Two series of silica-and alumina-supported platinum catalysts were investigated in the hydrodechlorination (HdCl) of tetrachloromethane. During an initial period of reaction carried out at a lower H 2 /CCl 4 ratio the catalysts, especially those characterized by high metal dispersion, deactivated with time-on-stream. Two catalyst screening protocols were used. The first one concerned a gradually increased hydrogen partial pressure, whereas during the second one the H 2 pressure was decreased. Although, in general, the hydrogen-rich reaction conditions resulted in improved catalyst performance (higher overall activity and selectivity to CHCl 3 ), the second protocol led to even better results. Reasons for such a behaviour are suggested. Because of very high activity of a few tested samples, changes in CCl 4 conversion with the hydrogen partial pressure do not reflect real reaction orders in hydrogen. The same reason may lead to falsification of apparent activation energies. In certain cases the relation between conversion and hydrogen pressure showed a maximum, suggesting that HdCl undergoes via a Langmuir-Hinshelwood mechanism, when hydrogen and CCl 4 compete for metal surface sites. Both carbon-and chlorinecontaining deposits were found in the post-reaction catalyst samples.Keywords CCl 4 Á Hydrodechlorination Á Platinum catalysts Á Alumina Á Silica Á Effect of metal dispersion Á Effect of hydrogen pressure, activation energy