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Static bifurcation in a FCC unit is a problem that arises whenever studying the control of a FCC unit.
The FCC unit is operated in the steady state.
30 ~ 50 wt% gasoline can be produced in FCC unit.
System I processes LCO component in hydro-treating and FCC unit, requiring two individual FCC unit and 1 hydro-treating unit.
Dushanzi Petrochemical Company's I FCC Unit is a high low parataxis riser wax oil FCC Unit with processing capacity of 0.8Mt/a.
However, none of these studies have considered a FCC unit with high efficiency regenerator.
The proposed design is tested using a non-linear simulation of the FCC unit model.
Two industrial systems are studied by simulation: styrene polymerization reactor and fluid catalytic cracking (FCC) unit.
Based on the mechanistic model of a FCC unit, a non linear controller is designed.
The proposed design is tested using a nonlinear simulation of the FCC unit model.
A dynamic real-time optimisation study of a FCC unit was carried out [10].
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