Segregating light and heavy feeds into independent risers resolves heat balance constraints while boosting olefin production.
A hydrocracking catalyst uses a carbonaceous substance to balance activity and suppress excessive cracking.
Introducing carbon monoxide into the riser reactor reduces sulfur content by over 50% without hydrotreating capital costs or octane loss.
A supported chromium II catalyst converts alkane reactants into lower and higher molecular weight aliphatic hydrocarbons.
Passing electric current through conductive particles heats the fluidized bed to 500-850°C for catalytic cracking.
Magnesium-modified ultra-stable rare earth Y zeolite resolves ammonium nitrogen pollution by replacing conventional salts with dispersing pre-exchange.
Magnesium-aluminum mixed metal oxide additives capture iron, nickel, and vanadium to protect fluid catalytic cracking catalysts from deactivation.
Oligomerization system with FCC zone cracks distillate to propylene using controlled branching and boiling points.
Converts FCC olefins to heavier compounds via oligomerization, resolving separation difficulty from refractory paraffins in recycle streams.