Ion Exchange Membranes Prevent Nanobubble Detachment But Do Not Limit Electrolysis Current

04 July 2025, Version 1
This content is a preprint and has not undergone peer review at the time of posting.

Abstract

Gas bubble evolution at electrochemical interfaces critically impacts electrolyzer performance and durability yet remains poorly understood at the nanoscale. Using reactive molecular dynamics at constant potential, we reveal that ion-exchange membrane proximity anchors nanobubbles on Pt nanoparticles, preventing detachment while maintaining average steady-state hydrogen evolution currents indistinguishable from those of membrane-free systems. In contrast, direct ionomer adsorption onto the catalyst results in larger reduction of the current due to active site occlusion. Anchored nanobubbles locally displace interfacial water, creating dehydrated regions at the membrane interface that can accelerate chemical degradation pathways in anion-exchange membranes. By resolving nanobubble dynamics in the 1–2 nm confinement regime inaccessible to experiments, our results demonstrate that membrane proximity governs bubble confinement without compromising efficiency, reframing it as a design parameter for durability management in electrolysis systems. These insights advance molecular-level strategies for catalyst–membrane interface engineering in hydrogen and CO₂ electrolyzers.

Keywords

electrolyzer
membrane-electrode assembly
nanobubbles
polymer electrolyte membranes
electrocatalysis
current-voltage relations

Supplementary materials

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Supporting Information
Description
The Supporting Information (PDF) includes six sections: • A. Simulation Methods – Describes the force fields, kinetic Monte Carlo algorithm, membrane model, GDL treatment, and current calculation proto-col. • B. Electrode-membrane Configurations – Details the setup of simulations for the different elec-trode positions, along with resulting bubble sizes and stationary currents. • C. Bubble Size Evolution – Presents the time evolution of the nanobubble size across different con-figurations. • D. Current Time Trace – Presents the time evo-lution of the current for different configurations. • E. Control Simulations with Flat Walls – Discusses systems where the membrane is replaced by flat hydrophilic walls at fixed distances from the elec-trode. • F. Water-Membrane Contact – Shows radial distribution functions (RDFs) between water and membrane before and after bubble nucleation.
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