Detailed kinetic modeling of Pt/C catalyzed conversion of glycerol to lactic acid, glycols, and alcohols with in situ formed hydrogen is reported. Experimental concentration-time profiles were obtained in a batch slurry reactor at different glycerol concentrations, nitrogen partial pressures, and NaOH concentrations in a temperature range of 130-1608C. Six different kinetic models were evaluated to describe the competing dehydrogenation, hydrogenolysis, dehydration, and CAC cleavage reactions, and discriminated to fit the experimental data. It is found that a "dual-similar-site" mechanism involving alkali promoted dehydrogenation, on two adjacent Pt sites to affect CAC and CAO cleavage best describes the experimental data. The dehydrogenation reaction proceeds with a significantly lower activation barrier (E a 5 53 kJ/mol) compared with the noncatalytic hydrothermal conversion (E a 5 128 kJ/mol). The activation energy for glycerol hydrogenolysis on Pt/C catalyst without adding hydrogen is estimated to be 64 kJ/mol. a Rate/adsorption constants with 95% confidence level b Rate constant unit: m 3 /kg cat.h. c Unit of E a and DH: kJ/mol. d Sensitivity analysis procedures in Supporting Information Table S4-1, unit: kJ/mol. Scheme 6. Energy diagram of tandem catalysis vs. hydrothermal and conventional hydrogenolysis reactions (left: hydrothermal conversion vs. catalytic dehydrogenation; right: hydrogenolysis with external H 2 vs. with in situ H 2 ).