Steam catalytic cracking is an alternative method to produce light tar fractions from coal tar. In this study, MnÀ Ce modified Fe 2 O 3 catalysts were prepared by impregnation method, and used for steam catalytic cracking of coal tar in a fixed-bed reactor at 550°C and atmospheric pressure. The results showed that the catalyst Fe80Mn15Ce5 (Fe/Mn/Ce mole ratio 80/15/5) exhibits the best performance in terms of highest light tar yield being 67.6 wt.%. Moreover, the decrease of weight hourly space velocity (WHSV) can further increase the pitch conversion and the light tar content. As a result, when the WHSV is 0.65 h À 1 , the light tar yield reaches 71.6 wt.% on Fe80Mn15Ce5. The structural variations of catalysts were characterized by several analytical techniques to reveal the improved catalytic performance. It is shown that the impregnation of MnO x improves the structural stability of Fe 2 O 3 due to the formation of FeÀ Mn solid solution, while the load of CeO x activates lattice oxygen. As a result, more active oxygen species generating from steam dissociation can participate in the catalytic upgrading of coal tar.