Membraneless seawater desalination

Patent metadata

Field	Value
Publication number	US-9932251-B2
Application number	US-201314136541-A
Country	US
Kind code	B2
Filing date	Dec 20, 2013
Priority date	Dec 21, 2012
Publication date	Apr 3, 2018
Grant date	Apr 3, 2018

Abstract

Disclosed are microfluidic devices and systems for the desalination of water. The devices and systems can include an electrode configured to generate an electric field gradient in proximity to an intersection formed by the divergence of two microfluidic channels from an inlet channel. Under an applied bias and in the presence of a pressure driven flow of saltwater, the electric field gradient can preferentially direct ions in saltwater into one of the diverging microfluidic channels, while desalted water flows into second diverging channel. Also provided are methods of using the devices and systems described herein to decrease the salinity of water.

First claim

What is claimed is:

1. A microfluidic device comprising
(a) a desalination unit comprising an inlet channel fluidly connected to a dilute outlet channel and a concentrated outlet channel, wherein the dilute outlet channel and the concentrated outlet channel diverge from the inlet channel at an intersection; and
(b) an electrode in electrochemical contact with the desalination unit in proximity to the intersection;
wherein the electrode is configured to generate an electric field gradient in proximity to the intersection.

2. The device of claim 1 , wherein the electrode comprises an anode.

3. The device of claim 1 , wherein the inlet channel has a width of from about 150 microns to about 25 microns.

4. The device of claim 1 , wherein the dilute outlet channel, the concentrated outlet channel, or both the dilute outlet channel and the concentrated outlet channel have a width of from about 80 microns to about 10 microns.

5. The device of claim 1 , wherein the sum of the area of a cross-section of dilute outlet channel and the area of a cross-section of the concentrated outlet channel is substantially equal to the area of a cross-section of the inlet channel.

6. The device of claim 1 , wherein the angle formed between the dilute outlet channel and the concentrated outlet channel at the intersection is 60 degrees or less.

7. The device of claim 1 , further comprising an auxiliary channel fluidly isolated from the desalination unit.

8. The device of claim 7 , wherein the electrode comprises a bipolar electrode electrochemically connecting the desalination unit and the auxiliary channel.

9. The device of claim 8 , wherein the bipolar electrode comprises an anode in electrochemical contact with the desalination unit and a cathode in electrochemical contact with the auxiliary channel.

10. The device of claim 7 , wherein the auxiliary channel comprises
a second desalination unit comprising an inlet channel fluidly connected to a dilute outlet channel and a concentrated outlet channel, wherein the dilute outlet channel and the concentrated outlet channel diverge from the inlet channel at an intersection; and an electrode in electrochemical contact with the second desalination unit;
wherein the electrode is configured to generate an electric field gradient in proximity to the intersection where the dilute outlet channel and the concentrated outlet channel diverge from the inlet channel.

11. A water purification system comprising a plurality of devices defined by claim 1 , wherein the inlet channels of the plurality of devices are fluidly connected to a water inlet, and the dilute outlet channels of the plurality of devices are fluidly connected to a water outlet.

12. The device of claim 1 , wherein the electrode is formed from a conductive material selected from the group consisting of a metal, a metal alloy, a metal oxide, a conductive carbon material, or a combination thereof.

13. The device of claim 1 , wherein the electrode is positioned at a location relative to the intersection such that the electric field gradient generated in proximity to the intersection can preferentially direct ions flowing through the inlet channel into the concentrated outlet channel.

14. The device of claim 1 , wherein the electrode is positioned on or within the floor of the inlet channel.

15. The device of claim 1 , wherein the electrode is positioned upstream of the intersection, and within about 500 microns of the intersection.

16. The device of claim 1 , wherein the electrode is positioned downstream of the intersection, and within about 100 microns of the intersection.

17. The device of claim 1 , wherein the electrode is positioned within about 50 microns of the intersection.

18. The device of claim 1 , wherein the dilute outlet channel has a width, and wherein a surface of the electrode in electrochemical contact with the desalination unit has a width of at least 50% of the width of the dilute outlet channel.

19. A method of decreasing the salinity of water comprising
(a) providing a flow of saltwater through the inlet channel of the device defined by claim 1 ;
(b) applying a potential bias to generate an electric field gradient that influences the flow of ions through the desalination unit of the device defined by claim 1 ; and
(c) collecting water from the dilute outlet channel of the device defined by claim 1 ;
wherein the water collected from the dilute outlet channel of the device defined by claim 1 has a lower electrical conductivity than the saltwater.

20. The method of claim 19 , wherein the saltwater comprises seawater.

21. The method of claim 19 , wherein the saltwater comprises brackish water.

22. The method of claim 19 , wherein the conductivity of the water collected does not exceed about 80% of the conductivity of the saltwater.

23. The method of claim 19 , wherein the water collected has a conductivity of less than about 0.1 S/m.

24. The method of claim 19 , wherein the water collected has a conductivity of from about 0.05 S/m to about 0.005 S/m.

25. The method of claim 19 , wherein the water collected has a conductivity of from about 0.005 S/m to about 5.5×10 −6 S/m.

26. The method of claim 19 , wherein potential bias applied ranges from about 1 volt to about 10 volts.

27. The method of claim 19 , wherein the rate of flow of the saltwater through the desalination unit of the device defined by claim 1 ranges from about 0.01 to about 1 microliter per minute.

28. A method of decreasing the salinity of water comprising
(a) flowing saltwater through a desalination unit comprising an inlet channel fluidly connected to a dilute outlet channel and a concentrated outlet channel, wherein the dilute outlet channel and concentrated outlet channel diverge from the inlet channel at an intersection; and
(b) performing a faradaic reaction at an electrode positioned in proximity to the intersection to generate an electric field gradient;
wherein the electric field gradient directs ions in the saltwater away from the dilute outlet channel.

Assignees

• Univ Texas

Inventors

• Crooks Richard A
• Knust Kyle N
• Perdue Robbyn K

Classifications

• C02F2103/08

  Seawater, e.g. for desalination · CPC title

• C02F1/4604 Primary

  for desalination of seawater or brackish water · CPC title

• C02F1/4696

  electrophoresis · CPC title

• C02F2001/46128

  Bipolar electrodes · CPC title