Charge-free mixing entropy battery

Patent metadata

Field	Value
Publication number	US-2016344069-A1
Application number	US-201615157126-A
Country	US
Kind code	A1
Filing date	May 17, 2016
Priority date	May 18, 2015
Publication date	Nov 24, 2016
Grant date	—

Abstract

Described herein is a mixing entropy battery including a cationic electrode for sodium ion exchange and an anionic electrode for chloride ion exchange, where the cationic electrode includes at least one Prussian Blue material, and where the mixing entropy battery is configured to convert salinity gradient into electricity.

First claim

What is claimed is:

1 . An electrochemical system comprising:
a battery including an anionic electrode and a cationic electrode; a first source of a first solution; a second source of a second solution, wherein the second solution has a greater salinity than the first solution; and a fluid conveyance mechanism connected between the battery and each of the first source and the second source, wherein the electrochemical system is configured such that:
during a first discharge stage of the battery, the anionic electrode and the cationic electrode are in contact with the first solution, and
during a second discharge stage of the battery, the anionic electrode and the cationic electrode are in contact with the second solution, and
wherein the fluid conveyance mechanism is configured to exchange the first solution with the second solution between the first discharge stage and the second discharge stage.

2 . The electrochemical system of claim 1 , wherein a voltage of the battery is negative during at least a portion of the first discharge stage.

3 . The electrochemical system of claim 1 , wherein a voltage of the battery is positive during at least a portion of the second discharge stage.

4 . The electrochemical system of claim 1 , further comprising a load connected between the anionic electrode and the cationic electrode, and wherein a current is configured to flow through the load from the anionic electrode to the cationic electrode during at least a portion of the first discharge stage.

5 . The electrochemical system of claim 1 , further comprising a load connected between the anionic electrode and the cationic electrode, and wherein a current is configured to flow through the load from the cationic electrode to the anionic electrode during at least a portion of the second discharge stage.

6 . The electrochemical system of claim 1 , wherein the cationic electrode includes a Prussian Blue material.

7 . The electrochemical system of claim 1 , wherein the anionic electrode includes polypyrrole.

8 . The electrochemical system of claim 1 , wherein the fluid conveyance mechanism is configured to exchange the second solution with the first solution between the second discharge stage and the first discharge stage.

9 . A method of converting salinity gradient into electricity, comprising:
providing a battery including an anionic electrode and a cationic electrode; discharging the battery while the anionic electrode and the cationic electrode are in contact with a first solution having a first salinity; exchanging the first solution with a second solution having a second salinity, wherein the second salinity is greater than the first salinity; and discharging the battery while the anionic electrode and the cationic electrode are in contact with the second solution.

10 . The method of claim 9 , wherein a voltage of the battery is negative during at least a portion of discharging the battery while the anionic electrode and the cationic electrode are in contact with the first solution.

11 . The method of claim 9 , wherein a voltage of the battery is positive during at least a portion of discharging the battery while the anionic electrode and the cationic electrode are in contact with the second solution.

12 . The method of claim 9 , wherein discharging the battery while the anionic electrode and the cationic electrode are in contact with the first solution includes flowing a current from the anionic electrode to the cationic electrode.

13 . The method of claim 9 , wherein discharging the battery while the anionic electrode and the cationic electrode are in contact with the second solution includes flowing a current from the cationic electrode to the anionic electrode.

14 . The method of claim 9 , wherein the cationic electrode includes a Prussian Blue material.

15 . The method of claim 9 , wherein the anionic electrode includes polypyrrole.

Assignees

• Univ Leland Stanford Junior

Inventors

• Ye Meng
• Cui Yi
• Pasta Mauro
• Xie Xing
• Criddle Craig S
• Davey Vaishnav V

Classifications

• H01M10/44 Primary

  Methods for charging or discharging (circuits for charging H02J7/00) · CPC title

• Y02E60/50

  Fuel cells · CPC title

• Y02E60/10

  Energy storage using batteries · CPC title

• Y02E10/30

  Energy from the sea, e.g. using wave energy or salinity gradient · CPC title

• H01M8/227

  Dialytic cells or batteries; Reverse electrodialysis cells or batteries · CPC title