Flow Battery Research Collective
Flow Battery Research Collective
October 9, 2025
Open-source hardware1: no patents, no licensing fees, free for commercial use (CERN OHL), modifications allowed, changes must be made public
Cooperative, not competitive: trying to establish global community of contributors (eventually, users)
Development published online in Git repository
Lower barriers to entry = more iterations, with more brainpower, for lower cost
Open-source provides valuable economic benefits: for €1 billion invested, €65 to 95 billion benefit to EU GDP1
In EU/UK academia:
French LAAS-CNRS lab creates open-source power electronics, commercializes them with company OwnTech (https://www.owntech.io/)
From the UK: OpenFlexure community, open-source, lab-grade microscopes
(https://openflexure.org)
Globally:
Recyclable photovoltaic panels: https://www.biosphere.solar/
Locally buildable small wind turbines: https://windempowerment.org/research-and-devlopment/small-wind-systems/the-piggott-turbine/, https://www.openafpm.net/
Potentiostat/galvanostat1
Specified entire system: pumps, tubing, reservoirs, documentation etc. Low-cost, widely available, safe components/materials for ease of replication.

Flow frame design inspired by O’Conner, Bailey et al.1
Our initial chemistry is zinc-iodine (architecture inspired by Xie et al.1 and electrolyte by Lee et al. 2), but we are exploring more varieties, such as: all-iron, zinc-iron, soluble iron-manganese (with chelates)
Negative Terminal (Anode): \(\ce{Zn_{(s)} -> Zn^2+ + 2e-}\)
Positive Terminal (Cathode): \(\ce{I3- + 2e- -> 3I- }\)
Overall: \(\ce{Zn_{(s)} + I3- -> Zn^2+ + 3I-}, E^\ominus = 1.3 V\)
Parasitic reaction: \(\ce{6I- + O2 + 2 H2O -> 2I3- + 4OH- }\)
Triethylene glycol is added to form soluble iodide complexes at higher SOCs
Easy to source, low-cost reagents (vs. vanadium, chromium…)
Compatible with cheap microporous membranes, such as paper
Resistant to dendrites
No appreciable hydrogen evolution
Acceptable energy density (>20Wh/L)
No strong acids or bases needed
Lower toxicity (vs. vanadium, chromium…)
2M KI, 1M ZnCl₂, 2M NH₄Cl with 5% triethylene glycol at 60mA/cm², Daramic AA-900, flow-through 3.2 mm graphite felt
Based on Liu et al1, all-iron hybrid RFB approach using highly concentrated divalent chloride salts, e.g. 4.5 M MgCl₂ or CaCl₂ alongside FeCl₂.
Negative Terminal (Anode): \(\ce{Fe_{(s)} -> Fe^2+ + 2e-}\)
Positive Terminal (Cathode): \(\ce{Fe^3+ + e- -> Fe^2+}\)
Hydrogen evolution greatly reduced.
Initial testing in progress, including approx. viscosity measurements: https://fbrc.nodebb.com/topic/44/only-fe-system/21
Design in FreeCAD, model in OpenFOAM
Design in FreeCAD, model in OpenFOAM
Development kit is now stable and certified
All-iron electrolyte exploration with development kit (water-in-salt)
Completed leak-testing validation of 175 cm² cell
Finishing control bench for testing 175 cm² cell
Initial testing of 175 cm² cell with Zn/I chemistry

Build a kit using our online documentation and designs, give feedback on instructions
Benchmark and standardize more electrolyte chemistries with the development kit (ideally compatible with porous separators!)
Help with CAD and FEM/CFD for our upcoming large-format flow frames
Help design a battery monitoring system (BMS) including pump motor control for larger flow batteries
Join with us on funding applications :)

redoxflow Groupe de Recherche - Réunion d’Automne 2025, Marseille