Two-stage regeneration with controlled oxygen partial pressure converts petroleum coke byproduct into valuable syngas.
Optimized pore architecture resolves the trade-off between catalytic activity and selectivity in hydrocracking processes.
Phosphorous modified sub-micron ZSM-5 zeolite increases propylene yields while maintaining gasoline output in fluid catalytic cracking.
Segmenting hydrocarbon feed into gasoline and cycle oil fractions allows optimized aromatic ring opening to boost BTX yield beyond theoretical limits.
Segmenting feedstock introduction suppresses pipe vibration while maintaining efficient heat recovery in aromatic production.
Differential pressure gauges monitor filter pressure differentials in fluidized catalytic cracking units to detect blockages and reduce problem detection time.
Integrating an FCC unit with an aromatic complex recycles coking cuts to preheat feedstock, resolving heat balance deficits from low coke production.