Determining the state of charge of an all-vanadium redox flow battery using uv/vis measurement

Patent metadata

Field	Value
Publication number	US-2019267648-A1
Application number	US-201716333292-A
Country	US
Kind code	A1
Filing date	Sep 8, 2017
Priority date	Sep 19, 2016
Publication date	Aug 29, 2019
Grant date	—

Abstract

A method for determining a charge state of a vanadium redox flow cell may comprise indirectly determining concentrations of V 4+ and V 5+ in a positive electrolyte by mixing positive and negative electrolytes with one another in particular proportions to reduce V 5+ present in the positive electrolyte. In this way, CT complexes of V 4+ /V 5+ may be avoided, the concentration of which is not determinable directly owing to the strong UV/vis absorption. Furthermore, the method enables determination of the concentrations of the negative electrolyte and positive electrolyte via UV/vis absorptions, which enables simple monitoring of the charge state of a vanadium redox flow battery.

First claim

1 .- 15 . (canceled)

16 . A method of determining a charge state of a redox flow cell having a negative half-cell and a positive half-cell, the method comprising steps of:
(i) determining the charge state of a negative electrolyte by determining concentrations of oxidized and reduced form of redox metal via absorption at a defined wavelength; (ii) mixing a defined volume of the negative electrolyte and a positive electrolyte; (iii) determining the concentrations of the oxidized and reduced form of the redox metal from the negative electrolyte or oxidized form of the redox metal from the negative electrolyte and reduced form of the redox metal from the positive electrolyte; and (iv) determining the charge state of the positive electrolyte by calculating original concentrations of the oxidized and reduced form of the redox metal from the positive electrolyte from the concentrations determined in steps (i) and (iii).

17 . The method of claim 16 wherein
step (i) comprises determining the charge state of the negative electrolyte by determining concentrations of V 2+ and V 3+ via absorption at a defined wavelength;
step (ii) comprises mixing the defined volume of the negative electrolyte and the positive electrolyte;
step (iii) comprises determining the concentrations of V 2+ and V 3+ or V 3+ and V 4+ via absorption at a defined wavelength in a mixture of the negative electrolyte and the positive electrolyte; and
step (iv) comprises determining the charge state of the positive electrolyte by calculating the original concentrations of V 4+ and V 5+ from the concentrations determined in steps (i) and (iii).

18 . The method of claim 17 wherein the concentrations of V 2+ are measured at a wavelength in a range from 800 to 900 nm.

19 . The method of claim 17 wherein the concentrations of V 3+ are measured at a wavelength in a range from 370 to 450 nm.

20 . The method of claim 17 wherein the concentrations of V 4+ are measured at a wavelength in a range from 700 to 850 nm.

21 . The method of claim 17 wherein the concentrations of V 2+ and V 3+ ions or V 3+ and V 4+ ions are determined by correcting an absorption ascertained by an absorption component of a respective other ion.

22 . The method of claim 17 wherein the charge state of the negative electrolyte is determined upstream of a feed to an electrolysis cell and in a region of an outlet from the electrolysis cell, wherein steps (ii) to (iv) are performed with the positive electrolyte and the negative electrolyte, each of which is branched off from the electrolysis cell upstream of the feed to the electrolysis cell and in the region of the outlet from the electrolysis cell.

23 . The method of claim 17 wherein a mixture of the negative electrolyte and the positive electrolyte generated in step (ii) is fed in equal proportions to the negative half-cell and the positive half-cell.

24 . The method of claim 17 wherein a mixture of the negative electrolyte and the positive electrolyte generated in step (ii) is fed in different proportions to the negative half-cell and the positive half-cell.

25 . The method of claim 17 comprising rebalancing a redox flow battery with a mixture of the negative electrolyte and the positive electrolyte generated in step (ii).

26 . The method of claim 16 configured to be calibration-free.

27 . The method of claim 16 wherein step (ii) comprises mixing the negative electrolyte with the positive electrolyte in a ratio ranging from 4:1 to 1:4.

28 . A vanadium redox flow battery comprising:
a positive half-cell; a negative half-cell; a membrane disposed between the positive half-cell and the negative half-cell; circuits for positive electrolytes and negative electrolytes, with each circuit comprising:
a reservoir for the respective electrolytes,
a feed for feeding the respective electrolytes into one of the half-cells,
an outlet for egress of the respective electrolytes from one of the half-cells into the reservoir, and
a pump for feeding the respective electrolytes into one of the half-cells;
a device for determining a UV/vis spectrum of the negative electrolytes, wherein the device is disposed in a region of the feed for feeding the negative electrolytes into the negative half-cell; outlets for the electrolytes disposed in a region of the feeds, wherein the outlets disposed in the region of the feeds are connected flush to one another and to a feed to a device for determining a UV/vis spectrum of a mixture of the negative electrolytes and the positive electrolytes; and a closed-loop control circuit for determining concentrations of V 2+ , V 3+ , and V 4+ from UV/vis spectra and calculating concentrations of V 4+ and V 5+ in the positive electrolytes from the concentrations of V 2+ and V 3+ in the negative electrolytes and the concentrations of V 2+ , V 3+ , and V 4+ in the mixture of the negative and positive electrolytes.

29 . The vanadium redox flow battery of claim 28 wherein the positive half-cell is an electrolysis cell, wherein a positive electrode is a corrosion-resistant electrode.

30 . The vanadium redox flow battery of claim 28 comprising feeds by which the mixture is recyclable into the circuits for the positive and negative electrolytes.

Assignees

• Thyssenkrupp Ind Solutions Ag
• Thyssenkrupp Ag

Inventors

• Helmle Stefan
• Bredemeyer Niels
• Polcyn Gregor Damian
• Tenhumberg Nils

Classifications

• H01M8/04186

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

• H01M8/04477 Primary

  of the electrolyte · CPC title

• H01M8/188 Primary

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

• H01M8/04201

  Reactant storage and supply, e.g. means for feeding, pipes · CPC title

• G01N2021/3129

  Determining multicomponents by multiwavelength light · CPC title