CO2 hydrogenation has been performed on a Pt-Ca/C catalyst. In a previ
ous TPR study, this sample has shown the highest activity among differ
ent carbon supported platinum catalysts. In the present work the Pt-Ca
/C catalyst is tested in isothermal experiments (between 473 and 573 K
) at pressures of 0.1, 1 and 2 MPa. The obtained results allow a compa
rison with other catalytic systems that reveals the high activity of t
his catalyst to hydrogenate CO2 and the positive effect of the Pt-Ca c
ombination. This catalyst, however, presents a high selectivity to CO2
that does not change with increasing pressure. To complete the study
of the reaction (CO2 hydrogenation) on the Pt-Ca/C catalyst, some kine
tic data, like the reaction order and the activation energy, have also
been calculated. The activation energy obtained in this study is 82 k
J/mol; the reaction orders for H-2 and for CO2 are very similar and th
ey vary between 0.24 and 0.47 depending on the reaction conditions.