See how multi-stage heat pump compression with intermediate cooling upgrades low-temperature he
See how a partition wall with high emissivity treatment and thermally conductive fill isolates
See how non-linear fluid channels in stacked thermal contact spread heat and recuperate energy
See how solar absorbers convert sunlight to heat for steam-methane reforming, reducing CO2 emis
See how an alumina-zirconia ceramic tube bundle reactor withstands 600–1800°C with optimized su
See how arranging multiple hydrogen-occluding elements between paired heaters reduces the heate
See how a moving reactor train uses radiative heat exchange between zones to achieve 75-80% sol
See how removable solid medium blocks enable continuous solar hydrogen production while reducin
See how nitrogen injection restores mass flow rate and crossover temperature in steam cracking
See how a two-section furnace transforms aluminium wire into particles and oxidizes them in ste
See how a reaction chamber uses direct magma heat transfer to eliminate electricity conversion
See how porous carbon fibrils capture pyrolysis carbon black to heal defects, boost tensile str
See how ferromagnetic hydrogen storage materials generate heat through magnetic hysteresis, eli
See how direct magma heat coupling eliminates electricity conversion losses in thermochemical r
See how serpentine fluid channels distribute concentrated solar flux across reactor volume to r
See how a three-dimensional conductive network uses electrical resistance heating to preheat pr
See how non-catalytic reforming of methane with CO2 at high temperature avoids catalyst poisoni
See how through-holes and endothermic functional groups accelerate moisture evaporation to enha
See how densified textile aggregates co-fed with fossil fuel reduce tar yield and syngas variab
See how aluminum wire is converted to particles and oxidized in steam to achieve high energy de
See how serpentine fluid channels distribute thermal load to reduce hot spots and extend reacto
See how combining multiple sub-processes adjusts syngas CO/H₂ ratio without catalyst poisoning
See how non-catalytic thermal reforming of CO2 and methane eliminates catalyst poisoning, enabl
See how an electrochemical hydrogen compressor replaces vapor compression to eliminate moisture
See how exothermic methanation reaction heat drives endothermic dehydrogenation to produce hydr
Segmented serpentine cooling keeps metal hydride near heat-transfer surfaces, enabling faster hydrogen refueling under high pressure.
Scissor baffles and internal heating elements create serpentine counter-flow gas heating in one compact vessel, cutting space and equipment cost.
An integrated pressure vessel combines preheating, expansion, superheating, and condensate removal to deliver dry turbine fuel gas in less space.
Multiple syngas sub-processes are combined to tune the CO/H2 ratio directly, avoiding cryogenic separation and catalyst poisoning.
Recycled fuel cell anode exhaust adds CO2 to a steam reformer, raising CO content and delivering syngas near the 2:1 H2/CO ratio for liquid fuels.
Dual-side gas flow around a tubular reformer increases heat transfer area, improving thermal efficiency and temperature uniformity.
Chemical discharge extracts lithium from used battery electrodes, then anti-solvent crystallization recovers high-purity materials with lower energy use.
Nickel-alloy outlet piping and controlled ammonia cracking temperature limit nitridation corrosion while sustaining hydrogen purity and efficiency.
A molten carbonate fuel cell converts CO2 and hydrogen streams into electricity while separating a high-purity CO2 output for hydrocarbon facilities.
Mixed aluminum, iron, or copper MOFs use sacrificial coordination bonds to remove sulfur from moist fluids without structural degradation.
Water vapor flow is adjusted to recycle-gas CO2 flow, improving reforming efficiency and reducing steam-generation energy use.
By coupling a combustion unit with dehydrogenation and reforming reactors, this module stabilizes hydrogen supply despite heat fluctuations.
Hydrogen fuel cells, solid oxide fuel cells, and methane pyrolysis cut diesel refueling, fuel use, and emissions in oilfield equipment.
A hydrogen storage alloy in alkaline electrolyte stores and releases hydrogen at normal conditions, avoiding compression and cryogenic transport.
Metallic microwave plasma reactors avoid dielectric degradation and solid deposits while sustaining stable high-pressure, high-flow plasma processing.
Encapsulated PCM dispersed in metal hydride stores and releases reaction heat, simplifying hydrogen storage thermal management and hardware.
Temperature changes across a reforming catalyst reveal fuel poisons early, helping protect solid oxide fuel cells and maintain efficiency.
Captured CO2 from DME reforming is purified for greenhouse use while hydrogen feeds a fuel cell to supply cleaner farm power.
A phase change material buffers heat to an LOHC dehydrogenation reactor, enabling faster warm-up while limiting hot zones and temperature drift.
Preheating water and smoothing steam pressure help this fuel cell steam generator deliver uniform reformer steam and limit carbon formation.
Sequential CPOx, oxygen removal, and reforming stages let SOFCs use peak shaving gas while limiting coking and catalyst deactivation.
Ventilating air from the fuel cell housing is routed into the reformer to flare leaked hydrogen and avoid hazardous zones.
An offset reformer layout and guided airflow improve section heating, stabilize steam reforming, and raise fuel cell power generation efficiency.
Outlet temperature shifts in a reformation catalyst expose sulfur or phosphorous fuel poisoning before it damages fuel cell components.
CO2 from natural gas reforming is captured into carbonate reactants, reused for hydrogen electrolysis, and paired with fuel-cell power generation.
Charged porous carbon particles in a slurry electrode store hydrogen compactly, improving round-trip energy use and enabling electricity or pure H2 output.
A pincer catalyst and ionic liquid enable LOHC hydrogen release below typical dehydrogenation temperatures, improving PEM fuel cell compatibility.
Theta-phase Al2O3 with low platinum and an auxiliary metal sustains high hydrogen conversion at high space velocity while cutting noble metal use.
Methane pyrolysis supplies hydrogen for fuel cells or engines, cutting oilfield diesel use while co-producing solid carbon instead of CO2.
Dual gas paths heat the tubular reformer from inner and outer sides, expanding heat transfer area and improving thermal efficiency.
A blended LOHC feed and fuel-cell heating approach generates hydrogen and electricity with net-zero carbon emissions without extra storage.
Heat exchange between combustion-heated air and reformed fuel gas reduces stack inlet temperature deviation, improving fuel cell stability.
Captures natural gas pressure letdown energy with a pipeline turboexpander and uses it to power water electrolysis for hydrogen production.
Rapid cooling and heat treatment refine grain boundaries in a Ti-Zr-Cr-Mn-Ni hydrogen-absorbing alloy to raise discharge capacity without rare earths or high Co.
A fuel cell and GRU recover CO2, steam, and power to drive catalytic reforming for methanol feedstocks with near zero GHG emissions.
Direct water injection into the anode exhaust recycle stream replaces bulky steam generators, cutting fuel cell humidification size and response time.
Direct water injection into the anode exhaust recycle stream replaces bulky steam generation, cutting fuel cell system size, complexity, and lag.
Sensor-based catalyst monitoring adjusts hydrogen production load in time to preserve gas quality within ISO standards.
A tailored iridium complex catalyst dehydrogenates concentrated formic acid at lower temperature while suppressing carbon monoxide and maintaining durability.
Alternating electromagnetic fields heat reactor walls directly, cutting external heat-transfer losses, reactor volume, and energy waste.
Ferrovanadium-modified TiMn and TiCrMn alloys cut hysteresis and improve hydrogen release kinetics at moderate temperature and pressure.
Branch tubes inside the SOFC manifold combine heat exchange and catalytic ammonia reforming, cutting reactor volume and system cost.
Preheating water and evaporating it in a coil tube helps deliver uniform steam to a fuel reformer and prevent carbon damage to fuel cell electrodes.
Condensed water cools the WGSR and humidifies recycled CO2, cutting carbon deposition while improving fuel cell exhaust reuse.
A dual-chamber microwave reactor converts sinusoidal energy to a radial wave to ignite stable plasma and limit constriction and contamination.
Feedback control adjusts fuel, water, and air flow from hydrogen output changes to keep reformer temperature and generation stable.
A hydrogen storage alloy dispersed in alkaline electrolyte enables normal-pressure hydrogen transport with fluidity and more precise release control.
A sealed electrochemical hydrogen cell stores and releases H2 at ambient conditions, avoiding self-discharge and high-pressure storage.
Captured CO2 and methane are converted into methanol to power wellbore equipment with lower emissions, lower energy demand, and safer fuel handling.
Acid treatment removes bismuth-ruthenium oxide by-products that trigger dendritic growth, stabilizing discharge capacity and battery life.
Recirculated hot anode off-gas evaporates atomized fuel in one mixing chamber, cutting SOFC plant complexity and improving load response.
A recyclable LOHC releases purified hydrogen for fuel-cell power while avoiding high-pressure storage and using carbon-neutral heat for dehydrogenation.
Mixed N-heterocycloalkyl hydrogen carriers enable lower-temperature hydrogen release and keep by-products liquid for easier discharge.
A four-phase molten salt reactor limits wall coke deposition while enabling lower-temperature methane pyrolysis and cleaner hydrogen-carbon separation.
A twisted porous metal catalyst support increases gas-solid reaction efficiency while keeping pressure loss low in methanation and reforming.
Alkali and alkaline earth metal catalysts capture CO2 and convert it to CO with high selectivity while cutting catalyst cost and energy use.
Forced circulation maintains threshold coke density, directing carbon onto circulating particles instead of reactor surfaces.