This paper investigates the transesterification of propylene carbonate with methanol to form dimethyl carbonate and propylene glycol in preparation for integrating this reaction into a reactive distillation column. The investigation of suitable catalysts matching the operating window of a reactive distillation column is essential to design a feasible process. Hence, a screening of nine heterogeneous and two homogeneous catalysts to identify a suited catalyst for this reaction is presented. Afterwards, the chemical equilibrium and reaction kinetics are investigated using an experimental and theoretical approach. Molar- and activity based chemical equilibrium constants were determined from the experimental results, and their temperature dependency was described using the van't Hoff equation. The reaction kinetics was measured using the homogeneous catalyst sodium methoxide to enhance the reaction rate. The theoretical description of the reaction kinetics was established using an activity based approach to account for the nun ideal thermodynamic liquid-phase behavior. The well-known Arrhenius equation was used to describe the temperature dependency of the reaction rate constant. (C) 2013 Elsevier Ltd. All rights reserved.