Gas Treatment TRIZ Cases

Dual-stage absorber recirculates enriched solution to block ammonia slip and prevent solid precipitation.

Thermal regeneration of desiccant during idle periods eliminates frequent replacement, extending service life and maintaining continuous operation.

Segmenting low Si/Al ratio zeolite from high stability silica-zeolite resolves the trade-off between cold-start adsorption capacity and hydrothermal durability.

Segmented channels with varied closure positions force exhaust gas through porous walls, reducing back pressure during cold start operation.

A zone-coated catalytic converter uses distinct upstream rhodium and downstream palladium layers to purify exhaust gases.

Oxidizing nitric oxide to nitrogen dioxide before selective catalytic reduction enables complete conversion with minimal reagent dosage.

A two-chamber separator uses a gas-permeable membrane and electrode to remove dissolved gases from liquid samples.

A three-stage membrane system uses a gas-gas ejector to compress permeate for efficient methane enrichment.

A bend in the exhaust flow passage refines urea water liquid particle size, resolving incomplete hydrolysis before the selective reduction catalyst.

Segmented catalyst zones convert harmful ammonia by-products into nitrogen while reducing NOx, CO, and HC emissions in stoichiometric CNG engines.

Patterned metal atoms on a mesoporous support retain xenon and krypton at elevated temperatures, overcoming the thermal instability of traditional zeolites.

Neodymium-doped ceria improves sulfur tolerance and low-temperature NOx release in adsorber catalysts.

A static mixer homogenizes dilute CO2 streams with fluid solvent to form a homogeneous gas-liquid mixture for subsequent chemical processing.

An ozone converter uses a bellows and piston to switch between bypass and active conversion modes based on ambient air pressure.

A rotating coalescer creates pumping pressure to maintain positive recirculation through a dynamic seal.

Biocatalysts accelerate CO2 absorption in carbonate solutions, reducing energy consumption during desorption.

A vehicle controller manages thermal energy from a heat accumulator and external recovery station to desorb captured carbon dioxide.

Tungsten, cobalt, and vanadium loaded on zeolite supports achieve over 90% NOx reduction efficiency.

A second catalyst layer with controlled large to medium pore ratios ensures uniform gas distribution for enhanced NOx storage.

Injecting nitrogen dioxide upstream of SCR-coated fabric filter bags promotes the fast SCR reaction, improving NOx removal efficiency below 250°C.

A gas treatment device integrates a sterile filter and catalyst into compressed gas lines to remove microbial contaminants and oxidative disinfectants.

Integrating fluid or mechanical harmonic balancers into spray dryer absorber atomizers reduces vibration and extends service life from 200 to over 12,000 hours.

Zoned CuO and platinum coatings on a wall flow substrate reduce hydrogen sulfide emissions while maintaining low back pressure.

Stabilized inorganic oxide supports minimize stable intermediate species formation, allowing complete regeneration at lower temperatures.

Segmented nozzles activate at specific heights to resolve inconsistent liquid distribution across varying flow rates in carbon dioxide capture systems.

Cooling combined turbine exhaust concentrates carbon dioxide, bypassing amine solvent reliability issues while lowering capture costs.

A catalytic bed deactivates reactive fuel vapors in storage tanks.

A high-purity silica sorbent bed captures heavy hydrocarbons via thermal swing adsorption.

Universal tank passages accommodate diverse engine routes, eliminating design complexity and supply chain bottlenecks.

Amorphous copper silicate adsorbs sulfurous stenches without releasing free copper ions that cause resin discoloration and deterioration.

SIFSIX-n-M metal organic frameworks separate carbon dioxide from vehicle exhaust gases through selective adsorption.

A potassium carbonate solvent absorbs carbon dioxide from compressed exhaust gas streams within a low emission power generation system.

Polymer composites with carbonate-infused activated carbon enable rapid carbon dioxide uptake through high porosity structures.

A direct contact cooler integrates ammonia stripping and flue gas cooling into a single unit to reduce thermal energy consumption.

Integrated sorbent-catalyst bypasses energy-intensive regeneration steps.

Modular gas processing cells share a common liquid space and fluid outlet within a single housing, reducing plot space and capital cost for CO2 capture.

Segmented cartridges with distinct media resolve adaptability complexity trade-offs in pollutant filtration.

Selenium-impregnated support adsorbs heavy metals from process streams across ambient to elevated temperatures.

A carbon capture device moves sorbent material between adsorption and desorption zones using an actuation mechanism.

Ceria nanoparticles disperse palladium on a composite alumina-zirconia support, preventing hydrocarbon poisoning and maintaining oxygen storage capacity.

Styrene-acrylonitrile filter media encapsulates fine fibers, preventing protrusion damage and eliminating stabilizer contaminants in electronic enclosures.

A TiO2-based composition captures halogenated impurities from synthesis gas at high temperatures, preventing catalyst poisoning in Fischer-Tropsch processes.

Limiting very fine particles below 5 μm stabilizes pneumatic conveyance, reducing pressure fluctuations and flow interruptions in flue gas treatment.

Reversible blowers drive vacuum pressure swing adsorption cycles, recovering energy from purge gas and equalization steps to reduce power consumption.

Optimizing the manganese-to-cobalt ratio in a barium zirconate perovskite catalyst resolves activity limitations, achieving 99.5% toluene decomposition rates.

A sweep membrane unit separates carbon dioxide from mixed combustion exhaust streams using selective permeation.

A centrifugal venturi sparger assembly produces a swirl flow to mix fuel gas with tail gas before catalytic reduction.

Hydrating calcium oxide prevents sintering and sulfur interference, maintaining sorbent porosity during cyclic CO2 capture.

Removing sealing elements creates a housing gap that improves rinsing efficiency and reduces hydrocarbon emissions.