FCC feedstock pretreatment was carried out in a bench-scale hydroprocessing unit at two seventies, reflecting hydrotreating (HT) and mild hydrocracking (MHC), with Ni-Mo/Al2O3 catalyst, followed by FCC experiments conducted in a microactivity test (MAT) unit. The severity of the treatment had a significant effect on long-term stability of catalytic cracking. The FCC conversion in the MHC operation declined faster than desulfurization or denitrogenation, due to the combined effect of deactivation in the polyaromatics-hydrogenation and in the denitrogenation functions. The change of FCC conversion was well expressed by the equation containing nitrogen and polyaromatics plus resin in the FCC feedstock.The combination of HT and FCC (HT-FCC) operation demonstrated an advantage of maximizing production of gasoline over MHC-FCC operation. In contrast, MHC-FCC operation showed an advantage of maximizing yield of middle distillate during the initial period, but this advantage became less gradually.
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