A multistage liquefaction scheme consisting of coal pretreatment, solv
ent-mediated hydrogen-transfer dissolution, and catalytic hydrocrackin
g steps was proposed in order to achieve the highest oil yields with c
omplete conversion of organic components in coal and-to enable the rec
overy and repeated use of the catalyst with its least deactivation. Th
e deashing pretreatment enhanced the depolymerization of coal macromol
ecules through the removal of bridging ion-exchangeable cations as wel
l as the better contact of donor solvent with coal macromolecules. The
highest oil plus asphaltene yield of ca. 75% was obtained through the
two-step liquefaction of acid-treated Morwell coal by the reactions o
f noncatalytic hydrogen transfer (donor solvent: tetrahydrofluoranthen
e, solvent/coal = 1) at 430 degrees C-2 min in the first step and the
following catalytic hydrogenation with a pyrite catalyst at 400 degree
s C-20 min. The multistep liquefaction scheme is discussed in terms of
the highest efficiency of utilization of solvent and catalyst at the
respective step. Two types of recoverable catalysts were investigated
to allow repeated use of the;catalyst in the primary liquefaction. The
first type was an acid-proof iron catalyst which was recoverable from
:a mixture with residual carbonates and chlorides that are soluble in
acids. Such a catalyst was applicable to particular coals; such as an
Australian brown coal which is completely liquefied,leaving calcium an
d magnesium carbonates as the major residual minerals after the primar
y liquefaction. The second type was characterized by its sulfur-proof
ferromagnetism for the recovery from the minerals and carbons by gradi
ent magnetic field. Fe3Al powder and carbon/ferrite composite catalyst
s were found to maintain their ferromagnetism after the sulfiding to b
e fairly active in the liquefaction of the brown coal. Procedures for
activation, recovery, and repeated use of these recoverable catalysts
were preliminarily examined.