Electrochemical desalination system

Patent metadata

Field	Value
Publication number	US-10821395-B2
Application number	US-201816200289-A
Country	US
Kind code	B2
Filing date	Nov 26, 2018
Priority date	Feb 7, 2018
Publication date	Nov 3, 2020
Grant date	Nov 3, 2020

Abstract

An electrodialytic battery system comprises an electrodialysis apparatus having first and second reservoirs, wherein concentration of an input solution in the first reservoir increases and concentration of the input solution decreases in the second reservoir during an operation mode. A first redox-active electrolyte chamber comprises a first electrode and a first solution of a first redox-active electrolyte material and has a reversible redox reaction with the first electrolyte material to drive an ion into the first reservoir. A second redox-active electrolyte chamber comprises a second electrode and a second solution of a redox-active electrolyte material and has a reversible redox reaction with the second electrolyte material to accept an ion from the second reservoir. A first type of membrane is disposed between the first and second reservoirs, and a second type of membrane, different from the first type, is disposed between the respective electrode chambers and reservoirs.

First claim

What is claimed is:

1. A system, comprising:
an electrodialytic battery unit, comprising:
a first reservoir comprising an input and an output, wherein the concentration of a first input solution of at least one salt dissolved in a solvent is changed from a first concentration to a second concentration during an operation mode;
a second reservoir comprising an input and an output, wherein the concentration of a second input solution of at least one salt dissolved in a solvent is changed, from a third concentration to a fourth concentration, in the opposite manner as the first input solution in the first reservoir during the operation mode;
a first redox-active electrolyte chamber comprising at least one first electrode and a first solution of a redox-active electrolyte material and configured to have a reversible redox reaction with the first redox-active electrolyte material to drive at least one ion into, or accept at least one ion from, the first input solution having the first concentration in the first reservoir;
a second redox-active electrolyte chamber comprising at least one second electrode and a second solution of a redox-active electrolyte material and configured to have a reversible redox reaction with the second redox-active electrolyte material to accept at least one ion from, or drive at least one ion into, the second input solution having the third concentration in the second reservoir;
a first type of membrane disposed between the first and second reservoirs; and
a second type of membrane, different from the first type, disposed between the first redox-active electrolyte chamber and the first reservoir and disposed between the second redox-active electrolyte chamber and the second reservoir.

2. The system of claim 1 , wherein the solvent of the first and second input solutions is water.

3. The system of claim 1 , wherein the first and second input solutions comprise at least one of seawater, groundwater, and pretreated waters thereof.

4. The system of claim 1 , wherein the at least one salt in at least one of the first and second input solutions is at least one of calcium chloride, lithium chloride, and lithium bromide.

5. The system of claim 1 , wherein at least one of the redox-active electrolyte materials is a ferrocene derivative, a viologen derivative, and ferrocyanide/ferricyanide.

6. The system of claim 1 , wherein one of the first and second electrodes comprises zinc and the solution the zinc electrode is in contact with comprises zinc (II).

7. The system of claim 1 , wherein one type of membrane comprises an anion exchange membrane and the other type of membrane comprises a cation exchange membrane.

8. The system of claim 1 , wherein the second type of membrane disposed between the first redox-active electrolyte chamber and the first reservoir, the first reservoir, the first type of membrane, and the second reservoir comprise a first cell, and a second cell having the same structure as the first cell is disposed between the first cell and the second electrode.

9. The system of claim 1 , further comprising a switching unit coupled to the outputs of the first and second reservoirs and an electrodialysis apparatus is coupled to at least one output of the switching unit, and the electrodialysis apparatus comprises a second electrodialytic battery unit.

10. The system of claim 1 , further comprising a switching unit coupled to the outputs of the first and second reservoirs and a second desalination system is coupled to at least one output of the switching unit, wherein the second desalination system uses a water treatment process other than that of the electrodialytic battery unit.

11. The system of claim 1 , wherein the operation mode is configured to be a charge mode or a discharge mode, wherein the charge mode comprises driving ions from the first electrode or first redox-active electrolyte material, and from the second reservoir, into the first reservoir forming a first salinate stream and driving ions from the second reservoir into the second electrode or second redox-active electrolyte material forming a first desalinate stream, and the discharge mode comprises driving ions from the second electrode or second redox-active electrolyte material, and from the first reservoir, into the second reservoir forming a second salinate stream, and driving ions from the first reservoir into the first electrode or first redox-active electrolyte material forming a second desalinate stream while releasing stored energy as output power.

12. The system of claim 11 , further comprising a holding tank configured to store at least one of the first and second desalinate streams, the system further configured to operate in an electrodialysis mode comprising using the solvent from the holding tank as the first and second input solutions to the first and second reservoirs and forming a third salinate stream and a third desalinate stream.

13. The system of claim 12 , wherein the third desalinate stream comprises water having a salt concentration of not more than about 0.5 ppt.

14. The system of claim 1 , wherein one of the first reservoir and the second reservoir generates a desalinated output during a charge mode, a discharge mode, and an electrodialysis mode.

15. The system of claim 1 , wherein the first solution and the second solution are different.

16. The system of claim 1 , wherein at least one of the redox-active electrolyte materials is a flow battery reactant.

17. A method for storing, or discharging, energy while separating solvent from a salt dissolved in the solvent, comprising:
providing an electrodialytic battery unit, comprising:
a first reservoir comprising an input and an output, wherein the concentration of an input solution of at least one salt dissolved in a solvent is changed from a first concentration to a second concentration during an operation mode;
a second reservoir comprising an input and an output, wherein the concentration of the input solution of at least one salt dissolved in a solvent is changed, from a third concentration to a fourth concentration, in the opposite manner as the input solution in the first reservoir during the operation mode;
a first redox-active electrolyte chamber comprising at least one first electrode and a first solution of a redox-active electrolyte material and configured to have a reversible redox reaction with the first redox-active electrolyte material to drive at least one ion into, or accept at least one ion from, the input solution having the first concentration in the first reservoir;
a second redox-active electrolyte chamber comprising at least one second electrode and a second solution of a redox-active electrolyte material and configured to have a reversible redox reaction with the second redox-active electrolyte material to accept at least one ion from, or drive at least one ion into, the input solution having the third concentration in the second reservoir;
a first type of membrane disposed between the first and second reservoirs; and
a second type of membrane, different from the first type, disposed between the first redox-active electrolyte chamber and the first reservoir and disposed between the second redox-active electrolyte chamber and the second reservoir; and

operating the electrodialytic battery unit in a first mode, generating a first output stream that is higher in concentration than the input solution, and a second output stream that is lower in concentration than the input solution.

18. The method of claim 17 , wherein the first mode is one of a charge mode, a discharge m

Assignees

• Palo Alto Res Ct Inc

Inventors

• Beh Eugene S
• Desai Divyaraj
• Benedict Michael
• Rivest Jessica Louis Baker

Classifications

• B01D61/463

  comprising the membrane sequence AC or CA, where C is a cation exchange membrane · CPC title

• B01D2313/50

  Specific extra tanks · CPC title

• B01D61/462

  comprising the membrane sequence AA, where A is an anion exchange membrane · CPC title

• B01D61/423

  comprising multiple electrodialysis steps · CPC title

• B01D2313/367

  Renewable energy sources, e.g. wind or solar sources · CPC title