Electrolyte Stream Management TRIZ Cases

Flowable electrolyte channels carry digital signals and sense deformation, cutting copper wiring, weight, and bulk in redox flow batteries.

A rebalancing cell uses charging-generated hydrogen to lower electrolyte pH in situ, preventing iron precipitation and battery downtime.

Mating protrusions and recesses form seal lines that separate flow channels, cutting flow battery sealing cost and assembly complexity.

Extended edge seal chambers redirect anode and cathode gases into parallel flow, reducing thermal distortion and contact loss in fuel cell stacks.

Reconfigurable subflow paths hold battery SOC, enable inline electrolyte diagnostics, and limit self-discharge and degradation.

By housing tanks, cell, pipes, and pump in one container, this battery cuts installation space and simplifies on-site assembly.

Parallel anode and cathode flow through extended edge seal chambers reduces thermal gradients, preserving fuel cell stack planarity.

Staged catalyst-bed reactors oxidize hydrogen and reduce metal ions to correct electrolyte imbalance and preserve redox flow battery capacity.

A vacuum degassing tank and pump remove gas from flow battery electrolyte during circulation, preserving stack efficiency without interrupting operation.

A wicking ionic barrier isolates the reference electrolyte to measure redox flow battery charge state with less drift, contamination, and cost.

Foreign matter detection triggers pressure changes in both circulation loops to scour stack blockages and keep flow batteries stable.

Sensors and a control unit verify the insulating cover is closed before conveyor startup, reducing electric shock risk during maintenance.

Partition plates with through-holes guide electrolyte through tank regions to suppress vortices, avoid stagnation, and improve utilization.

A portable hydrocyclone and sub-2-micron filter train purifies gel-shipped VRFB electrolyte on-site by precipitating and removing impurities.

A portable filter and thermal loop purifies densified VRFB electrolyte on-site, reducing fouling and extending battery component life.

Electrolyte concentration tuning lets one mediator handle charge and discharge, cutting viscosity and pump power in solid-active redox flow batteries.

Laminar electrolyte flow in membraneless microcells limits crossover and advective mixing, improving redox battery stability and life.

A three-chamber balancing cell uses bipolar membrane water splitting to correct flow battery pH and charge imbalance without added acids or bases.

An amine-containing alkaline electrolyte limits CO2 damage and water dilution, helping fuel cells maintain concentration and longer service life.

An internal stack reactor rebalances flow battery electrolyte before hydrogen bubbles coalesce, cutting parasitic power and catalyst use.

Doubly bridged aromatic active materials raise aqueous electrolyte solubility and multi-electron transfer, improving flow battery energy density and cycle life.

An injector placed inside the electrolyte tank entrains hydrogen with electrolyte flow to cut leakage, backpressure, and pump burden.

A dynamic fluidic network adjusts electrolyte flow paths for real-time diagnostics, lower energy waste, and shunt current management in flow batteries.

Returning electrolyte is used to drive radial tank mixing, cutting stirrer power demand, pipe loss, and support issues in redox flow batteries.

A tube-integrated magnetic field captures iron fragments in redox flow battery electrolyte before they score magnetic-drive pump housings.

Integrated guide channels in the electrode improve electrolyte homogeneity while reducing diffusion and hydrodynamic losses in redox flow batteries.

A vapor-phase solvent recovery loop rebalances incompatible redox flow battery electrolytes to preserve concentration, capacity, and efficiency.

Blocking material forms quasi-interdigitated bipolar plate channels that improve electrolyte distribution without costly machining or moulding.

Switchable fluidic paths isolate the electrode region for sampling and diagnostics while reducing self-discharge in flow batteries.

Hydrogen sulfide rebalances iron flow battery electrolytes by reducing excess Fe3+ to Fe2+, cutting rebalancing cost and complexity.

A porous-layer reactor contacts hydrogen and electrolyte at a controlled interface to cut mass transport losses in redox flow battery rebalancing.

Preassembled stack and tank frames cut on-site piping and field work, enabling faster transport, installation, and modular scaling.

Hydrogen from charging lowers third-electrolyte pH to rebalance iron flow batteries and prevent Fe(OH)3 precipitation without acid flushing.

A switchable fluidic network isolates the electrode region for sampling, enabling electrolyte diagnostics and tighter flow control with less waste.

Modular frame segments improve stack flatness and sealing in redox flow batteries while lowering tolerances, cross-contamination, and cost.

Open flux surface structures guide electrolyte along the electrode to cut hydraulic and voltage losses while improving mass transport in redox flow batteries.

Dynamic pump control calculates charge-discharge efficiency from inlet and outlet state of charge data, reducing pumping losses while preventing gas generation.

Optimized slit curvature reduces shunt current loss and suppresses frame strain while improving electrolyte heat dissipation.