Injection-molded conductive bipolar plate channels cut membrane contact area to reduce water buildup, pressure loss, and resistance.
Magnetic gas diffusion layers hold to metal bipolar plates, preventing slip during fuel cell and electrolysis stack assembly.
Elongated nanostructures extend from the separator into the diffusion layer to cut contact resistance in electrochemical cells.
Spatially varied 3D electrode porosity balances fluid flow and conductivity in electrochemical reactors to cut power losses and improve efficiency.
Adaptive control of modular H-bridge DC-DC converter units lets electrolysis systems use low-voltage DC sources with lower conversion losses.
A converted metal-compound electrolyte boosts ionic conductivity at lower solid oxide cell temperatures, cutting thermal stress and material cost.
Independent clamping on annular seals and elastic plates suppresses fuel cell stack gas leakage despite thermal expansion.
Staggering CO2 before H2O feed shifts electrolysis equilibrium to raise hydrocarbon output while cutting H2 use and power consumption.
A redox mediator and ion-selective membrane recover lithium from LiFePO4 in one step, cutting acid use, waste, and process complexity.
Controlled anode-cathode potential enables low-energy electrolysis to elute and recover cobalt and nickel from used battery materials.
Modeled conductive-element layouts contain heat in metallurgical vessel current collectors, preventing leaks and extending service life.
Separate oxygen and hydrogen tanks prevent explosive gas mixing while enabling high-purity extraction and nickel-hydrogen battery recycling.
A shared bidirectional converter with reverse current protection decouples electrolyzer and fuel cell power flow across distinct voltage bands.
An integrated ammonia fuel cell and bipolar-membrane stack cuts external power demand while enabling efficient hydrogen production and power generation.
Projections with side or top openings improve gas transport and contact pressure while avoiding costly sintering in PEM electrochemical cells.
Selective recycle from the second SOFC stack with water knockout cuts dilution and flow volume while improving fuel utilization and efficiency.
A descending solvent layer and side exhaust guide water-repellent gas over the full substrate, improving uniformity while reducing agent use.
Heating-medium channels in end plates keep humid hydrogen above the dew point, preventing blockage and stabilizing compression.
Profiled catalyst and microporous layers interlock to prevent delamination, improve electrical contact, and reduce water buildup in cells.
Measured component heights guide electrochemical stack assembly, avoiding rework and keeping final stack height within tolerance.
A pivoting plate with elastic contacts measures many electrolysis stack levels at once, avoiding manual welding in high-temperature QC.
An elastic layer between the anode and face seal closes pressure-driven gaps, preventing membrane sagging and rupture in hydrogen compression.
A coupled SOFC-SOEC setup turns CO2 and hydrocarbon gas into syngas using internally generated electricity, avoiding external power.
Conductive oxide supports with oxygen vacancies improve catalyst adhesion and stability, cutting Ir and Ru loading in PEM electrolyzers.
Slotted baffles and mesh in an electroplating paddle chamber curb fluid splashing, cut cleaning downtime, and stabilize metal deposition.
Rolling metal with penetration spaces shrinks surface openings to balance SOFC support strength, permeability, and mass-production cost.
A graded Sr/Ba perovskite electrolyte suppresses hole conduction while maintaining high ion transport and low resistance in proton cells.
A single separator with channels on both sides replaces paired anode and cathode plates, simplifying electrolysis stack assembly and lowering contact resistance.
A high-surface-area iridium-tantalum rutile oxide improves oxygen evolution activity and resists carbon corrosion during fuel cell reversal events.