Direct Conductive Path
The catalyst is integrated with a metallic current-collecting network to reduce unnecessary interlayers.

A modular NiFeOx electrode family designed for alkaline water electrolysis, AEM electrolysis, oxygen-evolution studies and electrolyzer development. Choose from fiber papers, foams and woven metal cloths, then match the interface chemistry to your test environment.
Youveim® E100–E107 electrodes are engineered to help researchers change the physical electrode platform without rebuilding the entire catalyst system. The same NiFeOx concept can be supplied on stainless steel, titanium or nickel in fiber-paper, foam or woven-cloth formats.
This modular approach supports faster screening of contact resistance, electrolyte compatibility, gas release, compression behavior, flexibility and long-duration stability across alkaline electrochemical devices.
The catalyst is integrated with a metallic current-collecting network to reduce unnecessary interlayers.
Porous and woven substrates provide connected channels for electrolyte access and bubble evacuation.
Select thin cloth, fiber paper or 3D foam according to cell geometry, compression and flow-field design.
Available for coupon testing, custom cutting, MEA preparation and electrolyzer fixture matching.
Move from basic OER screening to integrated alkaline or AEM electrolyzer evaluation using a consistent product family and comparable catalyst-loading options.
A nickel–iron oxide catalyst layer positioned for oxygen-evolution studies and alkaline anode development.
Compare stainless steel, titanium and nickel across fiber paper, foam and woven-cloth structures.
Choose a general binder, anion-exchange ionomer, hydrophobic PTFE interface or Au-coated substrate upgrade.
Standard sizes range from 1 × 1 cm to 20 × 20 cm, with non-standard cutting and processing available.
The table is a selection guide for relative positioning. Final choice should be confirmed against electrolyte, temperature, pressure, compression, flow-field and lifetime requirements.
| Series | Base Substrate | Architecture | Conductivity | Corrosion Resistance | Flexibility | Gas Release | Recommended Positioning | Variants |
|---|---|---|---|---|---|---|---|---|
| E100 | Stainless-steel fiber paper | Planar porous fiber network | General OER screening and interface studies | N / A / T G | ||||
| E102 | Titanium fiber paper | Planar porous Ti fiber network | Corrosion-focused and long-duration testing | N / A / T G | ||||
| E103 | Nickel fiber paper | Planar porous Ni fiber network | ALK/AEM anodes and MEA-style assemblies | N / A / T G | ||||
| E104 | Nickel foam | Three-dimensional open-cell foam | High-current gas evolution and thick porous electrodes | N / A / T G | ||||
| E105 | Stainless-steel cloth | Flexible woven metal mesh | Flexible electrodes and woven-substrate studies | N / A / T G | ||||
| E106 | Nickel cloth | Flexible woven Ni mesh | Lightweight alkaline/AEM testing and flexible stacks | N / A / T G | ||||
| E107 | Titanium cloth | Flexible woven Ti mesh | Flexible, corrosion-resistant and long-duration systems | N / A / T G |
Relative ratings use a four-level scale (Low, Moderate, High and Very High) for product selection guidance; they are not certified material-property values.
Every substrate series can be configured through the product suffix system, allowing the catalyst–electrolyte interface or current-collector surface to be adapted to the target device.
A practical reference configuration for general electrocatalysis and comparative OER testing.
Designed for alkaline and AEM environments where an OH⁻-conducting interfacial phase is preferred.
A hydrophobic interface option for gas management, bubble detachment and water-distribution studies.
An Au-coated metal-substrate option for improved contact behavior and demanding interface-stability studies.
Choose a substrate architecture according to the role of the electrode in the device, not only according to catalyst chemistry.
Use nickel-based fiber paper, foam or cloth for anode development, catalyst-layer screening and fixture-level performance evaluation. Titanium or stainless-steel platforms can support comparative studies and specialized interface requirements.
Compare catalyst loading, binder chemistry, substrate topology and geometric area using a consistent electrode family.
Pair the NiFeOx oxygen-evolution electrode with a suitable cathode architecture in alkaline or anion-exchange systems.
Evaluate contact stability, substrate oxidation, compression and electrolyte exposure with optional Au-coated upgrades.
Prices are reference values in USD per piece. Au-coated models and non-standard configurations require a separate quotation.
The full data set is rendered dynamically, keeping the HTML compact while preserving every standard model, loading and size combination from the supplied source.
| Series | Substrate | Model / Interface | Loading mg cm⁻² | 1 × 1 cm | 2 × 2 cm | 3 × 3 cm | 4 × 4 cm | 5 × 5 cm | 10 × 10 cm | 20 × 20 cm |
|---|
Reference pricing: USD per piece. “Quote” indicates that substrate coating, dimensions, quantity or processing requirements must be confirmed individually.
Share the operating conditions together with the requested physical format to reduce iteration during quotation and engineering review.
Specify OER test cell, AEM electrolyzer, alkaline fixture, CO₂ electrolyzer anode or stack-level use.
Choose metal chemistry and architecture based on conductivity, corrosion, compression and gas-management needs.
Choose N, A, T or G according to electrolyte chemistry, ion transport and contact-stability requirements.
Provide catalyst loading, size, quantity, cutting tolerance, active area and any MEA-processing request.
Use these answers as a starting point; final recommendations depend on the complete electrochemical and mechanical operating conditions.
N uses a Nafion® binder, A uses an anion-exchange ionomer, T uses a PTFE-based hydrophobic interface, and G identifies an Au-coated substrate upgrade.
Nickel-based E103, E104 and E106 are practical starting points. The A suffix is intended for anion-conducting interface matching, while the final selection should also consider cell compression, flow field and electrode thickness.
The Au-coated configuration depends on substrate, coating specification, dimensions, quantity, masking and processing requirements, so it is confirmed on a project basis.
Yes. Provide the target size, active area, NiFeOx loading, substrate, quantity, cutting method, fixture geometry and operating conditions for review.
No. They are reference prices in USD per piece. Bulk purchasing, custom processing, taxes, logistics and project-specific requirements should be confirmed before ordering.
Cutting, electrode matching, MEA-related processing and electrolyzer-fixture support can be discussed based on membrane type, active area, sealing structure and target operating conditions.
Availability, specifications and delivery options may vary by platform. Search for the Youveim® model number or contact SCI Materials Hub for the current listing and configuration.
Browse international listings and contact the seller regarding model availability, dimensions and shipping options.
Visit eBay ↗Search by the Youveim® brand or electrode model for available research-grade products and accessories.
Visit Amazon ↗Explore cross-border purchasing options for standard electrode sizes and selected laboratory configurations.
Visit AliExpress ↗View product introductions, electrode structures, assembly guidance and electrochemical application demonstrations.
Visit YouTube ↗Send the electrolyte, temperature, current-density target, active area, fixture structure and expected test duration.
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