Directed reducing agent injection and staged agitation optimize flow index response consistency in chromium-based catalysts.
A bimodal mesoporous alumina catalyst enables selective hydrogenation of gasoline diolefins using specific pore volume distributions.
Cobalt-loaded carbon nanotubes replace expensive precious metals to lower catalyst costs while maintaining high hydrogen production rates.
Sequential alkylene oxide blocks activate double metal cyanide catalysts, preventing deactivation and maintaining high space time yields.
Alkaline aging reduces silica surface area to enable rapid thermal activation of chromium catalysts in large batches.
A nickel catalyst promoted with copper and sulfur achieves selective olefin hydrogenation while maintaining high activity.
A self-activating hydroprocessing catalyst uses a specific nickel-to-molybdenum ratio to enhance desulfurization activity over time.
A porous alumina carrier with controlled pore sizes enhances catalytic activity in hydroprocessing applications.
Dual calcination stabilizes nickel particles on alumina, resolving the activity versus stability trade-off in polyetheramine synthesis.
Segmenting catalyst particles by size in an ebullated bed reactor reduces sediment yield while maintaining hydrodesulfurization performance.
Modular LED fixtures with photocatalytic titanium dioxide coatings resolve heat dissipation limits while degrading air pollutants under visible light.
Alcohol-based solvothermal synthesis disperses ruthenium on cerium oxide, lowering reaction temperatures and energy costs while maintaining hydrogen purity.
Acoustic cavitation replaces complex multi-step thermal processes to synthesize high-performance porous multimetallic nanocrystals without templates.
Partial reduction of cobalt oxide at 220-250°C preserves C5+ selectivity while lowering energy consumption.
Washing the double metal cyanide catalyst with an aqueous polyether polyol solution increases carbon dioxide content while lowering the cyclic carbonate ratio.
Stepwise impregnation of sepiolite with tungsten, nickel, and molybdenum prevents metal interaction, achieving over 95% lignin conversion to 2-ethoxyphenol.
Copper dispersed in sub-stoichiometric spinel ceramic matrix prevents metal migration, extending particle lifespan and reducing attrition.
Reduced chromium catalysts adjust flow index response through controlled drying and oxidation state management.