Here you can find my research work, publications, and academic contributions.
Under review at ICLR 2026
Towards a Physics Foundation Model
Florian Wiesner, Prof. Matthias Wessling, Prof. Stephen Baek
With this work, I wanted to explore whether the concept of foundation models (LLMs for language) can be applied to physics simulations. The idea is to train a single model on a large corpus of diverse simulation data, such that it can generalize to new physical systems without retraining.
I also wrote a blog post explaining the work in more detail.
Foundation models have revolutionized natural language processing through a ``train once, deploy anywhere'' paradigm, where a single pre-trained model adapts to countless downstream tasks without retraining. Access to a Physics Foundation Model (PFM) would be transformative -- democratizing access to high-fidelity simulations, accelerating scientific discovery, and eliminating the need for specialized solver development. Yet current physics-aware machine learning approaches remain fundamentally limited to single, narrow domains and require retraining for each new system. We present the General Physics Transformer (GPhyT), trained on 1.8 TB of diverse simulation data, that demonstrates foundation model capabilities are achievable for physics. Our key insight is that transformers can learn to infer governing dynamics from context, enabling a single model to simulate fluid-solid interactions, shock waves, thermal convection, and multi-phase dynamics without being told the underlying equations. GPhyT achieves three critical breakthroughs: (1) superior performance across multiple physics domains, outperforming specialized architectures by up to 29x, (2) zero-shot generalization to entirely unseen physical systems through in-context learning, and (3) stable long-term predictions through 50-timestep rollouts. By establishing that a single model can learn generalizable physical principles from data alone, this work opens the path toward a universal PFM that could transform computational science and engineering.
Unveiling the Role of PTFE Surface Coverage on Controlling Gas Diffusion Layer Water Content
Florian Wiesner, James Woodford, Mayank Sabharwal, Matthias Hesselmann, Seongyeop Jung, Matthias Wessling, Marc Secanell
Accurate prediction of water content in fuel cells or electrolyzers is crucial for their performance. We developed a new algorithm which is fast and accurate (enough). I am not sure if this simulation will be used in industry, but it opened up new questions and challenges regarding the role of PTFE and where to place it.
Gas diffusion layers (GDLs) are usually coated with a hydrophobic agent to achieve a delicate balance between liquid and gas phases to maximize mass transport. Yet, most GDL numerical models to date have assumed an average contact angle for all materials, thereby eliminating the possibility of studying the role of the polytetrafluoroethylene (PTFE) content. This study introduces two mixed wettability algorithms to predict the mixed wetting behavior of GDLs composed of multiple materials. The algorithms employ contact angle and distance to solid materials to determine the critical capillary pressure for each pore voxel. The application of the algorithms to the estimation of capillary pressure vs saturation curves for two GDLs, namely, a micro-computed tomography (μ-CT) reconstructed SGL 39BA GDL and a stochastically reconstructed Toray 120C GDL, showed that, in agreement with experimental data, the addition of PTFE resulted in a decrease in saturation at a given capillary pressure. For Toray-120C, the mixed wettability model was capable of reproducing experimentally observed features in the intrusion curve at low saturation that could not be reproduced with a single wettability model, providing a clear link between PTFE coverage and intrusion at low saturation. Numerical results also predicted an increased breakthrough pressure and a decrease in saturation with increasing PTFE, in agreement with experimental observations. The decreased saturation at breakthrough improves gas transport through the layer while maintaining the layer's ability to remove water. Diffusivity simulations confirm the increase in diffusivity at breakthrough with increasing PTFE, thereby providing a rationale for the addition of PTFE, as well as for the optimal amount. This study emphasizes the importance of multimaterial wetting models and calls for more detailed investigations into PTFE and ionomer distributions in GDLs and catalyst layers, respectively.
Spatio-Temporal Electrowetting and Reaction Monitoring in Microfluidic Gas Diffusion Electrode Elucidates Mass Transport Limitations
Sebastian Brosch, Florian Wiesner, Alexandra Decker, John Linkhorst, Matthias Wessling
We developed a novel experimental setup (microfluidic) to visualize and study the complex interactions between water and electrodes in CO₂ reduction reactors. We hope to find new insights into the behavior of such gas diffusion electrodes.
The use of gas diffusion electrodes (GDEs) enables efficient electrochemical CO2 reduction and may be a viable technology in CO2 utilization after carbon capture. Understanding the spatio-temporal phenomena at the triple-phase boundary formed inside GDEs remains a challenge; yet it is critical to design and optimize industrial electrodes for gas-fed electrolyzers. Thus far, transport and reaction phenomena are not yet fully understood at the microscale, among other factors, due to a lack of experimental analysis methods for porous electrodes under operating conditions. In this work, a realistic microfluidic GDE surrogate is presented. Combined with fluorescence lifetime imaging microscopy (FLIM), the methodology allows monitoring of wetting and local pH, representing the dynamic (in)stability of the triple phase boundary in operando. Upon charging the electrode, immediate wetting leads to an initial flooding of the catalyst layer, followed by spatially oscillating pH changes. The micromodel presented gives an experimental insight into transport phenomena within porous electrodes, which is so far difficult to achieve. The methodology and proof of the spatio-temporal pH and wetting oscillations open new opportunities to further comprehend the relationship between gas diffusion electrode properties and electrical currents originating at a given surface potential.
Additive Manufacturing of Intertwined Electrode Pairs - Guided Mass Transport with Gyroids
Florian Wiesner, Alexander Limper, Cedric Marth, Anselm Brodersen, Matthias Wessling, John Linkhorst
During this study, I had access to a metal 3D printer. I used it to create novel electrode designs based on mathematical surfaces called triply periodic minimal surfaces (TPMS). Such 3D electrodes can have significantly higher surface area than conventional parallel plate electrodes as well as improved mass transport. Additionally, it is just fun to create crazy-looking metal things!
Electrochemical flow reactors facilitate the storage of renewable energies and the carbon-neutral production of platform chemicals. To maximize the reactor efficiency, unhindered mass transport in the flow channel and high surface electrodes is required. However, state-of-the-art reactors are limited by the conventional parallel plate designs. Herein, 3D intertwined electrode pairs are presented, based on triply periodic minimal surfaces that facilitate mass transport and provide high surface areas. Three gyroid designs with outer dimensions of 20 × 40 × 70 mm are manufactured from stainless steel via selective laser melting and implemented into a conventional flow cell. By design, the electrodes are rendered porous through the targeted control of the energy density during fabrication. Mass transport characterization by use of the fast ferri-/ferrocyanide redox reaction demonstrates that smaller unit cells and thus shorter interelectrode distances achieve significantly increased current densities. Moreover, the addition of convective channels formed by second-level gyroid structures removes diffusion boundary layers by promoting convective flow in electrode vicinity. The convective flow enhancement of the microscale channels even surpasses the effect of the unit cell size reduction, demonstrating importance of mass transport control. The integrated electrode design holds great potential for efficient next-generation electrochemical flow reactors.
Process model for high salinity flow-electrode capacitive deionization processes with ion-exchange membranes
Alexandra Rommerskirchen, Michael Alders, Florian Wiesner, Christian J Linnartz, Anna Kalde, Matthias Wessling
This was my Bachelor thesis. I developed a model (in gProms) for the flow-electrode capacitive deionization (FCDI) process. FCDI is a novel water desalination technology our chair uses to recover lithium from brines (battery waste). The simulation is able to predict the process behavior for a wide range of salinities.
Flow-electrode capacitive deionization (FCDI) is an electrically driven water desalination technology promising for many applications, such as industrial wastewater treatment. FCDI exploits the pumpability of carbon slurries, enabling a continuous process suitable for a wide range of feed salinities. Previously, we demonstrated the applicability of FCDI processes with incorporated ion-exchange membranes for the desalination and concentration of saline brines containing 60–120 g/L NaCl. At such elevated salinities, steep concentration gradients occur across the membranes of an FCDI cell. Hence, the characteristics of the membranes become crucial for the overall process performance. It is not yet fully understood, which physical phenomena dominantly influence the ion transport. In this article, we present the first FCDI process model focusing on brine treatment. While our previously published FCDI model (Rommerskirchen et al., 2018) was suitable for simulating the treatment of low salinity solutions, the model at hand includes more non-idealities and focuses on the ion transport through the ion-exchange membranes. We introduce a constriction factor (sigma-factor) for the diffusion coefficients to model the electrical double layer behavior within the membranes at steep concentration gradients. Hence, the model is now also suitable for the simulation of continuous FCDI processes for brine treatment and shows good correlation with experimental results.