Real-time waste composition sensing adjusts plasma temperature and timing to cut energy use while converting mixed solid waste into hydrocarbon gas.
A cyclonic oxidation reactor combines oxidation and gas-solid separation to shrink CLC plant size, cut capex, and support CO2 capture.
Multiple reduced-pressure gas-laden feedstock streams improve reactor distribution and pressure maintenance during carbonaceous gasification.
Dual buffer tanks and a repurposed gas supply maintain powder hopper pressure when one tank is unavailable, while differential pressure reveals filter damage.
Hollow fiber membranes selectively permeate oxygen to react with biomass, producing syngas for hydrogen generation.
Stationary gas distributors enable flexible operation across drying, pyrolysis, and combustion without physical alteration.
Using a CO2 transport gas with a specific weight ratio reduces oxygen consumption and minimizes downstream separation burdens.
A two-stage bio-reforming reactor system processes raw syngas and recycle streams to produce chemical-grade bio-syngas.
Continuous biochar production merges cooling, magnetic separation, and screening to resolve trade-offs between purity and throughput.
Segmented oxygen zones minimize solid ash carbon content while maintaining a high CO/CO2 molar ratio in the produced syngas.
A gas conversion device uses a silo to continuously replenish a solid reactant bed via gravity for uninterrupted plasma processing.
A feed injector outer tube tip uses ceramic matrix composite material to withstand extreme thermal environments.
A side feed gasifier with a centre ash dump and refractory lining.
Heated granular material mixes with biogenic feedstock inside a pressure vessel to initiate gasification and produce hydrogen.
Recycled CO2 pressurizes a sluice vessel while carbonaceous feed absorbs methanol, eliminating expensive absorbers and meeting vent regulations.
A hydrous pyrolysis process filters synthesis gas streams using C-O-H compounds to remove tars and particulates for direct energy utilization.
Replacing expensive coke with spent pot liner bricks reduces fossil fuel consumption while maintaining bed strength through cement binders.
A rotary steel tube with helicoids moves ashes through a reactor coated with alumina refractory material.
A waste gasification reactor converts diverse refuse into synthesis gas through integrated thermal processing.
A flow splitter divides fuel mixture streams using specific tube diameters to ensure uniform distribution.
Diluting hydrogen streams with nitrogen from adsorption regeneration before combustion reduces waste and improves efficiency.
Heat pipes transfer thermal energy between partitioned reaction zones, resolving the trade-off between processing efficiency and system complexity.