Technical
and economical evaluations were carried out for upgrading
of heavy crude oil by a combined scheme of deasphalting and hydrotreating.
Deasphalted oil was obtained at 60 °C temperature, 25 kgf/cm2 pressure, 5:1 solvent/oil ratio, and 1 h residence time,
using n-heptane as the solvent. The deasphalted oil
product was upgraded by means of hydrotreating at low severity reaction
conditions: 360 °C temperature, 60 kgf/cm2 pressure,
and 4 h reaction time. The technical and economic analyses demonstrated
that the upgrading scheme is an appropriate option for producing transportable
oil.