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VRFB electrolyte technology: 40 years of patents

Vanadium Redox Flow Battery Electrolyte Technology — PatSnap Insights
Energy Storage

Vanadium redox flow battery electrolyte technology is the chemical heart of grid-scale energy storage — and after four decades of incremental refinement, molecular solvation engineering and chloride-phosphate co-stabilization are converging to redefine what is commercially achievable. This landscape maps the innovation signals from 1987 to 2026 across patents, national laboratories, and academic institutions worldwide.

PatSnap Insights Team Innovation Intelligence Analysts 13 min read
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Reviewed by the PatSnap Insights editorial team ·

The Commercial Baseline and Its Concentration Ceiling

The canonical VRFB electrolyte — 1.6–2.0 M vanadium dissolved in 4–5 M sulfuric acid — has been the commercial standard since foundational work at the University of New South Wales in the late 1980s, first formalised in the Pinnacle VRB / Unisearch Limited all-vanadium cell patent filed in Australia in 1987. That baseline has remained essentially unchanged for nearly four decades, which makes the current wave of concentration-enhancement research all the more significant.

1.6–2.0 M
Commercial vanadium concentration baseline
3.6 M
Highest demonstrated vanadium concentration (CENELEST/UNSW)
180%
Operational temperature window expansion (PNNL, 2021)
>30%
Energy density increase via bi-additive solvation (PNNL, 2021)

The fundamental constraint on the baseline formulation is thermal precipitation of V(V) — the fully oxidised vanadium species on the positive side — at elevated temperatures. Above roughly 40°C, V(V) begins to precipitate from sulfuric acid solution, setting a practical ceiling on both concentration and operating temperature range. Addressing this constraint has been the single most active area of VRFB electrolyte research in the dataset reviewed for this report.

The first systematic breakthrough came from UNSW Australia in 2015, when researchers demonstrated that adding phosphoric acid (H₃PO₄) at just 1 wt% extended the V(V) precipitation induction time from 3 days to more than 47 days at 30°C. Polyphosphates were also evaluated as alternatives. This enabled a 3 M vanadium electrolyte — a 50–87% concentration increase over the commercial baseline — with corresponding gains in volumetric energy density. CENELEST/UNSW subsequently pushed concentrations to 3.6 M by combining precipitation inhibitors with an oxygen reduction approach that replaces the positive electrolyte half-reaction entirely.

Adding phosphoric acid (H₃PO₄) at 1 wt% to a VRFB sulfuric acid electrolyte extends V(V) precipitation induction time from 3 days to more than 47 days at 30°C, enabling stable 3 M vanadium concentrations — a finding demonstrated by UNSW Australia in 2015.

The alternative supporting electrolyte approach takes a different route: replacing or supplementing sulfuric acid with hydrochloric acid, phosphoric acid, or mixed chloride-phosphate systems to modify vanadium solvation and raise solubility ceilings. Fraunhofer Institute for Chemical Technology’s 2019 comparative study directly evaluated 1.6 M vanadium in sulfuric acid (4.7 M SO₄²⁻) against hydrochloric acid (6.1–7.6 M Cl⁻), finding comparable energy efficiencies but distinct thermal and electrochemical profiles. Two more recent patent filings — Battelle Memorial Institute’s active EP patent (2025) claiming chloride ions from MgCl₂ plus phosphate ions from (NH₄)₂HPO₄, and Fraunhofer-Gesellschaft’s active DE patent (2024) targeting operation above 40°C without chloride — both converge on phosphate co-ions as the mechanism for extending thermal stability. This consensus across independent institutions in different jurisdictions is a strong signal of an approaching commercial standard, as noted by researchers publishing through Nature and aligned energy storage journals.

Figure 1 — Vanadium Electrolyte Concentration Progress: Baseline vs. Demonstrated Maximum
VRFB Vanadium Electrolyte Concentration Milestones: Commercial Baseline to 3.6 M Demonstrated Maximum 0 1.5 M 3.0 M 4.0 M Vanadium Concentration (M) 1.6 M Baseline Low (UNSW 1987) 2.0 M Baseline High (commercial) 3.0 M H₃PO₄ additive (UNSW, 2015) 3.6 M O₂ reduction (CENELEST, 2019) Commercial baseline Phosphate-enhanced O₂-reduction system
Phosphoric acid additives (UNSW, 2015) and oxygen-reduction approaches (CENELEST, 2019) have pushed achievable vanadium concentrations from the 1.6–2.0 M commercial baseline to 3.0–3.6 M, with direct implications for volumetric energy density.

Dalian Rongke Power — China’s largest VRFB manufacturer — holds an active EP patent (2019) claiming a positive-to-negative electrolyte volume ratio of 1:1.5–1:1.2 with 0.01–0.5 mol/L additives including sulfate, phosphate, pyrophosphate, and polyphosphate, specifically to enable high-energy-density operation while reducing hydrogen evolution capacity loss. This filing signals that Chinese OEM IP strategy is now extending into Western patent jurisdictions, a development that European system integrators and project developers should monitor closely.

Additive Science and Molecular Solvation Engineering

The most consequential recent advance in VRFB electrolyte science is the shift from empirical additive screening to rational molecular solvation engineering — a paradigm change demonstrated most clearly by Pacific Northwest National Laboratory’s 2021 publication on bi-additive solvation chemistry.

The PNNL approach uses competing cation additives (NH₄⁺, Mg²⁺) and bonding anion additives (SO₄²⁻, PO₄³⁻, Cl⁻) at concentrations at or below 0.1 M to restructure the vanadium aqua-solvate coordination shells — the molecular-scale arrangement of water and counter-ions around each vanadium ion. By tuning these coordination shells, the research team demonstrated an expansion of the operational temperature window by 180% and an increase in energy density by more than 30%. The significance of this result is that it was achieved not by changing the base electrolyte chemistry but by adding small amounts of carefully selected co-ions.

“Competing cation and bonding anion bi-additives at concentrations at or below 0.1 M can expand the VRFB operational temperature window by 180% and increase energy density by more than 30% — without changing the base sulfuric acid electrolyte chemistry.”

The Chinese Academy of Sciences’ Institute of Process Engineering (2022) evaluated five phosphonate additives — HEDP, HDTMPA, ATMPA, EDTMPS, and DTPMP — each at 0.5 wt% in the positive electrolyte. Most improved V(V) thermal stability, with HEDP and HDTMPA showing the best performance. This systematic screening approach complements PNNL’s solvation-first design methodology and provides a practical shortlist for formulation development.

Key finding: carbohydrate additives for crossover suppression

Wuhan University of Science and Technology (2022) demonstrated that α-lactose monohydrate at 1 wt% in the negative electrolyte achieves 71% capacity retention after 30 cycles, compared to 29.5% for the control — a 2.4× improvement — with significant vanadium crossover inhibition. This result positions carbohydrate-based additives as a low-cost, accessible route to capacity management.

α-Lactose monohydrate at 1 wt% in the negative VRFB electrolyte achieves 71% capacity retention after 30 cycles versus 29.5% for a control electrolyte without the additive, according to research from Wuhan University of Science and Technology published in 2022.

Fraunhofer-Gesellschaft’s 2024 DE patent takes a distinct approach: a chloride-free electrolyte comprising vanadium ions, sulfate ions, and phosphoric acid, with conductivity specified in the range of 280–420 mS·cm⁻¹, specifically targeting operation above 40°C. The chloride-free formulation addresses corrosion concerns in some system architectures while still achieving the thermal stability gains that phosphate co-ions provide. This work, alongside the broader body of phosphonate additive research documented by institutions including those affiliated with Fraunhofer, reflects the maturation of additive science from academic curiosity to patentable commercial formulation.

Explore the full VRFB electrolyte patent landscape, including additive formulation claims and assignee mapping, in PatSnap Eureka.

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Figure 2 — Phosphonate Additive Performance: V(V) Thermal Stability Ranking
Phosphonate Additive Performance Ranking for V(V) Thermal Stability in VRFB Positive Electrolyte 0 Low Medium High (Best) Relative V(V) Thermal Stability Improvement (qualitative ranking at 0.5 wt%) HEDP Best HDTMPA Best ATMPA Moderate EDTMPS Low DTPMP Low
Among five phosphonate additives evaluated at 0.5 wt% by the Chinese Academy of Sciences (2022), HEDP and HDTMPA showed the best V(V) thermal stability improvement; ATMPA was moderate; EDTMPS and DTPMP showed lower performance.

Electrolyte capacity management — distinct from composition — is also emerging as a performance differentiator. Research from DLR Oldenburg (2020), Clausthal University of Technology (2021), the University of Alberta (2022), and Chosun University (2023) all addressed electrolyte imbalance detection, modelling, and rebalancing methodologies. As commercial VRFB deployments scale up, the ability to detect and correct electrolyte state-of-charge imbalances in real time will increasingly separate competitive systems from commodity ones.

Hybrid Redox Couples and Non-Aqueous Electrolytes

A distinct and strategically important innovation stream explores augmenting or replacing the standard vanadium redox chemistry with secondary redox couples or non-aqueous media — approaches that address fundamental thermodynamic and solubility constraints that additives alone cannot overcome.

Hydraredox Technologies has built the most extensive IP position in hybrid electrolyte chemistry. Its core concept — adding Ce³⁺/Ce⁴⁺ to the V⁴⁺/V⁵⁺ positive electrolyte at concentrations sufficient to buffer anode polarization approaching 1.5 V — prevents oxygen evolution on carbon electrodes, a failure mode that limits cycle life and efficiency at high states of charge. The company’s EP patent (2020) extends this approach by incorporating methane-sulfonic acid as a supporting electrolyte component. The breadth of Hydraredox’s filing strategy — WO (2014), AU (2015, 2018), EP (2016, 2020), IN (2016), and US (2018) — means that any developer exploring ancillary redox couples in the positive electrolyte must conduct thorough freedom-to-operate analysis against this family.

What is a deep eutectic solvent (DES) electrolyte?

A deep eutectic solvent is a mixture of two or more components — typically a hydrogen bond donor and a hydrogen bond acceptor — that forms a liquid at temperatures well below the melting points of the individual components. In VRFB applications, DES electrolytes offer a wider electrochemical stability window than water, potentially enabling higher cell voltages without the risk of water electrolysis that constrains aqueous systems.

The non-aqueous route is still pre-commercial but is attracting meaningful research investment. Addionics Ltd. and the Imperial White City Incubator demonstrated in 2020 that DES-based VRFB electrolytes yield 50% higher efficiency and capacity utilization compared to ionic liquid alternatives, with nitrogen-doped graphene electrodes adding a further 10% improvement. Numerical modelling of non-aqueous systems has also been published by Shenzhen University (2022) and Nanchang Institute of Science and Technology (2023), indicating that the theoretical framework for non-aqueous VRFB design is maturing. The fundamental appeal of these systems is their ability to address the cell voltage ceiling imposed by water electrolysis in aqueous VRFBs — a ceiling that limits the energy density achievable regardless of vanadium concentration, as documented by research bodies including the U.S. Energy Information Administration in its grid storage technology assessments.

Deep eutectic solvent (DES) electrolytes in vanadium redox flow batteries demonstrated 50% higher efficiency and capacity utilization compared to ionic liquid electrolytes in a 2020 study by Addionics Ltd. and the Imperial White City Incubator; nitrogen-doped graphene electrodes provided an additional 10% improvement.

The EPFL Lausanne group has explored a related but distinct application: a vanadium-manganese redox dual-flow battery architecture in which pre-charged electrolytes discharge through catalytic hydrogen evolution and oxygen evolution reactors, enabling simultaneous electricity storage and green hydrogen production. This dual-use application represents an emerging vertical for VRFB electrolyte chemistry beyond the conventional stationary storage use case, and aligns with broader hydrogen economy initiatives tracked by organisations such as the International Energy Agency.

Figure 3 — VRFB Electrolyte Innovation Timeline: Key Milestones by Era
VRFB Electrolyte Innovation Timeline: Key Milestones from 1987 Foundational Era to 2026 Emerging Adjacencies 1987 –2004 Foundational UNSW / Pinnacle VRB core cell concept 2010 –2019 Development 3 M electrolyte; Ce³⁺/Ce⁴⁺ hybrid; Rongke EP patent 2020 –2023 Acceleration PNNL solvation (+180% temp window); DES VRFB 2024 –2026 Convergence Battelle EP; Fraunhofer DE; Pure Lithium AU (2026) Foundational era Development cluster Recent acceleration Active frontier
The VRFB electrolyte innovation timeline spans four decades, from the foundational UNSW/Pinnacle VRB cell concept (1987) through the development cluster (2010–2019) and recent acceleration (2020–2023) to the current convergence phase (2024–2026) characterised by active Battelle, Fraunhofer, and Pure Lithium filings.

Patent Landscape: Assignees, Jurisdictions, and Freedom-to-Operate Risks

The VRFB electrolyte patent landscape is characterised by a small number of highly active assignees pursuing multi-jurisdictional strategies, a large body of now-expired foundational prior art in the public domain, and several active patent families that present material freedom-to-operate risks for new market entrants.

Jurisdiction distribution across the patents reviewed shows AU (5 records) and EP (5 records) as the dominant active filing destinations, followed by US (2 records), DE (1 record), WO (1 record), and IN (1 record). The EP and AU concentration reflects both Hydraredox Technologies’ systematic multi-jurisdictional filing strategy and the European activity of Battelle Memorial Institute and Fraunhofer-Gesellschaft.

The most prolific active assignee is Hydraredox Technologies Holdings Ltd. / Hydraredox Technologies Inc., with filings across WO (2014), AU (2015, 2018), EP (2016, 2020), IN (2016), and US (2018) — all covering variants of the Ce³⁺/Ce⁴⁺ ancillary redox couple concept. This represents a focused IP consolidation strategy around a single core innovation across six jurisdictions. For any developer exploring hybrid positive electrolytes or overcharge protection mechanisms, a thorough freedom-to-operate analysis against this family is non-negotiable.

Hydraredox Technologies holds active VRFB electrolyte patents in six jurisdictions — WO (2014), AU (2015, 2018), EP (2016, 2020), IN (2016), and US (2018) — all covering the concept of Ce³⁺/Ce⁴⁺ ancillary redox couples in the positive electrolyte to buffer anode polarization and prevent oxygen evolution.

By contrast, the foundational Pinnacle VRB / Unisearch Limited patents — including the 1987 AU core cell patent and the 2001 US high-energy-density electrolyte patent — are now inactive, meaning the core prior art is in the public domain. This is strategically important: it means that the baseline VRFB electrolyte formulation (vanadium in sulfuric acid) is freely available for commercial use, but that improvements and specific formulations remain subject to active claims held by Battelle, Fraunhofer, Rongke, Sumitomo, and Hydraredox.

Sumitomo Electric Industries holds an active AU patent on impurity-controlled electrolytes specifying arsenic and antimony content at or below 15 ppm for precipitate reduction — reflecting Japanese manufacturing precision in electrolyte specification and a distinct IP angle on electrolyte quality rather than composition. Dalian Rongke Power’s active EP patent on operating ratios and additive types signals that Chinese OEM IP expansion into Western markets is already underway, a trend that patent professionals and project developers in Europe should track through tools such as the European Patent Office‘s Espacenet database.

Run a freedom-to-operate analysis on VRFB electrolyte patent families — including Hydraredox, Battelle, and Rongke claims — using PatSnap Eureka’s AI-powered patent intelligence.

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Emerging Directions and Strategic Implications for 2026 and Beyond

Five forward-looking directions emerge from the most recent filings and publications (2021–2026) in this dataset, each carrying distinct strategic implications for R&D teams, IP professionals, and system integrators.

1. Molecular solvation engineering as the next design paradigm

PNNL’s 2021 bi-additive approach — using competing cations and bonding anions at or below 0.1 M to restructure vanadium aqua-solvate coordination shells — represents a fundamentally more rational approach than empirical additive screening. The 180% operational temperature window expansion and more than 30% energy density increase reported suggest this approach will define the next generation of electrolyte formulation. R&D teams not investing in molecular-level characterisation of vanadium solvation structures risk falling behind this design frontier.

2. Chloride-phosphate co-stabilisation approaching commercial standard

The convergence of Battelle Memorial Institute’s EP patent (2025) and Fraunhofer-Gesellschaft’s DE patent (2024) on phosphate co-ions as a mechanism for extending thermal stability above 40°C — from independent institutions in different jurisdictions — signals an approaching commercial standard. Whoever secures broad claims in this sub-space will have significant freedom-to-operate leverage over the next generation of high-energy-density VRFBs.

3. Non-aqueous and DES electrolytes: disruptive risk on a 5–10 year horizon

Non-aqueous and deep eutectic solvent electrolytes remain pre-commercial, but the combination of Addionics Ltd.’s 2020 experimental results (50% higher efficiency vs. ionic liquid comparison) and growing numerical modelling activity from Chinese universities suggests momentum is building. These systems address the fundamental cell voltage ceiling imposed by water electrolysis in aqueous VRFBs. R&D teams not monitoring this sub-space risk being caught off-guard by a technology transition within a 5–10 year horizon, a concern echoed in long-duration energy storage roadmaps published by bodies such as WIPO in its green technology patent landscape reports.

4. Catalytic electrolyte preparation: an underexploited IP opportunity

KAIST’s 2019 demonstration of catalytic V³·⁵⁺ production using formic acid reduction over Pt/C in a continuous flow reactor, and Clausthal University of Technology’s 2020 work on V₂O₅ dissolution achieving full dissolution in approximately 10 minutes, are primarily in the literature rather than in patent filings in this dataset. This suggests that scalable, low-cost electrolyte preparation processes may represent an open IP filing space for developers focused on reducing the electrolyte cost component — currently a large fraction of total VRFB system cost.

5. Electrolyte management as a performance differentiator

The cluster of electrolyte imbalance detection, modelling, and rebalancing publications from DLR Oldenburg (2020), Clausthal University of Technology (2021), University of Alberta (2022), and Chosun University (2023) indicates that electrolyte management — not just composition — is becoming a primary performance differentiator in commercial VRFB systems. As deployments scale to multi-megawatt installations, real-time capacity recovery and state-of-charge monitoring will be as commercially important as the electrolyte formulation itself.

“Electrolyte preparation cost reduction is an underexploited IP opportunity: KAIST’s catalytic V³·⁵⁺ production route and Clausthal’s V₂O₅ dissolution work are primarily in the literature rather than in patent filings — suggesting an open filing space for IP-conscious developers.”

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References

  1. All Vanadium Redox Battery — Pinnacle VRB Limited (Unisearch Limited), AU, 1987
  2. High Energy Density Vanadium Electrolyte Solutions — Pinnacle VRB Limited, US, 2001
  3. High Energy Density Vanadium Electrolyte Solutions — Pinnacle VRB, ES, 2004
  4. All-Vanadium Redox Flow Battery System with Ce³⁺/Ce⁴⁺ Ancillary Couple — Hydraredox Technologies Inc., WO, 2014
  5. All-Vanadium Redox Flow Battery System with Ce³⁺/Ce⁴⁺ Ancillary Couple — Hydraredox Technologies Holdings Ltd., AU, 2015
  6. All-Vanadium Redox Flow Battery System with Ce³⁺/Ce⁴⁺ Ancillary Couple — Hydraredox Technologies Holdings Ltd., EP, 2016
  7. All-Vanadium Redox Flow Battery System with Ce³⁺/Ce⁴⁺ Ancillary Couple — Hydraredox Technologies Holdings Ltd., IN, 2016
  8. All-Vanadium Redox Flow Battery System with Ce³⁺/Ce⁴⁺ Ancillary Couple — Hydraredox Technologies Holdings Ltd., AU, 2018
  9. All-Vanadium Redox Flow Battery System with Ce³⁺/Ce⁴⁺ Ancillary Couple — Hydraredox Technologies Ltd., US, 2018
  10. All-Vanadium Redox Flow Battery System with Ce³⁺/Ce⁴⁺ Couple and Methane-Sulfonic Acid — Hydraredox Technologies Holdings Ltd., EP, 2020
  11. All-Vanadium Redox Flow Battery and Operation Method Thereof — Dalian Rongke Power Co., Ltd., EP, 2019
  12. All-Vanadium Sulfate Acid Redox Flow Battery System — Battelle Memorial Institute, EP, 2025
  13. Chloride-Free Electrolyte Composition for Extended Operation at High Temperatures — Fraunhofer-Gesellschaft, DE, 2024
  14. Electrolyte for Redox Flow Battery and Redox Flow Battery System — Sumitomo Electric Industries, Ltd., AU, 2020
  15. Mitigating Capacity Loss in Batteries with Vanadium Based Positive Electrodes — Pure Lithium Corporation, AU, 2026
  16. Vanadium Electrolyte for All-Vanadium Redox-Flow Batteries: The Effect of the Counter Ion — Fraunhofer Institute for Chemical Technology, 2019
  17. A High Energy Density Vanadium Redox Flow Battery with 3 M Vanadium Electrolyte — UNSW Australia, 2015
  18. Vanadium Oxygen Fuel Cell Utilising High Concentration Electrolyte — CENELEST / UNSW, 2019
  19. Accelerated Design of Vanadium Redox Flow Battery Electrolytes Through Tunable Solvation Chemistry — Pacific Northwest National Laboratory, 2021
  20. Preparation of Electrolyte for Vanadium Redox-Flow Batteries Based on Vanadium Pentoxide — Clausthal University of Technology, 2020
  21. Catalytic Production of Impurity-Free V3.5+ Electrolyte for Vanadium Redox Flow Batteries — KAIST, 2019
  22. Influence of Several Phosphate-Containing Additives on the Stability and Electrochemical Behavior of Positive Electrolytes — Chinese Academy of Sciences, Institute of Process Engineering, 2022
  23. Mitigating Capacity Decay by Adding Carbohydrate in the Negative Electrolyte — Wuhan University of Science and Technology, 2022
  24. Evaluation of a Non-Aqueous Vanadium Redox Flow Battery Using a Deep Eutectic Solvent and Graphene-Modified Carbon Electrodes — Addionics Ltd. / Imperial White City Incubator, 2020
  25. European Patent Office — Espacenet Patent Database
  26. WIPO — Green Technology Patent Landscape Reports
  27. International Energy Agency — Long-Duration Energy Storage Roadmaps

All data and statistics in this article are sourced from the references above and from PatSnap‘s proprietary innovation intelligence platform. This landscape is derived from a targeted set of patent and literature records and represents a snapshot of innovation signals within this dataset only; it should not be interpreted as a comprehensive view of the full industry.

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