodialysis system comprising an anode and a cathode and at least two monovalent selective ion exchange membranes between the anode and the cathode, wherein at least one of the monovalent selective ion exchange membranes separates at least one diluate channel with a comparatively diluted ion concentration from at least one concentrate channel with a comparatively concentrated ion concentration in the electrodialysis system, wherein each monovalent selective ion exchange membrane selectively allows at least one monovalent ion to pass through the membrane while blocking or significantly inhibiting the transport of multi-valent ions through the membrane;
flowing the concentrated brine through at least the at least one concentrate channel while applying a voltage to the anode and cathode; and
flowing additional aqueous solution mixed with concentrated brine from the desalination system through the at least one diluate channel such that the proportion of aqueous solution in the flow into the at least one diluate channel is lower than 0.61 or greater than 0.81, and wherein the ratio of the flow through the at least one diluate channel to the flow through the at least one concentrate channel is in a range from 0.3 to 81.
2. The method of claim 1 , wherein the desalination system is a reverse-osmosis system, comprising a reverse-osmosis membrane in a chamber; wherein purified water is passed through the membrane to a permeate side of the chamber; and wherein dissolved solutes are retained in the concentrated brine as retentate on an opposite side of the membrane upstream from the purified water and removed from the chamber.
3. The method of claim 2 , wherein the aqueous solution is seawater.
4. The method of claim 3 , wherein the aqueous solution flowing to system and the aqueous solution flowing to the diluate channels are of the at least one diluate channel have different salinity concentrations.
5. The method of claim 2 , wherein the proportion of aqueous solution in the flow into the at least one diluate channel is in a range from 0.81 to 0.95.
6. The method of claim 2 , further comprising directing an initial feed composition through a preliminary desalination system that produces outputs of substantially pure water and a desalination brine that serves as the aqueous solution.
7. The method of claim 2 , wherein the aqueous solution is seawater, and wherein the concentrated brine has a salinity greater than 35 g/kg and no greater than 70 g/kg.
8. The method of claim 1 , wherein the desalination system includes a high-pressure reverse-osmosis stage that operates with the aqueous solution flowing in or the concentrated brine flowing in at a pressure of 7 to 15 MPa on the feed side of the high-pressure reverse-osmosis membrane.
9. The method of claim 1 , wherein the aqueous solution comprises industrial waste water.
10. The method of claim 1 , wherein the application of the voltage to the anode and cathode maintains a current density of 200-1,500 A/m 2 across the monovalent selective ion exchange membrane.
11. The method of claim 1 , wherein the application of the voltage to the anode and cathode maintains a current density of 500-1,500 A/m 2 across the monovalent selective ion exchange membrane.
12. The method of claim 1 , further comprising:
extracting further-concentrated brine from the at least one concentrate channel of the electrodialysis system;
injecting the further concentrated brine into a crystallizer; and
crystallizing salt from the further concentrated brine in the crystallizer.
13. The method of claim 1 , further comprising employing nano-filtration, ultra-filtration, or lime-softening to treat the aqueous solution before it is directed through the desalination system.
14. The method of claim 1 , further comprising employing nano-filtration, ultra-filtration, or lime-softening to treat the aqueous solution before it is directed through the electrodialysis system.
15. The method of claim 1 , further comprising extracting further-concentrated brine from the at least one concentrate channel of the electrodialysis system and directing the further-concentrated brine through a system selected from any of (a) a mechanical-vapor-compression system, (b) a multi-effect evaporator, (c) a membrane-distillation system, and (d) a counterflow-reverse-osmosis system to concentrate the further-concentrated brine still further.
16. The method of claim 1 , wherein the electrodialysis system is split into separate sub-systems in fluid communication with each other with some sub-systems exclusively having electrodialysis membranes that are not monovalent selective and other sub-systems exclusively having monovalent selective ion exchange membranes.
17. The method of claim 1 , further comprising extracting further-diluted brine from the at least one diluate channel of the electrodialysis system, wherein the further-diluted brine has a reduced concentration of monovalent ions.
18. The method of claim 1 , further comprising extracting further-diluted brine from the at least one diluate channel of the electrodialysis system and directing the further-diluted brine through a nanofiltration system that separates the diluted brine into a permeate stream that is richer in monovalent ions than a retentate stream that is richer in non-monovalent ions than the permeate stream.
19. The method of claim 18 , wherein the retentate stream from the nanofiltration system is fed to another industrial facility in need of monovalent-free waters.
20. The method of claim 18 , wherein the permeate stream has a majority of monovalent ions and is comparatively sparse in divalent ions is mixed with the aqueous solution and recirculated back to the desalination system.
21. The method of claim 18 , further comprising extracting further-concentrated brine from the at least one concentrate channel of the electrodialysis system and directing the further-concentrated brine through a system selected from (a) a mechanical-vapor-compression system, (b) a multi-effect evaporator, (c) a membrane-distillation system, and (d) a counterflow-reverse-osmosis system to concentrate the further-concentrated brine still further and to achieve zero liquid discharge desalination, wherein the retentate stream from the nanofiltration system is fed to other industrial facilities in need of monovalent-free waters, and wherein the permeate stream has a majority of monovalent ions and is comparatively sparse in divalent ions is mixed with the aqueous solution and recirculated back to the desalination system.