Three methods of preparing catalysts for direct coal liquefaction (DCL
) are presented, using ferric sulfide as a precursor. Of these, one in
volves the physical mixing of the coal and the supercritically dried c
atalyst, and the other two involve impregnation of the catalyst in the
coal. In one of the latter two, the catalyst is prepared in situ as w
ell. The in situ impregnated sample (IIS) of catalyst plus coal result
s in a high level of coal conversion. The nominal loading of the catal
yst is 1.67 wt%, but even lower loadings, <0.5 wt%, show significant i
mprovements in activity and oil yield relative to uncatalysed DCL. For
DCL using the IIS catalyst, a solvent with negligible hydrogen-donati
ng and shuttling abilities can be used; a more active solvent, with gr
eater ability to donate and shuttle hydrogen from the gas phase to the
coal, results in only a slight improvement in activity and oil yield.
Hence the IIS approach appears to be an efficient method of catalyst
introduction for carrying out catalytic DCL.