Direct Heating Destructive Distillation TRIZ Cases

Electrolysis adds hydrogen and oxygen to biomass gasification, improving syngas H2/CO ratio while reducing excess CO2 in renewable fuel production.

Plastic waste is sized, mixed into coker feed, and processed in existing cokers to raise liquid yield while limiting coke formation.

Alternating retort surfaces and zoned crossflow steam maintain pyrolysis temperature gradients, improving shale oil yield with lower energy use.

A zigzag multi-stage furnace and stable molten salt flow enable continuous plastic waste pyrolysis with more uniform heating and less clogging.

Alternating flighted augers and paddles keep high-ash biomass moving through reaction and cooling zones to limit crusting and produce consistent biochar.

Recycling part of the produced syngas back upstream cuts oxygen and CO2 demand while improving carbon conversion and cold gas efficiency.

Bottom-fed hot gas starts torrefaction before grinding, improving biomass fineness and reducing downstream comminution energy.

Fluidized-bed heat treatment and magnetic separation turn iron compounds in lignite into magnetic forms, lowering iron in silicon reductants.

Temperature, pressure, flowrate, and oxygen sensors adjust heated fumes and inert gas to limit uncontrolled combustion and improve pyrolysis uniformity.

Using oxygen with less than 10% nitrogen and CO2 dilution, porous-media oxidation creates uniform heat without NOx.

Vibrating conveyance and ceramic heating elements address obstructions while integrated reactors improve hydrogen recovery.

A rounded-corner retort uses crossflow steam and staged temperatures to improve shale movement, heat transfer, and pyrolysis efficiency.

Mild acidic catalyst converts plastic waste into hydrocarbon wax, reducing soot and impurities without extra cleaning.

A circulation gasification furnace design extracts solid residue via a dedicated discharge section to maintain material utilization efficiency.

Cement lining in the reactor vessel enables simultaneous high-efficiency syngas production and significant biochar yield generation.

A mobile pyrolysis reactor circulates syngas through woodchips and biochar to filter impurities.

Electromagnets control ferrous element release to break char, reducing processing time while maintaining energy recovery.

Rapid thermal fracturing separates volatile matter from coal in an oxygen-depleted zone, reducing processing time and impurities.

High temperature pyrolysis of coked oil sands generates syngas while heat recycling reduces energy consumption, eliminating large waste ponds and CO2 emissions.

A molten aluminum alloy bath breaks down coal into elemental components during gasification.

Rapid-heating coking coal in a fluidized bed improves caking properties, enabling high-strength coke production with non-coking coals.

A retort system processes coal in an oxygen-free environment to vaporize toxins and produce cleaner char.

Multi-channel gas distribution creates zoned temperature control in the reactor, preventing caking middling coal swelling and semi-coke clumping.

Thermal screw conveyor pre-dries carbon waste using recovered heat, preventing sticky ash formation and enabling continuous operation.

A retort chamber isolates organic and inorganic materials through controlled thermal depolymerization.

Continuous coal reformer extracts volatile matter through vertical vapor draws while maintaining a specific temperature gradient.

Segmented reactors produce high-heating-value gas to substitute primary fossil fuels in cement rotary ovens.

A thermolysis reactor equipped with dual mixers and vertical baffles processes waste plastics into solvents, oils, and waxes.

A multipurpose coke plant blends Indiana coal to produce high-quality coke and pyrolysis gas for synthetic fuel generation.

Zoned heat exchange in a shale pyrolysis retort reduces production costs by optimizing energy use and accommodating nonuniform particle sizes.

Reprocesses CO2 exhaust with organic mass to produce pyrolysis gases, reducing fossil fuel consumption in calcination.

Serial rotary kilns transfer hot waste rock char between streams to preheat disparate carbonaceous feedstocks.

A catalytic conversion unit treats recirculated fluidization gas to lower oxygen levels before entering the thermal reactor.

Partial oxidation reformer converts methane to CO and H2, resolving high energy input trade-offs in indirect gasification bioconversion.