A bimodal porous dealkylation catalyst resolves low conversion rates and high energy consumption by selectively dealkylating C9+ aromatics at lower temperatures.
Steam mediates demethoxylation of alkylmethoxyphenols using MoP/SiO2 and HZSM-5 catalysts, avoiding coke formation and dehydroxylation.
Uniform hydrogenation metal distribution in hydroalkylation catalysts enhances benzene conversion and cyclohexylbenzene selectivity.
Lewis acids mediate DMF cycloaddition to para-xylene, minimizing 2,5-hexanedione byproducts for higher yields.
Refractory coatings reduce carbon uptake on reactor surfaces, preventing carburization during high-temperature methane conversion.
Replacing toxic benzyl trimethyl quaternary ammonium ions with low-cost choline cations reduces synthesis costs while maintaining crystal quality.
A segmented catalyst system combines methanol synthesis and dehydration layers to produce dimethyl ether from synthesis gas.
Separate gas distributors control mass transfer to prevent rapid methanol consumption, boosting benzene conversion above 40%.
Acidic solid pretreatment converts ethanol feedstock to diethyl ether, protecting zeolitic catalysts from nitrogen impurities and extending operational life.
Staged fluidized bed reactor converts oxygenates to hydrocarbons, increasing gasoline yield without alkylation units.