Products TRIZ Cases

TJE-2 metal-organic framework adsorbs acetylene selectively via ultra-microporous channels, reducing energy consumption compared to cryogenic distillation.

A double-stage pressure swing adsorption method recovers hydrogen from biomass pyrolysis gas using sequential purification steps.

A continuous-cycle thermo-chemical decomposition apparatus uses a flame cap mechanism to prevent oxygen descent into the reaction chamber.

Tapered draft tubes reverse syngas flow to decrease drag on entrained quench liquid, resolving high moisture content issues in gasification systems.

A plug screw feeder adjusts rotational speed dynamically to maintain optimal biomass compression.

Segmented cooling recovers low-grade heat from acidic condensate to generate stripping steam, reducing pressure loss and material costs.

Segmented heating zones isolate chlorine removal before pyrolysis, preventing organic recombination and stabilizing pressure fluctuations.

Membrane wall gasification reactor protects refractory linings from degradation while converting deactivated catalyst-laden residue into synthesis gas.

Silver catalyst with rhenium and co-promoters maintains stability despite aging.

Sulfonyl polybenzimidazoles resolve thermal stability and solubility trade-offs, enabling H2/CO2 separation at 485°C.

Heating wet biomass via hydrous pyrolysis generates hydrogen on-site, eliminating costly transportation infrastructure and reducing energy consumption.

A thermoplastic polyurethane waterproof tape laminates a light-blocking film to seal mobile terminal micro interstices.

A mass transfer contactor unit integrates heat exchange channels within flow diversion barriers to cool process fluids during carbon dioxide scrubbing.

Parallel adsorption vessels cycle between capture and regeneration to recover hydrogen sulfide from Claus tail gas streams.

Direct mineral carbonation utilizes contaminant-laden carbon dioxide to produce stable composite sequestration products, eliminating costly purification steps.

Modifies pressure cycles and feed gas flow during compressor shutdown to sustain high hydrogen purity while reducing investment costs.

Ammonia injection equipment reduces mist generation materials in flue gas, preventing CO2 absorption liquid entrainment and scattering losses.

A compost controller monitors load currents to detect device errors and adjusts operations for continuous processing.

Vegetal or mineral oil washing removes tar from combustible gases, achieving less than 200 mg/Nm3 content while converting solid waste into energy.

A catalyst tower uses diameter expansion to buffer upstream pressure and allow gas expansion.

A Fenton reagent composition using modifying agents to delignify lignocellulosic biomass at reduced temperatures.

Segmented pyrolysis removes plastic matrix residues and oxidizes fiber surfaces to maintain mechanical properties.

BCDA-based semi-alicyclic polyimide membranes enable high gas permeability and selectivity for hydrogen, carbon dioxide, and oxygen separation.

A combined synthesis gas generation system merges a partial oxidation reactor with a catalytic reformer into a single integrated unit.

Integrated mineral carbonation uses combustion heat to activate serpentine at 580-800°C, reducing energy costs for industrial carbon dioxide sequestration.

A two-stage compressor integrates catalysts to convert oxygen and carbon monoxide using compression heat alone.

Ammoniated condensate absorbs carbon dioxide from process gases to concentrate the gas for reuse in soda ash production.

Plasma-assisted pyrolysis recovers high-quality carbon fibers from composite waste.

Reacting carbonaceous materials with sulfur compounds to form elemental carbon and sulfur products.

A gas separation tube selectively permeates helium from semiconductor exhaust streams using a porous membrane structure.

Pressure swing adsorption extracts inert CO2 from Fischer-Tropsch synthesis gas, resolving diffusion resistance and boosting C5+ hydrocarbon yield.

Atmospheric and vacuum distillation of bio-oil removes sulfur and metal impurities before stepwise calcination aligns carbon domains for industrial use.

Automated conductivity measurement determines degradant concentration in acidic gas-absorbing solutions.

Motor torque monitoring determines fill level without load cells, eliminating weight drift and calibration needs.

A solid catalyst component comprising a zeolite with a modifier and Group VIII metal alloyed with a transition metal converts mixed waste plastics.

Successive catalytic hydrolysis, acid washing, and activated carbon adsorption remove hydrofluoric acid contaminants to achieve high purity.

A composter device integrates a vertical rotating drum with a heat exchanger to condense moisture from exhaust air.

A heated reactor converts hydrogen sulfide into high-purity sulfur and hydrogen using catalytic decomposition at moderate temperatures.

Raman spectroscopy detects component concentrations in high-pressure urea streams, replacing costly chromatography to eliminate measurement delays.

A dual fluidized bed pyrolysis apparatus transfers hot particles between combustion and pyrolysis zones using a non-mechanical valve.

A heterocyclic amine and high-boiling solvent composite absorbent maintains a single phase state during carbon dioxide capture.

Electrospraying charged aqueous phases forms droplets with protective membranes, preventing coalescence in high-viscosity systems.

A copper catalyst oxidizes oxygen within a pressure swing adsorption bed, reducing bed volume and maintaining high hydrogen recovery.

A rotating oxidizer supply tube distributes gas through multiple ports inside a cylindrical storing unit.

Integrated pyrolysis reactor circulates heat transfer material to combustion boiler, eliminating additional fuel consumption.

A pyrolysis reactor uses a molten metal bath to decompose organic materials while a dedicated circuit recovers lost metal.

Separate oil lances co-feed fuel to maintain reactor productivity when biomass replaces coal in the feedstock.

A powdered desorption catalyst accelerates CO2 release from amine solutions.

Continuous static mixing of diisocyanate into aliphatic polyester prepolymer prevents evaporation and gelation during coupling reactions.

Replacing cryogenic cold boxes with a warm demethanizer column eliminates NOx explosion hazards while achieving high purity ethylene recovery.