Metal-bearing compounds convert halogens to oxidize mercury, preventing SCR catalyst deactivation and extending service life.
A gasification reactor uses microwave dielectric heating to drive the water-gas shift reaction for efficient dihydrogen production.
A reactively-driven oxygen transport membrane system performs primary and secondary reforming to produce synthesis gas.
Nickel-modified red mud catalysts enhance acidity and methane conversion rates while suppressing coke formation through composite material synergies.
A rocket-style impinging injector mixes reactants in a fluidized bed reactor using high-velocity streams.
Merging water-gas shift and catalytic oxidation into one pressure vessel reduces pipe complexity and energy losses in naval platforms.
Electrolytically generated hydrogen enriches sulfur-free hydrocarbon streams before autothermal reforming to produce synthesis gas.
Adjusting hydrocarbon feed flow stabilizes oxygen transport membrane reactor temperature, preventing thermal runaway during syngas production.
A pressure equalizing part connects a gasification furnace to an annulus section at a high temperature region.
A mesoporous alumina catalyst features a metal oxide coating layer that protects active sites from oxidation and aggregation during synthesis gas production.
A ruthenium catalyst on lanthanum-cerium-zirconium oxide support enables selective carbon monoxide methanization.
An integrated device melts magnesium and atomizes droplets into uniform powder for hydrogenation.
Sulfided platinum-iron catalysts remove carbon monoxide from hydrogen-rich streams at low temperatures, preventing fuel cell poisoning.
Recycling pressure swing adsorber residuals reduces capital expenditure on pipeline systems while maintaining plant efficiency.
Solid-phase synthesis creates spinel carriers with large specific surface area to resolve small reaction areas in ammonia decomposition.
A nickel ruthenium catalyst composition drives dry reforming reactions to produce syngas with high conversion efficiency.
A process plant generates pure and process steam streams from a single PC-boiler to supply shift conversion units.
A polyester base polymer with less than 40 ppm phosphorous incorporates a non-polymeric oxidizable organic compound and transition metal catalyst.
Segmented microwave plasma sources scale production volume without enlarging single device size or increasing electromagnetic interference.
Bulk alumina support allows sulfur-tolerant reforming catalyst to maintain activity despite feed contamination, eliminating costly sulfur removal processes.
Integrating oxidative coupling with hydroformylation eliminates costly separation steps while optimizing the syngas ratio for higher propanal yield.
Converting harmful carbon dioxide emissions into methanol feedstock, eliminating costly sequestration and preventing atmospheric release.