A Spanish subbituminous coal has been processed in two-stage liquefact
ion in a non-integrated process. The first-stage coal liquefaction has
been carried out in a continuous pilot plant in Germany at Clausthal
Technical University at 400-degrees-C of temperature, 20 MPa hydrogen
pressure and anthracene oil as solvent. The second-stage coal liquefac
tion has been performed in continuous operation in a hydroprocessing u
nit at the Instituto de Carboquimica at 450-degrees-C and 10 MPa hydro
gen pressure, with two commercial catalysts: Harshaw HT-400E (Co-Mo/Al
2O3) and HT-500E (Ni-Mo/Al2O3). The total conversion for the first-sta
ge coal liquefaction was 75.41 wt% (coal d.a.f), being 3.79 wt% gases,
2.58 wt% primary condensate and 69.04 wt% heavy liquids. The heteroat
oms removal for the second-stage liquefaction was 97-99 wt% of S, 85-8
7 wt% of N and 93-100 wt% of 0. The hydroprocessed liquids have about
70% of compounds with boiling point below 350-degrees-C, and meet the
sulphur and nitrogen specifications for refinery feedstocks. Liquids f
rom two-stage coal liquefaction have been distilled, and the naphtha,
kerosene and diesel fractions obtained have been characterized.