The feasibility of producing distillate fuels (gasoline, diesel and av
iation fuels) from coal syncrude was determined. A syncrude from direc
t liquefaction of subbituminous coal was first deasphalted by ultrason
ic disaggregation in n-hexane, to reduce the heteroatom content. The o
il was then catalytically hydrogenated in a continuous hydroprocessing
unit at 450 degrees C and 10 MPa hydrogen pressure. The hydroprocesse
d oil was fractionated by vacuum distillation and the cuts obtained we
re characterized. The high aromaticity of the hydroprocessed oil neces
sitated a second hydrotreatment under conditions suitable for hydrogen
ation of aromatic structures. Deasphalting removed 39% of the N, 43% o
f the S and 47% of the O. The first hydrotreatment removed 99% of the
S, 87% of the N and 37% of the O, and increased the H/C ratio. The sec
ond hydrotreatment provided an important reduction in aromaticity, nec
essary to achieve certain fuel quality specifications.