A residue from deasphalting a syncrude obtained by direct coal liquefa
ction of a subbituminous Spanish coal was processed by thermal hydrotr
eatment. Kinetic study of the cracking reaction and coke formation rea
ction has been performed. The viscosity, coke content, boiling point d
istribution, elemental analysis, and aromaticity of the reaction produ
cts have been determined. The experimental data fits with the first-or
der kinetic model proposed. The main effects observed with the thermal
hydrotreatment have been a large decrease of the viscosity that varie
s from 4608 cSt in the feedstock to 147 cSt in the products. The conve
rsion of the heavy fraction (bp > 350 degrees C and soluble in toluene
) and asphaltenes increased with the temperature and residence time, a
nd the formation of coke was inhibited even at the hardest reaction co
nditions used. At 425 degrees C a kinetic control conducts the reactio
n, the cracking reaction with lower activation energy was more favorab
le and the coke formation (condensation) remained almost completely in
hibited.