In
this work we used the vacuum distillation residue from an Iranian
heavy crude oil refinery in a solvent deasphalting (SDA) process using
different temperatures (60–120 °C), pressures (5–9
bar), solvents (n-pentane and ethyl acetate), and
solvent to feed ratios (3 to 1, 5 to 1, and 7 to 1). The resulting
products included deasphalted oil (DAO) and residue (PITCH). The DAO
yields in SDA when n-pentane was used as solvent
were significantly higher than those when ethyl acetate was used as
solvent. The DAO was subsequently processed by thermal cracking at
500 °C and atmospheric pressure to investigate the effect of
solvent deasphalting processing conditions on the yield of coke and
liquid products as well as the metal and sulfur content of the produced
coke. The results indicated that SDA effectively removed up to 45%
of vanadium and up to 40% of nickel from the vacuum residue. Simulated
distillation (SimDis) results of the liquid products of thermal cracking
of DAO indicated that for both n-pentane and ethyl
acetate as the SDA solvent, an increase in the solvent to feed ratio
resulted in increased amount of lighter compounds (C5–C20) of the liquid products.