The Green Hydrogen Buildout Has a Materials Problem

Water electrolysis — splitting water into hydrogen and oxygen using electricity — is the core reaction behind every green hydrogen project now under construction, from Saudi Arabia's 2.2 GW NEOM complex to the multi-gigawatt alkaline electrolyzer lines commissioning across Germany, the Netherlands, China, and South Korea. Scaling electrolysis from lab bench to gigawatt-scale industrial infrastructure is not just an electrical engineering problem. It is a materials sourcing problem, and nickel foam sits near the center of it.

Every electrolyzer stack needs an electrode substrate that can hold catalyst material, conduct current with minimal loss, survive a highly corrosive electrolyte for a multi-year service life, and let hydrogen and oxygen gas bubbles escape without disrupting the reaction. Very few materials satisfy all four requirements at a cost that scales to gigawatt production. Nickel foam is the material the alkaline electrolysis industry has converged on.

Why this matters beyond the hydrogen industry

Independent market analyses now estimate that electrolyzer applications account for roughly 55–65% of global nickel foam electrode substrate demand by value — ahead of nickel-metal-hydride batteries, supercapacitors, and industrial filtration combined. For anyone sourcing or manufacturing nickel foam, electrolyzers are no longer a niche application; they are the demand driver.

The Four Properties Electrolyzer Electrodes Actually Need

Alkaline water electrolyzers run at high current densities inside a bath of concentrated potassium hydroxide (KOH) electrolyte, typically operating for a decade or more without electrode replacement. That combination of conditions rules out most low-cost conductive materials quickly:

  • High surface area for catalyst loading. Nickel foam's open, three-dimensional cellular structure provides dramatically more surface area per unit volume than a flat plate or mesh electrode, which means more catalytic reaction sites for the same stack footprint — directly improving current density and reducing the size (and cost) of the stack needed for a given hydrogen output.
  • Metallic electrical conductivity. As a solid nickel structure rather than a coated or composite material, the foam conducts current with minimal resistive loss through the electrode itself, which matters at the current densities modern alkaline stacks are designed to run at.
  • Corrosion resistance in KOH electrolyte. Nickel is one of the few economical metals that remains chemically stable in concentrated alkaline solution over years of continuous operation — the same property, incidentally, that makes it useful in nickel-metal-hydride batteries, which also use alkaline electrolyte.
  • Efficient gas bubble release. Electrolysis generates hydrogen and oxygen gas continuously at the electrode surface. If bubbles cling to the electrode instead of escaping, they physically block active reaction sites and increase cell voltage — wasted energy that shows up directly on the electricity bill for every kilogram of hydrogen produced. Foam's interconnected open-pore geometry is significantly better at releasing bubbles than a flat or lightly perforated electrode.
A note on PEM electrolyzers

Proton exchange membrane (PEM) electrolyzers use an acidic polymer membrane instead of liquid KOH — and nickel corrodes rapidly in acidic conditions. PEM systems generally require titanium substrates, often with platinum-group catalyst coatings, on at least one electrode. Nickel foam's advantage is specific to alkaline and the emerging anion exchange membrane (AEM) electrolyzer category, which is itself gaining share because it aims to combine alkaline-electrolyzer material costs with PEM-style compact stack design.

Specifying Electrolyzer-Grade Nickel Foam: Pore Size Is the Key Trade-Off

Not all nickel foam is interchangeable across applications. The pore size that makes sense for an air filter is not the pore size that makes sense for an electrolyzer electrode, and this is where a materials supplier's application experience matters more than the headline "nickel foam" spec.

Filtration-grade nickel foam — the kind used in server dust filters or HVAC applications — is typically specified in the 10–30 PPI (pores per linear inch) range, prioritizing airflow and particle capture geometry. Electrolyzer electrode substrates run considerably finer, commonly in the 60–110 PPI range, because the priority shifts to maximizing surface area for catalyst loading per unit volume. The trade-off runs in the opposite direction from filtration: finer pores mean more surface area and more reaction sites, but also a greater risk of gas bubbles becoming trapped inside the structure if the pore network isn't well interconnected. Getting this balance right is a real materials engineering decision, not a catalog lookup.

Scale of material required

Industry estimates put nickel foam consumption at roughly 10–30 square meters per megawatt-class alkaline electrolyzer stack, depending on stack design and target current density. A single gigawatt-scale project — the size now common in Saudi, European, and Chinese green hydrogen buildouts — can require tens of thousands of square meters of electrode-grade foam. At that scale, supply reliability and consistent pore geometry across production batches become as important as the base material properties.

Why This Is the Fastest-Growing Segment for Nickel Foam

Nickel foam has been a known material in NiMH batteries and industrial filtration for decades. What has changed is the scale of the electrolyzer buildout it now feeds. The European Union's hydrogen strategy targets tens of gigawatts of installed electrolyzer capacity this decade. Saudi Arabia's NEOM green hydrogen complex alone represents a 2.2 GW alkaline electrolyzer commitment. Multiple market analyses tracking the electrolyzer supply chain now place electrolyzer applications at an estimated 55–65% share of global nickel foam electrode substrate demand by value as of 2026 — a level that would have been unthinkable a decade ago, when batteries and filtration dominated demand.

For hood and equipment manufacturers who already know nickel foam from filtration or EMI shielding applications, the practical takeaway is this: the same base material family is now being pulled into a much larger, faster-growing market, and the specification requirements are different enough (finer PPI, higher surface area, electrolyte compatibility) that they're worth understanding before assuming a filtration-grade product will work as an electrode substrate.

Nickel Foam: Filtration Grade vs. Electrolyzer Grade

Choosing the Right Nickel Foam Grade by Application

Filtration-Grade Nickel Foam

  • Typical PPI: 10–30
  • Priority: Airflow, particle capture
  • Environment: Air, dry conditions
  • Key applications: HVAC, server dust filters, kitchen exhaust

Electrolyzer-Grade Nickel Foam

  • Typical PPI: 60–110
  • Priority: Surface area, catalyst loading, gas release
  • Environment: Concentrated KOH electrolyte
  • Key applications: Alkaline & AEM electrolyzer electrodes

Both grades start from the same manufacturing process family — electrodeposition of nickel onto a polymer foam template, followed by pyrolysis and sintering to leave a pure metallic nickel scaffold — but the template pore size, foam density, and post-processing are tuned differently for each end use.



Frequently Asked Questions

Nickel foam is used as the gas diffusion layer and electrode substrate in alkaline water electrolyzers because it combines very high surface area for catalyst loading, excellent electrical conductivity, and strong corrosion resistance in concentrated KOH electrolyte. Its open, interconnected pore structure also lets hydrogen and oxygen gas bubbles escape efficiently, reducing bubble-induced resistance losses during electrolysis.
Alkaline electrolyzers use a liquid KOH electrolyte and are the dominant commercial technology; nickel foam is the standard electrode substrate here because nickel is stable in alkaline conditions. PEM electrolyzers use an acidic polymer membrane instead, which corrodes nickel — PEM systems generally require titanium or platinum-group-coated substrates. Nickel foam's core application is concentrated in alkaline and emerging anion exchange membrane (AEM) electrolyzer designs, not acidic PEM stacks.
Industry estimates place nickel foam consumption at roughly 10 to 30 square meters per megawatt-class electrolyzer stack, depending on stack design and current density. A gigawatt-scale electrolyzer project can require tens of thousands of square meters of electrode-grade nickel foam.
Electrolyzer electrode substrates typically use finer, higher-surface-area nickel foam than filtration-grade material, commonly in the 60 to 110 PPI range, to maximize catalyst surface area while still allowing generated gas bubbles to escape without excessive entrapment. The optimal pore size trades off surface area, gas permeability, and mechanical handling during electrode fabrication.
Yes. Multiple independent market analyses place electrolyzer applications at an estimated 55 to 65 percent of global nickel foam electrode substrate demand by value as of 2026, driven by gigawatt-scale alkaline electrolyzer projects across Germany, the Netherlands, China, South Korea, and the Middle East. This makes electrolyzers the largest single application segment for nickel foam, ahead of NiMH batteries and industrial filtration.
Yes. PrometheanFoam manufactures open-cell nickel foam across a range of PPI grades, including higher-surface-area grades suited to electrode and gas diffusion layer applications. Electrolyzer OEMs and system integrators can contact PrometheanFoam at prometheanfoam.com or (307) 533-4550 for technical datasheets, sample kits, and qualification-quantity orders.
Dr. James Mitchell
Chief Technical Officer, PrometheanFoam
Dr. Mitchell has 15+ years in advanced materials engineering, with a focus on open-cell metallic foam for energy storage, electrolysis, filtration, and EMI shielding. He has co-authored peer-reviewed research on metal foam electrode and filtration mechanisms, and holds a Ph.D. in Materials Science and Engineering.