Method for producing high-purity electrolyte for vanadium redox flow battery using catalytic reactor

Patent metadata

Field	Value
Publication number	US-10978728-B2
Application number	US-201916382599-A
Country	US
Kind code	B2
Filing date	Apr 12, 2019
Priority date	Apr 12, 2019
Publication date	Apr 13, 2021
Grant date	Apr 13, 2021

Abstract

The present invention relates to a method for producing a 3- to 3.5-valent vanadium solution from a 4-valent vanadium solution by a catalytic reaction in the presence of a reducing agent, which generates a gas product during oxidation; a method for producing an electrolyte for a vanadium redox flow battery; and an apparatus for producing a liquid electrolyte for a vanadium redox flow battery. The present invention is characterized in that when a 3- to 3.5-valent vanadium electrolyte is produced from a 4-valent vanadium electrolyte by a catalytic reaction in the presence of a reducing agent, which generates a gas product during oxidation, the gas product produced in the catalytic reaction is captured with inert gas bubbles, which are carrier gases, and is removed from the reaction solution of the catalytic reaction by gas-liquid phase separation, thereby accelerating the catalytic reaction towards the forward reaction.

First claim

What is claimed is:

1. A method for producing an electrolyte for a vanadium redox flow battery, comprising:
a first step of purging the interior of a first vessel for supplying a 4-valent vanadium solution accommodating a 4-valent vanadium solution with an inert purge gas to prevent oxidation of the 4-valent vanadium solution;
a second step of supplying the inert gas which escaped from the first vessel for supplying a 4-valent vanadium solution after the first step into the interior of a catalytic reactor, in which a 3- to 3.5-valent vanadium solution is produced from the 4-valent vanadium solution by a catalytic reaction in the presence of a reducing agent, which generates a gas product during oxidation, and capturing the gas product of the catalytic reaction with gas bubbles, followed by subjecting the gas product to gas-liquid phase separation from the reaction solution of the catalytic reaction, thereby accelerating the catalytic reaction towards the forward reaction; and
a third step of purging a second vessel for supplying a 3- to 3.5-valent vanadium solution accommodating a 3- to 3.5-valent vanadium solution with a mixed gas of the inert gas and the gas product of the catalytic reaction captured with gas bubbles by the inert gas in the second step, which escaped to the exterior of the catalytic reactor in a gas state, to prevent oxidation of the 3- to 3.5-valent vanadium solution, followed by discharging the mixed gas to the exterior of the second vessel.

2. The method of claim 1 , wherein the 4-valent vanadium solution is supplied to the catalytic reactor of the second step from the first vessel for supplying a 4-valent vanadium solution, in which the oxidation is prevented by an inert purge gas in the first step, and
the 3- to 3.5-valent vanadium solution produced in the catalytic reactor of the second step is supplied to the second vessel for supplying a 3- to 3.5-valent vanadium solution of the third step.

3. The method of claim 1 , wherein, in the second step, the inert gas supplied to the catalytic reactor captures the gas product of the catalytic reaction, thereby gradually increasing the size of the gas bubbles, while reducing the surface area and density of the gas bubbles.

4. The method of claim 1 , wherein the gas product of the catalytic reaction, which is captured with gas bubbles by the inert gas, and the 3- to 3.5-valent vanadium solution produced in the catalytic reaction in the second step are supplied to the second vessel for supplying a 3- to 3.5-valent vanadium solution from the catalytic reactor and subjected to gas-liquid separation, and the second vessel for supplying a 3- to 3.5-valent vanadium solution is purged with the mixed gas of the inert gas and the gas product of the catalytic reaction to prevent oxidation of the 3- to 3.5-valent vanadium solution, followed by discharging the mixed gas to the exterior of the second vessel.

5. The method of claim 1 , wherein the gas product of the catalytic reaction is captured with the inert gas by mixing of gases in the step 2 to allow the gas product to escape to the exterior in a gas state, and thus the gas product is moved upwards in the catalytic reactor and discharged to the exterior of the catalytic reactor at a higher rate than the 3- to 3.5-valent vanadium solution in a liquid state, which is the product of the catalytic reaction.

6. The method of claim 1 , wherein the catalytic reaction of the second step is represented by Reaction Scheme 1 below, Reaction Scheme 2 below, or both:

7. The method of claim 1 , wherein the inert purge gas in the first step is nitrogen, and the gas product of the catalytic reaction in the second step is carbon dioxide.

8. The method of claim 1 , wherein the second vessel for supplying a 3- to 3.5-valent vanadium solution is an air-tight vessel,
wherein the 3- to 3.5-valent vanadium solution produced in the catalytic reactor, and the mixed gas of the inert gas and the gas product of the catalytic reaction, which escaped to the exterior of the catalytic reactor, are supplied to the second vessel for supplying a 3- to 3.5-valent vanadium solution, and
the second vessel for supplying a 3- to 3.5-valent vanadium solution is purged with the mixed gas, thereby producing a purged 3- to 3.5-valent vanadium solution in the second vessel, while containing the mixed gas and the 3- to 3.5-valent vanadium solution in the air-tight vessel in a state of being subjected to gas-liquid separation.

9. The method of claim 1 , wherein the first step to the third step are carried out in a continuous process in terms of gas flow.

Assignees

• Korea Inst Energy Res

Inventors

• Ryi Shin-Kun
• Jeon Myung-Seok
• Han Jae Yun
• Kim Chang-Hyun

Classifications

• H01M8/188 Primary

  by recharging of redox couples containing fluids; Redox flow type batteries · CPC title

• H01M8/04179

  by purging or increasing flow or pressure of reactants · CPC title

• H01M8/04186 Primary

  of liquid-charged or electrolyte-charged reactants · CPC title

• Y02E60/50

  Fuel cells · CPC title

• H01M8/04164

  by condensers, gas-liquid separators or filters · CPC title