A reactor burner block uses a secondary space and distributor ring to introduce auxiliary oxygen homogeneously across the firing zone.
Oxygen injection into a catalyst bed converts tars and hydrocarbons, preventing PAH formation and simplifying the apparatus.
A reactor agitator circulates biogenic mass during drying to prevent solidification and ensure consistent dry substance output.
A metal component with a nanoleaf surface structure catalyzes water and carbon dioxide conversion to hydrogen gas, suppressing carbon monoxide production.
Segmented mixing apparatus vaporizes liquid fuel via heat transfer before combining it with oxygen gas, resolving uniformity and pressure drop contradictions.
A hydrogen-absorbing alloy with 20 mole percent samarium reduces hysteresis between absorption and desorption pressures.
Soft oxidation converts methane to carbon disulfide using hydrogen sulfide, suppressing CO2 formation and improving C4+ yield.
A nickel-zinc desulphurisation material removes residual sulphur from hydrocarbon streams using a simplified single-calcination process.
Hydride battery utilizes hydrogen-absorbing alloy with 0.15 to 10 MPa plateau pressure to resolve low energy density trade-offs.
A perovskite oxide semiconductor absorbs visible light to decompose water into hydrogen and oxygen gases.
An endothermic reactor converts atmospheric heat and humidity into diatomic hydrogen and stoichiometric oxygen for fuel cell applications.
A single reactor catalytic process converts renewable lipids into hydrogen and hydrocarbons using metal sulfides encapsulated in sodalite cages.
An asymmetric baffle in the quench chamber removes entrained coolant from syngas, preventing re-entrainment and downstream equipment damage.
A palladium catalyst supported on cerium oxide enables selective partial oxidation of methane to synthesis gas at low temperatures.
A yolk-shell catalyst structure combines nickel and platinum with a porous ceramic shell to deliver high activity in dry reforming processes.
A regenerative liquid sorbent system circulates absorbent fluid through a membrane separator to capture air contaminants.
A gasification burner uses a retracted separating wall to create a gas exchange passage between coaxial channels.
Vertical fuel processor design integrates steam and shift reformers to resolve volume complexity trade-offs while improving thermal efficiency.
Integrated reformate heating drives multi-stage evaporation, resolving the trade-off between waste heat recovery and capital cost.
A liquid expansion system continuously depressurizes high-pressure slurry using an expansion turbine or reverse-flow centrifugal pump.
A rhodium-platinum catalyst supported on cerium-modified alumina enables stable hydrogen production from hydrocarbon feedstocks.
Confined reforming catalyst converts hydrocarbons to synthesis gas within the reduction zone of a chemical loop combustion reactor.
Supported iridium complexes merge homogeneous activity with heterogeneous stability, suppressing CO formation to enable efficient hydrogen generation.
Injecting methanol with in-situ generated carbon monoxide into heat treatment furnaces to produce precise hydrogen and carbon monoxide atmospheres.
Dissolved ruthenium catalyst in water-immiscible organic solvent enables continuous hydrogen release from aqueous formate.
A two-stage methane reforming process converts intermediate gas into solid carbon using a second catalyst reactor.
Nested cylindrical zones recover heat from the reaction chamber to preheat reagents, reducing thermomechanical stress and device complexity.
Partial dehydrogenation reduces reactor volume and flow tube length while maintaining sufficient hydrogen release rates for mobile applications.
Thermal treatment of the wet cake eliminates dewatering steps while utilizing sensible heat to enhance gasification efficiency.
A reactor coolant injector shifts synthesis gas H2:CO ratios by injecting cooling fluid near the reaction zone outlet.