Mo/SiO2-catalyzed dehydration converts 2-furamide to 2-furonitrile, addressing hazardous carbonyl chemistry and difficult process regeneration.
Multi-stage membranes and high- and low-pressure recycle loops remove CO2 and H2S while reducing compression energy.
Parallel screens and cross-flow channels distribute gas uniformly through a compact CO2 absorbent bed while reducing breathing resistance.
Metal-ion MOR zeolites target slow, energy-intensive capture from dilute humid air with desiccant-assisted regeneration near 100°C.
A co-current water wash removes chemical and particulate contaminants before amine treatment, reducing foaming and fouling in sour-gas sweetening.
Baffle reversal separates mixed flow and uses centrifugal force to bring contaminated-gas microparticles into contact with decontamination solution.
Compressed and buffered hydrogen or ammonia waste gases drive variable-speed microturbines, recovering electricity instead of releasing or burning them.
Oxy-fuel combustion heats sequential reformers while recycling CO2-rich gases, integrating hydrogen production with carbon capture.
Quinone electroactive species reversibly bind Lewis acid gases as anion adducts, supporting selective separation even in the presence of dioxygen.
Heating air to at least 8000 K ionizes greenhouse gases, while superconducting magnets separate CO2 and CH4 for scalable removal.
An internal weir divides the chamber so immiscible fluids undergo co-current and countercurrent contact through separate flow paths.
MnOx/FeOx replaces V2O5/TiO2 in SCR, targeting high NOx conversion at 100–300°C in humid, SO2-exposed conditions.
A surge tank buffers PSA pressure changes and recycled methane flow, addressing bed pressure limits that reduce biogas methane recovery.
A porous barium MOF uses 17–19 Å molecular-honeycomb pores to capture CO₂ and convert it to cyclic carbonates through nine cycles.
Fe, Co, or Ni supported by ceria and alumina promotes H2S oxidative cracking while limiting sintering at high temperature.