The electrochemical cycling processes of acetone/IPA were simulated to determine the carbon footprint in comparison to the thermochemical processes. Electrochemical hydrogenation (ECH) of acetone has been performed in an electrochemical flow reactor with reported IPA selectivity of up to 100% and acetone concentrations of up to 7M on Pt/Ru in the literature. The acetone ECH simulation was performed on a basis of a flow reactor. The feed contained 2M acetone concentration in water owing to better results observed at lower acetone concentrations in acetone ECH system. Figure illustrates the details of the acetone ECH process using a process flow diagram. The ECH reactor was modelled as a block with 98% conversion and 100% IPA selectivity to match that of TCH process. The reaction was an overall process where acetone ECH operated at the cathode coupled with OER at the anode (reactions 1-3). Thus, the applied cell voltage was assumed to be 1.11V which is the theoretical thermodynamic potential of the acetone ECH.