The concept of two-stage riser (TSR) fluid catalytic cracking (FCC) was tes
ted in the laboratory. The goals were to improve product distribution and i
ncrease product yield. A series of FCC runs was carried out in a pilot unit
. At a similar conversion level, the results showed that the TSR FCC was be
tter than the one-stage riser (OSR). The yields of gasoline and light oil i
ncreased by 2-3% and 3-4%, respectively, and the gas decreased. The researc
h and motor octane numbers of gasoline from the TSR FCC were higher than th
ose from the OSR FCC by 2-3 and 1-2 units, respectively. Compared with the
one-stage FCC, the gasoline produced from the TSR FCC contains less alkene
and more iso-alkane. (C) 2001 Elsevier Science Ltd. All rights reserved.