This work studies the influence of Fe, Fe-Mo, Co-Mo, and Ni-Mo catalys
ts on the coprocessing of a Lignite from the Bergueda (Catalonia, Spai
n) with a vacuum residue of petroleum. Given the high mineral matter c
ontent of this Lignite, it was demineralized to prevent any interferen
ce with the catalyst performance. A set of supported Fe-based catalyst
s as well as two commercial hydroprocessing catalysts were tested. The
experimental results show that coal conversion increases with all cat
alysts, although those containing molybdenum yield the largest values
(50-60%). The percentage of iron in the catalyst does not have a stron
g influence on this conversion, suggesting functional problems. Signif
icantly high coal conversions are also obtained in experiments with al
umina (approximate to 40%) or without catalyst (approximate to 44%), s
uggesting that the demineralization process causes fragmentation of th
e coal structure. The production of oils is larger with the Mo-based c
atalysts (19-25%) and on the order of 8% for the Fe-based catalysts.