The heterogeneously catalyzed hydrogenation of biomass‐or CO2‐derived glycolic acid (GA) is a renewable pathway for obtaining the bulk chemical ethylene glycol (EG). In this study, the reaction network of the aqueous‐phase hydrogenation of GA is investigated over a Ru/C catalyst. As previous studies indicated, several parallel and consecutive reactions can occur in addition to the desired reaction to EG. These reactions are experimentally assessed by employing different (possible) reaction intermediates and products as reactants. The data for all individual reactions and GA hydrogenation at different reaction temperatures (120‐180°C) is combined to propose a catalytic reaction pathway network and to develop a corresponding microkinetic model. The model describes the catalytic data in the range up to 150°C, where EG is the main reaction product, with high accuracy. It is shown that selectivity for EG is highest at 120°C and decreases strongly with increasing temperatures both due to the parallel reaction of GA into AcA, which has a significantly higher activation energy than the overall hydrogenation of GA into EG, and due to degradation of EG into ethanol and volatile products. Temperatures exceeding 150°C predominantly yield volatile products, suggesting low yields of EG or AcA at higher temperatures despite enhanced GA conversion.
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