Return flow system for ion concentration polarization (ICP) desalination

Patent metadata

Field	Value
Publication number	US-11780754-B2
Application number	US-202016839152-A
Country	US
Kind code	B2
Filing date	Apr 3, 2020
Priority date	Jan 25, 2018
Publication date	Oct 10, 2023
Grant date	Oct 10, 2023

Abstract

The present invention provides return flow ICP and ED systems and methods that can be used for water desalination and/or concentration of a wide range of target brine and other aqueous and contaminated streams.

First claim

What is claimed is:

1. A method of purifying and/or concentrating a first water stream containing impurities comprising the steps of:
a. directing the first water stream into an inlet of a channel as a feed stream that comprises water and charged contaminants, wherein the channel is defined, at least in part, by a first ion exchange membrane and a second ion exchange membrane, wherein the ion exchange membranes are juxtaposed and characterized by the same charge,
wherein the channel is further characterized as having an inlet end and a return flow end, wherein the inlet end is the end of the channel at which the inlet is located, and the return flow end is the end of the channel downstream from the inlet end,
the channel further comprising a first outlet and a second outlet, wherein the inlet and at least the first outlet are located on the inlet end of the channel and are separated by a first porous membrane that traverses the length of the channel between the ion exchange membranes and terminates at a return flow zone, wherein the return flow zone is a section of the channel at the return flow end, and wherein the return flow end is at least partially closed;

b. applying an electric field across the channel causing formation of a charged-contaminant-depletion zone comprising a purified water stream and formation of a charged-contaminant-enrichment zone comprising a concentrated charged-contaminant aqueous stream,
wherein at least part of the feed stream enters the return flow zone and forms a first return flow stream that flows to the opposing side of the first porous membrane, the first return flow stream flowing in the direction of the first outlet, and at least part of the feed stream, including the water and the charged contaminants, adjacent to the first porous membrane flowing through the first porous membrane joining the first return flow stream,
wherein the purified water stream is the stream directed to the first or the second outlet, and the concentrated charged-contaminant aqueous stream is the stream directed to the other of the first and the second outlet; and

c. collecting the purified water stream and/or the concentrated charged-contaminant aqueous stream from the first and/or second outlet.

2. The method of claim 1 , wherein the ion exchange membranes are cation exchange membranes, wherein each cation exchange membrane has a cathodic side and an anodic side.

3. The method of claim 1 , wherein the ion exchange membranes are anion exchange membranes.

4. The method of claim 1 , wherein the first porous membrane is a non-ionic porous membrane.

5. The method of claim 1 , wherein the second outlet is located at the return flow end.

6. The method of claim 1 , wherein the second outlet is located at the inlet end.

7. The method of claim 1 , wherein the electric field is created by an electrode and a ground each located external and parallel to the channel.

8. The method of claim 7 , wherein the electrode forms a second channel with the first ion exchange membrane and the ground forms a third channel with the second ion exchange membrane.

9. The method of claim 8 , wherein the second and third channels are filled with an electrolyte solution.

10. The method of claim 9 , wherein the electrolyte solution is the first water stream.

11. The method of claim 2 , wherein the first outlet is located on the cathodic side of the first porous membrane, the inlet is located on the anodic side of the first porous membrane, and the purified water stream is directed to the first outlet.

12. The method of claim 11 , wherein the second outlet is located at the return flow end, and optionally on the anodic side of the first porous membrane.

13. The method of claim 2 , wherein the first outlet is located on the anodic side of the first porous membrane, the inlet is located on the cathodic side of the first porous membrane, and the concentrated water stream is directed to the first outlet.

14. The method of claim 13 , wherein the second outlet is located at the return flow end, and optionally on the cathodic side of the first porous membrane.

15. The method of claim 1 , wherein the second outlet is located on the inlet end of the channel, wherein the inlet is located between the first outlet and the second outlet, and wherein the inlet and the second outlet are separated by a second porous membrane that traverses the length of the channel between the ion exchange membranes and terminates at the return flow zone, and wherein the return flow end is fully closed.

16. The method of claim 15 , wherein the ion exchange membranes are cation exchange membranes.

17. The method of claim 15 , wherein the ion exchange membranes are anion exchange membranes.

18. The method of claim 15 , wherein the second porous membrane is a non-ionic porous membrane.

19. The method of claim 16 , wherein the first outlet is located on the cathodic side of the first porous membrane, and the second outlet is located on the anodic side of the second porous membrane, wherein the purified water stream is directed to the first outlet, and the concentrated charged-contaminant aqueous stream is directed to the second outlet,
wherein at least part of the feed stream enters the return flow zone and forms a second return flow stream that flows to the opposing side of the second porous membrane and flows in the direction of the second outlet, and at least part of the feed stream, including the water and the charged contaminants, adjacent to the second porous membrane flowing through the second porous membrane joining the second return flow stream.

20. The method of claim 1 , wherein the first water stream comprises salt.

21. The method of claim 20 , wherein the first water stream is brine.

22. The method of claim 1 , wherein the first water stream comprises biomolecules.

Assignees

• Massachusetts Inst Technology

Inventors

• Han Jongyoon
• Yoon Junghyo

Classifications

• C02F1/4695 Primary

  electrodeionisation · CPC title

• C02F1/469

  by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis · CPC title

• C02F1/4693 Primary

  electrodialysis · CPC title

• C02F2201/46

  Apparatus for electrochemical processes · CPC title

• Y02A20/124

  Water desalination · CPC title