Thermal Non-Catalytic Cracking TRIZ Cases

A dual-reactor HSFCC flow boosts crude-to-olefin conversion by combining separation, C4 processing, steam cracking, and naphtha reforming.

An endothermic fuel processor uses waste heat to cool a load while converting raw fuel into processed fuel for electricity generation.

Waste plastic-derived paraxylene is purified through staged conversion to produce high-purity recycled DMT using existing chemical facilities.

Separating crude into light, medium, and heavy cuts enables low-pressure hydrotreating and flexible steam cracking with ULSD output and slower coking.

Waste plastic pyrolysis vapor is integrated with distillation and steam cracking to produce high-purity recycled-content paraxylene.

Pyrolysis vapor and residue from waste plastic are fed to an FCC unit to produce high-purity paraxylene with recycled content.

Solvent liquefaction and dehalogenation let waste plastic run through FCC units to produce high-purity recycled para-xylene.

Oxygen in a molten salt matrix enables catalyst-free hydrocarbon cracking with internal heat generation, lower CO2 emissions, and cleaner olefin streams.

High-purity recycled paraxylene from waste plastic is purified and fed into existing TPA lines to produce r-PTA and r-PET with lower fossil feed reliance.

Recycling non-jet-range oligomerized olefins through steamcracking boosts jet-range yield and reduces oxygenate carbon loss and cost.

Char from biomass pyrolysis is gasified in a fluidized bed to supply heat, produce syngas, and fit existing refinery processing.