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Microporous layers (MPLs) are not new to electrochemistry. Their role has been well understood and optimized in PEM fuel cells over decades of development. As electrolyzers gained momentum, it was natural to assume that this existing knowledge base could be directly applied.

However, shared origins do not mean shared operating reality. The assumption that MPLs behave similarly across both systems is increasingly limited. As PEM electrolyzers evolve, it becomes clear that they are governed by fundamentally different constraints.

Operating in unique environments

The anodic environment of a PEM electrolyzer introduces conditions that are far more aggressive than those in fuel cells. High potential, pressure gradients, and strongly oxidative conditions define the operating space. These factors place immediate limitations on material choices and structural stability.

This is why commonly used carbon-based MPLs in fuel cells are no longer viable. Instead, electrolyzers require corrosion-resistant, carbon-free solutions capable of maintaining integrity under sustained oxidative stress. The operating environment itself fundamentally reshapes what an MPL must be.

MPL’s functional role shifts with the application

Fuel cells and electrolyzers may share a layered architecture, but their functional priorities diverge. In fuel cells, MPLs are largely designed to support reactant diffusion and manage water removal under power generation conditions. The focus is on balancing gas transport and preventing flooding. 

In electrolyzers, the role reverses. The system depends on continuous water supply to sustain the oxygen evolution reaction, while efficiently removing generated oxygen. This changes the design logic entirely, making hydration, oxygen evacuation, and interface stability, the dominant factors.
 

Higher current densities push limits

Modern PEM electrolyzers are being pushed to operate at significantly higher current densities, often exceeding ranges typical for fuel cells. Under these conditions, transport phenomena become more dynamic and less forgiving. Bubble formation, thermal gradients, and local dry-out begin to directly impact performance.

These effects are not isolated; they interact across the interface. As a result, MPL uniformity becomes critical, not just overall performance. Small inconsistencies in structure or coating can translate into system-level inefficiencies.
 

Amplifying risk with reduced design margins

At the same time, stack architectures are shifting toward thinner membranes and lower iridium loadings. While these changes improve cost efficiency, they reduce tolerance for resistance, uneven contact, or flow irregularities. The system becomes more sensitive to interfacial behavior.

In this context, the MPL plays a dual role. It acts as an enabler of performance, but also as a potential source of instability if not carefully engineered. What was once a supporting layer becoming a critical control point.
 

Still early-stage, but important

Compared to fuel cells, MPL development for electrolyzers is still in an earlier phase. Challenges such as scalability, coating uniformity, and integration with advanced MEAs remain open. However, this should not be seen as a limitation.

It represents a window to innovation. As hydrogen production scales, MPL design will increasingly influence efficiency, durability, and ultimately the cost of hydrogen. This shifts MPL development from incremental improvement to a strategic lever.
 

Looking ahead

If MPLs in electrolyzers are not simply adapted from fuel cells, then the question becomes more fundamental. Which design principles, material choices, and integration strategies will define the next generation of systems? The answer will likely come from rethinking MPLs as system-level components. Not as inherited solutions—but as interfaces engineered specifically for the demands of high-current, cost-sensitive hydrogen production.