An electrode module uses an insulating layer to separate parts for electrically adsorbing metal ions from liquid.
A direct coupling device concentrates sunlight to power a proton exchange membrane electrolyser.
A plating apparatus uses a gas flow generator and suction mechanism to remove processing liquid from substrate holders during transport.
A segmented lower shield encircles sputtering targets to manage heat flow and stabilize temperatures during plasma processing.
Fluorocarbon polymer coating seals anodized layer cracks to stop aluminum gas generation and substrate contamination.
A boric acid-free nickel electroplating bath uses alkylsulfonic zwitterions and saccharine to deposit satin nickel layers.
A high density plasma etchback process uses increased DC power and magnetic fields to boost ionization levels in PVD chambers.
Metal-containing cluster catalyst optimizes reaction efficiency and selectivity by controlling cluster size and composition.
Heated water generates high hydrostatic pressure to drive charged liquid microjets, converting waste heat into electricity and hydrogen gas.
Segmenting anodes into multiple independent power feeding portions resolves non-uniform current distribution and improves manufacturing precision.
Thermocompression bonding of a 1 μm pore reduction electrode prevents electrolyte swelling and maintains proton conduction during carbon dioxide reduction.
A surface pressure applying member converts seal pressing force into uniform pressure, preventing electrolyte membrane wrinkles during hydrogen generation.
A metal-carbon dioxide battery generates hydrogen gas at the anode while capturing carbon dioxide as alkali bicarbonate at the cathode.
A bismuth nanoparticle array on gallium nitride nanowires drives carbon dioxide conversion to formic acid.
Interrupting gas suction during electrolytic solution passage prevents leakage and ensures uniform metal film thickness.
Refractory metal gaskets prevent diffusion bonding in threaded connectors, maintaining sealing reliability during stack disassembly at 900°C.
Segmented parallel gas introduction tubes ensure uniform film composition while allowing easy removal without chamber disassembly.
A concentric conduit assembly channels water by gravity to an electrolysis cell while routing generated gas through an annular space.
An elastically deformable compression film transfers catalytic active layers onto proton exchange membranes via uniform pressing.
A protonic conductivity membrane electrolysis cell with a composite noble metal reduction catalyst enables efficient electrochemical hydrogenation of aromatic hydrocarbons.
Current sensors and feedback mechanisms adjust line currents to compensate for seed layer thickness variations and contact resistance.
An insulating support part maintains a fixed gap between adjacent electrochemical cells, preventing liquid leakage and stabilizing the gas flow path.
Periodic anodic pulses regenerate poisoned copper surfaces while cathodic phases drive hydrocarbon synthesis, sustaining high Faraday efficiency.
A substrate monitoring system detects surface oxide by measuring current and voltage responses during electrolyte immersion.