Fuel cell exhaust CO2, water, and heat are reused in methane reforming to cut energy use and enable near-zero-GHG syngas production.
Fuel cell exhaust CO2 and water are reformed with natural gas into syngas and methanol while using cell heat and power to cut emissions.
Uses transition alumina pore control to create alpha-alumina supports with high pore volume for silver impregnation and lower secondary reactions.
A supported organometallic catalyst enables terminal C-H functionalization of hydrocarbons and polyolefins without chain cleavage or cross-linking.
Non-thermal DBD plasma with a liquid ground electrode converts CO2 and C1-C4 hydrocarbons to oxygenates at low temperature without extra heating.
High-pressure flooded vessels and partial oxygen desorption cut flammable gas risk while recycling propene in 1,2-propanediol production.
An extractant phase recovers tungstate and phase transfer catalyst before distillation, cutting catalyst loss in 1,2-propanediol production.
Liquid CO2 enables near-ambient PAH ozonolysis that adds oxygen functional groups while minimizing combustion and energetic intermediates.
A palladium-treated aqueous phase decomposes formic acid before distillation, reducing corrosion during 1,2-propanediol recovery.
UV-visible irradiation reduces supported chromium catalysts to convert hydrocarbons into alcohols and carbonyls under milder, halogen-free conditions.
A dual-catalyst route uses in situ oxidants from CO2 hydrogenation to raise methane-to-methanol conversion and selectivity under milder conditions.
A two-phase propene and hydrogen peroxide route raises propylene oxide output without expanding the main reactor, while cutting separation energy.
A continuous milli-reactor Grignard step raises triptane yield and suppresses side reactions in multi-step fuel synthesis.
Catalytic osmate (VI) dihydroxylation with amine N-oxide reoxidants cuts waste and toxicity while delivering high-yield cis-diols.