See how a segmented alumina and molecular sieve layer design allows controlled water breakthrou
See how an ASU pre-purification unit allows temporary N₂O elevation during chiller trips to mai
See how a segmented alumina and molecular sieve layer design allows controlled water breakthrou
See how a manganese oxide and copper oxide catalyst on rare earth support removes ozone and VOC
See how CO2 scrubbing with zeolites and oxygen injection reduce HVAC air replacement rates, low
See how composite adsorbent laminates with segmented zeolite and alumina layers enable rapid cy
Gas scrubbers and oxygen injection maintain indoor air quality while cutting HVAC thermal load and outside air replacement.
Copper-manganese oxide on supported substrates removes ozone and VOCs at lower cost while sustaining air-cleaning performance over time.
CO2 scrubbing and oxygen enrichment cut outside air intake, maintaining indoor air quality while lowering HVAC thermal load and energy use.
Sequential cooling, NOx removal, reheating, and Hg0 adsorption protect aluminum cryogenic equipment while enabling reliable CO2 purification.
Gas scrubbers and oxygen injection maintain indoor air quality while reducing outside air exchange, HVAC thermal load, and energy use.
Integrated pre-treatment, reaction, and heat exchange improve fluorine and N2O removal while recovering waste heat and lowering energy use.
A graphitized carbon shell over NiO-alumina nanoparticles enables lower-temperature N2O decomposition and VOC combustion with lower catalyst cost.
A grooved brake lining and negative-pressure filter capture friction gases and particles, reducing brake emissions and component fouling.
Moisture is removed upstream so adsorbent collectors can continuously recover anaesthetic agents and cut exhaust pollution.
A vacuum-linked groove and filter collect brake lining gases and particles during friction, reducing emissions and protecting nearby components.
PGM on doped TiO2 improves ammonia oxidation and N2 selectivity while lowering N2O formation and preserving hydrothermal stability.
Air plasma generates NOx that is absorbed in staged pH-controlled loops to cut ammonia loss, odor, and nitrogen depletion from organic material.
A mixed iron chabazite and iron beta zeolite catalyst cuts NOx and N2O with stable activity over a wide temperature range.
Phasewise NOx variation makes the SCR NH3/NOx ratio oscillate, improving low-temperature conversion while limiting ammonia slip and deposits.
Combustion in a surrounding second reactor heats the reduction zone, cutting abatement energy use while widening operating conditions.
Adding ammonia upstream lets the N2O catalyst also reduce NOx during startup and shutdown, cutting plume emissions without extra heating.
Vertical sorbent panel-beds remove ammonia from indoor air without raising ventilation rates, cutting heat loss, emissions, and energy use.
A staged denitration and ammonia decomposition catalyst layout lowers NOx and ammonia while suppressing N2O in high-NOx exhaust.
An axially coated Cu-Fe zeolite SCR catalyst balances high NOx conversion with lower N2O emissions under standard and fast SCR conditions.
Molten alkali borate sorbents capture and separate multiple non-CO2 acid gases at high temperature, cutting process steps and regeneration energy.
Reflective surfaces, solar concentration, and thermal control help plasmonic reactor cells cut energy use while sustaining photocatalytic reforming.
A floating sieve and support structure lets an axial catalyst bed expand thermally, simplifying replacement while preventing bypassing.
Spinel Ni-Co catalyst compositions maintain N2O decomposition at low temperature in moist, sulfur dioxide-containing exhaust gas.
Gas-permeable tubular members spread exhaled nitrous oxide evenly through the catalyst bed, improving decomposition and limiting hot spots.
A Pt-rich zone paired with high-Cu/Al zeolite boosts ammonia conversion while limiting N2O and NOx in engine exhaust.
A staged catalyst train combines passive SCR, ammonia oxidation, regulated SCR, and N2O decomposition to cut greenhouse exhaust emissions.
Rare earth ion-exchanged AEI zeolite coatings improve NH3-SCR catalyst stability, low-temperature activity retention, and SO2 poisoning resistance.
Sequential catalysts first decompose ammonia, then break down N2O and NOx in ammonia-fueled combustion exhaust to cut emissions.
Ozone added to the nitric acid stream before absorption accelerates NOx oxidation, cutting exhaust emissions without high-pressure complexity.
A dual-zone copper molecular sieve coating places lower Cu upstream and higher Cu downstream to raise NOx conversion while limiting N2O.
A ruthenium catalyst on titanium oxide with zirconium or silicon maintains nitrous oxide decomposition rates longer by resisting deactivation.
Dispersed anatase TiO2 penetrates concrete to continuously reduce NOx and VOCs while also sealing and hardening existing surfaces.
A wet scrubber and downstream catalyst bed cut residual PFC by-products and hydrocarbons after lower-temperature abatement.
Copper CHA zeolite tuned with potassium and cesium improves NOx conversion across a broad temperature range without using separate catalysts.
A hydrogen-rich, oxygen-poor plasma chamber breaks fluorine- and nitrogen-containing gases while keeping NOx below 200 ppm.
An iron-exchanged high-purity Nu-86 zeolite improves NOx and N2O conversion while resisting inhibitor-driven catalyst deactivation.
A hydrogen-rich plasma flame breaks down fluorine- and nitrogen-based greenhouse gases while keeping NOx below 200 ppm.
Upstream and downstream oxygen sensing reveals N2O production in an ammonia slip catalyst, enabling reductant control to limit NH3 slip and emissions.
Upstream and downstream oxygen data reveals N2O-producing ammonia slip catalyst conditions and supports reductant control to limit NH3 slip.
Alkali-doped non-stoichiometric cobalt spinel uses oxygen vacancies and mesoporosity to sustain high N2O conversion at lower temperatures.
A platinum-on-siliceous support paired with SCR catalysts cuts ammonia slip while improving nitrogen yield and limiting NOx and N2O byproducts.