Iron Salt Battery Electrolyte Preparation With pH-Controlled Fe3+ Reduction

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Existing methods for preparing FeCl2 solutions for iron salt batteries face safety hazards, high costs, and purity issues, particularly due to the use of concentrated HCl and high-purity FeCl2 salts or byproducts.

Innovation Solution

A method involving the reaction of iron(III) chloride with elemental iron in a dilute hydrochloric acid solution, controlled by pH monitoring, followed by conversion in an electrochemical cell to produce a FeCl2 electrolyte with controlled Fe3+ concentration, using safer and lower-cost materials.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If concentrated HCl is used to prepare FeCl2 solution, then the FeCl2 solution can be prepared effectively, but safety hazards increase

Engineering Contradiction:
ImproveFeCl2 solution preparationVSAvoidsafety hazards
Core Design Contradiction:
Ease of manufactureVSObject-affected harmful factors

Solution Approach 1:

The patent changes the concentration parameter of HCl from concentrated to dilute (pH less than 1), which maintains the chemical reaction effectiveness while significantly reducing the safety hazards associated with concentrated acid handling and storage

Inventive Principle:
Principle #35Parameter changes

2Manufacturing precision

If high purity FeCl2 salts are purchased and dissolved, then the electrolyte purity is improved, but the cost increases

Engineering Contradiction:
Improveelectrolyte purityVSAvoidcost
Core Design Contradiction:
Manufacturing precisionVSEase of manufacture

Solution Approach 1:

The patent uses inexpensive iron filings as a sacrificial reagent that reacts with FeCl3 to produce FeCl2. The iron filings are consumed in the reaction and do not need to be recovered, providing a cost-effective source of FeCl2 compared to purchasing high-purity salts

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

Solution Approach 2:

The patent replaces the chemical purification process with an electrochemical reduction process. By applying a small cathodic current, Fe3+ ions are reduced to Fe2+ directly in the electrolyte, achieving high purity without expensive chemical reagents or multiple purification steps

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

3Ease of manufacture

If FeCl2 is obtained as a byproduct of the chlorine process, then the cost is reduced, but purity issues arise

Engineering Contradiction:
ImprovecostVSAvoidpurity
Core Design Contradiction:
Ease of manufactureVSManufacturing precision

Solution Approach 1:

The patent uses electrochemical reduction at the cathode to convert Fe3+ to Fe2+ with high selectivity and efficiency. This electrochemical method provides precise control over the reduction process, achieving high purity FeCl2 electrolyte without the contamination issues associated with byproduct recovery from chlorine processes

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

4Productivity

If FeCl2 solution is prepared by oxidation of metallic iron in concentrated HCl, then the FeCl2 can be produced, but safety hazards and cost issues arise

Engineering Contradiction:
ImproveFeCl2 productionVSAvoidsafety hazards
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The patent changes the HCl concentration from concentrated to dilute (pH less than 1), which is sufficient to dissolve the iron and maintain Fe2+ in solution while dramatically reducing the safety hazards of handling concentrated acid

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

Instead of oxidizing iron to produce FeCl2 directly in concentrated acid, the patent first prepares a dilute FeCl3 solution and then reduces it electrochemically to FeCl2. This inverted approach avoids the need for concentrated acid and high-temperature oxidation, improving safety while maintaining productivity

Inventive Principle:
Principle #13The other way round (Inversion)

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

The method achieves a safer, cost-effective, and environmentally friendly production of high-purity FeCl2 electrolyte by reducing hazardous material use and optimizing processing conditions.

Implementation Method 1

supplying elemental iron, Fe, into the reactor, wherein the elemental iron reacts with iron(III) to iron(II)

Methodology Applied
Scientific EffectRedox reaction: Redox Reactions

Implementation Method 2

A flow rate of the reactor solution through the anode is controlled to obtain a final Fe 3+ concentration of less than 5% of the total iron concentration

Methodology Applied
Scientific EffectElectrochemical reduction: Electrolysis

Data Source

PatentEP4683016A1Method for preparation of iron salt battery electrolyte
Publication Date: 2026.01.21 VOLTSTORAGE GMBH
  • EP4683016A1 patent drawingFigure 1
  • EP4683016A1 patent drawingFigure 2
  • EP4683016A1 patent drawingFigure 3

AI summary

The invention provides a method for preparation of an iron salt battery electrolyte. The method comprises the following steps: supplying iron(III) chloride, FeCl3, into an agitated reactor containing a dilute solution of hydrochloric acid, HCl, having a pH value less than 1; supplying elemental iron, Fe, into the reactor, wherein the elemental iron reacts with iron(III) to iron(II); monitoring the pH value of reactor solution; using the monitored pH value to control supplying additional hydrochloric acid, HCl, into the reactor in order to maintain a pH of the reactor solution less than 1; and converting excess Fe3+ to Fe2+ in an electrochemical cell having a membrane or a separator between an anode and a cathode thereof by directing the reactor solution from the reactor through the anode of the electrochemical cell. A flow rate of the reactor solution through the anode is controlled to obtain a final Fe3+ concentration in the anode outlet FeCl2 stream of 15% or less than 15% of a total dissolved iron concentration as the iron salt battery electrolyte.