Catalytic hydrocracking of a residue from deasphalting a syncrude obta
ined by direct coal liquefaction of a subbituminous Spanish coal was c
arried out at different temperatures and reaction times. Kinetic study
of the cracking reaction has been performed. The viscosity, coke cont
ent, boiling point distribution, elemental analysis, and aromaticity o
f the reaction products have been determined. The experimental data fi
t with the first-order kinetic model proposed. The main effects observ
ed with the thermal hydrotreatment have been a large decrease of the v
iscosity of products that varies from 4608 cSt in the feedstock to 79
cSt. The conversion of the heavy fraction (bp > 350 degrees C and solu
ble in toluene) increased with the temperature and residence time, and
the formation of coke was inhibited even at the softest reaction cond
itions used.