Products TRIZ Cases

Separate zones for coal and biomass devolatilization reduce oxygen requirements while overcoming supply chain stability issues.

Merging bagasse with sugar filtration waste balances carbon-to-nitrogen ratios, enabling healthy plant growth while reusing industrial byproducts.

Isobaric thermal adsorption separates radon from carbon dioxide using active carbon substrates at atmospheric pressure.

Floating separation in a degassing basin removes air bubbles from rich solutions, preventing re-trapping caused by swirling flows in liquid cyclones.

Controlling heater skin temperature at 150 to 200 degrees Celsius prevents chemical reactions on the adsorbent during H2/CO mixture purification.

Organohalogen compound protects immobilized quaternary onium salt from degradation, maintaining high conversion rates during cyclic carbonate production.

Getter ceramics sorb vaporized alkalis to prevent lining damage and downstream clogging during biomass gasification.

Excess base enables complete biomass conversion to liquid hydrocarbons without expensive pretreatment, resolving low yield issues in wet feedstocks.

A horizontal reactor system separates carbon and glass fibers from composite materials through sequential thermal processing.

A melt pump delivers molten plastic to a reactor via a melting tank, preventing gas backflow and bridging.

Segmented absorption zones with varying amine concentrations minimize olefin co-absorption and solvent degradation during carbon dioxide removal.

A feed composition containing living pathogen-free worms delivers beneficial microbiota to poultry.

Amine absorption tower circulates liquid to an electrolysis apparatus for carbon monoxide production.

Porous organic nanocomposites trap photosensitizers in polymer matrices, preventing leaching and maintaining high photocatalysis efficiency.

Functionalized porous polymer networks adsorb carbon dioxide with high selectivity, reducing regeneration energy compared to amine scrubbing.

Solvents dissolve waste polycarbonates into a recovery solution, where functional compounds repair molecular weight to match virgin material quality.

A sensor detects recovered carbon dioxide to correlate target adsorption amounts, reducing energy loss during low-concentration recovery.

Aromatic heterocyclic amine catalysts facilitate carbon dioxide reduction to synthesis gas, resolving electrode instability and high energy consumption.

Segmented gates isolate fresh feed from pathogen-free discharge, eliminating contamination risks while enabling quasi-continuous biogas production.

Segmented absorption and regeneration columns circulate absorbing liquid through branching paths, reducing energy required for regenerating the liquid.

A polyolefin mixture blends recycled and virgin polymers to create lightweight materials.

Segmented modular units deploy near waste sources to eliminate transportation costs while maintaining processing capacity.

Task-specific ionic liquids capture carbon dioxide via reactive amine groups, eliminating volatile amine loss found in aqueous scrubbing systems.

A plasma incineration system ionizes oxygen to create a self-sustaining exothermic reaction that converts waste into hydrogen gas.

Treating refinery fuel gas via thermal swing adsorption and membranes purges pressure swing adsorption units, increasing hydrogen recovery from 88.9% to 93.1%.

High-pressure steam dries carbonaceous fuel in a flash dryer within an integrated gasification apparatus.

Tethering imidazole to an amine reduces vapor pressure and regeneration energy while maintaining effective CO2 removal.

A pyrolytic gas generating device uses a horizontal heat generator to process biomass feedstock efficiently.

A CO2 absorption liquid regeneration tower uses a segmented storage design with a smaller lower capacity part to reduce liquid residence time.

Feeding feed gas to a stripper column instead of an absorption column eliminates periodic pressure changes and reduces investment costs.

Engineered carbonic anhydrase variants overcome temperature stability limits to reduce energy penalties in industrial CO2 capture processes.

A NiO-Sr2TiO4 solid solution catalyst produces fine nickel grains to reform hydrocarbon gas with carbon dioxide or water vapor.

Segmenting rubber feedstock into 0.5-15 mm particles increases reactor throughput and product purity while reducing carbon grinding requirements.

Reducing unit converts SO2 to H2S for membrane recovery, cutting capital costs and emissions.

A sulfur dioxide-selective membrane separates SO2 from Claus process outlet streams to enable efficient sulfur recovery.

Segmenting capture into two systems allows the second absorber to release carbon dioxide at lower temperatures, reducing reboiler energy consumption.

Flash tank vaporizes CO2 absorbent while integrated heat exchangers transfer thermal energy between rich and lean streams.

A composite electrolyte membrane uses a metal-grafted porous structure to enhance proton conductivity and thermal stability.

Segmented water rinsing and co-current basic solution absorption reduce carbon dioxide and fine particulate matter emissions from industrial waste gases.

Liquifies recycled pyrolysis gas via compression and cooling, enabling transport as a chemical feedstock instead of burning it for facility heat.

Real-time sensor feedback regulates blowdown gas flow to stabilize tail gas output, reducing surge vessel size and capital costs.

Transverse intake holes disperse light phase reagents to resolve non-uniform distribution bottlenecks in urea synthesis reactors.

Self-heating fluidized bed torrefaction eliminates external energy needs, achieving 85% energy recovery and improved fuel handling.

Zinc chloride catalyzes hydrocarbon cracking at 500°C to yield CO2-free hydrogen and a separable carbon phase.

Saccharomyces cerevisiae anabolizes biochemical nutrients from food scraps under aerobic conditions to form stable biomass and nutrient-rich broth.

Polymerising heated carbon mixtures yields dense solid carbon materials with low sulphur content and ash yield, replacing depleting coking coal reserves.

Continuous recrystallization with polyethoxylated sorbitan stearate produces dense crystals, eliminating high energy drying costs.

Carbodiimide compounds enable dialkyl carbonate synthesis from carbon dioxide and alcohols, resolving low conversion rates and hazardous phosgene use.

A high-speed mixer precipitates polymer particles from solution using controlled shear forces.

Segmented deN2O and deNOx stages lower N2O and NOx concentrations while preserving energy recovery through high-temperature operation.