Hydrocracking of phenanthrene was studied in a fixed bed continuous flow reactor under 60 bar total pressure using a bifunctional catalyst constituted of Pt deposited on silica-alumina. GC-MS analysis was utilised in order to identify the numerous products formed during phenanthrene hydrocracking. Following a kinetic study, a reaction pathway was proposed based on a multi-step mechanism: hydrogenation of aromatic rings, isomerisation and cracking of naphtenic rings, and rearrangements. Reaction temperature showed a great effect in terms of selectivity and catalysts comparison was therefore done at a temperature of 300 degreesC. Three bifunctional catalysts: platinum supported on silica-alumina, on H-Y zeolite and on H-beta zeolite were compared in terms of activity and selectivity A close examination of product distribution indicated that the major contributing factor was the pore structure of the support. Zeolite structures favoured overcracking because of the numerous collisions with acid sites that perhydrophenanthrene could undergo during its diffusion.