Electrical energy generation in fluidic channels and membranes using spontaneous capillary flow

Patent metadata

Field	Value
Publication number	US-10944123-B2
Application number	US-201816141657-A
Country	US
Kind code	B2
Filing date	Sep 25, 2018
Priority date	Sep 25, 2017
Publication date	Mar 9, 2021
Grant date	Mar 9, 2021

Abstract

Described herein are systems and methods for the generation of electric current and/or electric potential utilizing micro- or nano-channels and capillary flow, including fluidic or microfluidic batteries and electrochemical cells. The provided systems and methods use capillary force to promote fluid flow through micro- and nano-fluidic channels by evaporating fluid at one terminus of the channel, and the resulting fluid flow generates electric potential and or current. Advantageously, the described systems and methods remove the need for pressurized vessels or external pumps, increasing net energy generation and decreasing complexity and size of potential fluidic batteries.

First claim

I claim:

1. A microfluidic electrochemical system comprising:
a fluid inlet for introduction of an aqueous solvent;
a microfluidic channel in fluid communication with said fluid inlet;
wherein said microfluidic channel has charged walls; and
wherein said microfluidic channel has an average length of greater than or equal to 1 μm and an effective cross sectional diameter of less than or equal to 10 μm;
wherein said microfluidic channel comprises a charged membrane positioned along a surface of said microfluidic channel; and

an evaporation chamber in fluid communication with said microfluidic channel;
wherein evaporation of said solvent in said evaporation chamber drives flow of said solvent through said microfluidic channel due to capillary force thereby generating an electrical current flowing through said solvent in the direction of said microfluidic channel.

2. The system of claim 1 further comprising a first electrode positioned proximate to said fluid inlet and a second electrode positioned proximate to said evaporation chamber.

3. The system of claim 1 further comprising a plurality of fluid inlets operably connected to a plurality of microfluidic channels operably connected to at least one evaporation chamber configured to form a microfluidic channel array;
wherein said array is configured such that evaporation of said solvent in said at least one evaporation chamber drives flow of said solvent through each of said microfluidic channels due to capillary force thereby generating an electrical current flowing through each of said microfluidic channels.

4. The system of claim 3 further comprising a plurality of evaporation chambers;
wherein each of said microfluidic channels is in fluidic communication with an individual evaporation chamber.

5. The system of claim 1 , wherein said charged membrane is a sulfonated membrane.

6. The system of claim 1 , wherein said charged membrane is Nafion, a sulfonated polystyrene membrane or any combination thereof.

7. The system of claim 1 , wherein said microfluidic channel is supported by or embedded in a substrate.

8. The system of claim 7 , wherein said substrate is a glass plate, a borosilicate glass plate, silicon, a polymer or a combination thereof.

9. The system of claim 1 , wherein said solvent is selected from the group consisting of: water, deionized water; NaCl, KCl, LiCl, methanol, ethanol any combination thereof.

10. A microfluidic electrochemical system comprising:
a fluid inlet for introduction of an aqueous solvent;
a microfluidic channel in fluid communication with said fluid inlet;
wherein said microfluidic channel has charged walls; and
wherein said microfluidic channel has an average length of greater than or equal to 1 μm and an effective cross sectional diameter of less than or equal to 10 μm;
wherein said microfluidic channel comprises a charged membrane positioned along a surface of said microfluidic channel; and

an evaporation chamber in fluid communication with said microfluidic channel;
wherein said evaporation chamber further comprises a polyelectrolyte coating to increase a rate of evaporation of said solvent;
wherein evaporation of said solvent in said evaporation chamber drives flow of said solvent through said microfluidic channel due to capillary force thereby generating an electrical current flowing through said solvent in the direction of said microfluidic channel.

11. The system of claim 10 , wherein said polyelectrolyte coating is polydiallyldimethylammonium chloride (PDADMA).

12. The system of claim 1 , wherein said evaporation chamber further comprises a patterned surface to increase the rate of evaporation of said solvent.

13. The system of claim 1 , wherein said microfluidic channel is configured to provide a gradient along the axial length of said microfluidic channel.

14. The system of claim 3 , wherein said microfluidic channel array is configured to provide a gradient along the axial length of said plurality of microfluidic channels.

15. The system of claim 14 , wherein said gradient is a temperature gradient or an ionic concentration gradient.

16. A microfluidic electrochemical system comprising:
a fluid inlet for introduction of an aqueous solvent;
a microfluidic channel array comprising:
a plurality of fluid inlets for introduction of an aqueous solvent;
a plurality of microfluidic channels each in fluid communication with said fluid inlet;
wherein each of said microfluidic channels has charged walls; and
wherein each of said microfluidic channels has an average length of greater than or equal to 1 μm and an effective cross sectional diameter of less than or equal to 10 μm;
wherein said microfluidic channel array is configured to provide a gradient along an axial length of said plurality of microfluidic channels;

a charged membrane in fluid communication with said microfluidic channel array;
an evaporation chamber in fluid communication with said microfluidic channel;
wherein evaporation of said solvent in said evaporation chamber drives flow of said solvent through said microfluidic channel due to capillary force thereby generating an electrical current flowing through said solvent in the direction of said microfluidic channel.

17. The system of claim 16 , wherein said microfluidic channel array is configured to provide a gradient across said charged membrane.

18. The system of claim 16 , wherein said gradient is a temperature gradient or an ion concentration gradient.

19. The system of claim 16 , wherein said charged membrane is Nafion, a sulfonated polystyrene membrane or any combination thereof.

20. The system of claim 16 , wherein said charged membrane is positioned proximate to said evaporation chamber.

21. A microfluidic electrochemical system comprising:
a fluid inlet for introduction of an aqueous solvent;
a charged membrane supported by a substrate and in fluid communication with said fluid inlet; wherein said substrate is configured to provide a gradient along a flow path of said charged membrane;
an evaporation chamber in fluid communication with said charged membrane;
wherein evaporation of said solvent in said evaporation chamber drives flow of said solvent charged membrane along said flow path due to capillary force thereby generating an electrical current flowing through said solvent in the direction of said flow path.

22. The system of claim 21 , wherein said gradient is a temperature gradient or an ion concentration gradient.

Assignees

• Univ Wyoming

Inventors

• Dutta Debashis

Classifications

• Y02P70/50

  Manufacturing or production processes characterised by the final manufactured product · CPC title

• H01M2010/0495

  Nanobatteries · CPC title

• H01M8/04089

  of gaseous reactants · CPC title

• H01M4/602

  Polymers · CPC title

• Y02E60/50

  Fuel cells · CPC title