Rising CO2 levels in the atmosphere are becoming increasingly problematic, due to the effect of CO2 on climate change. CO2 capture and utilization has high potential as strategy to close the carbon cycle. An example of utilization of CO2 is the electrochemical reduction of CO2 to more valuable compounds. This thesis discusses the electrochemical reduction of CO2 to oxalic acid. Until now, oxalic acid as target product of the electrochemical CO2 reduction has not been studied in great depth, mainly because it only forms in non-aqueous solutions. The influence on several parameters, namely cathode material, applied potential,
anolyte, catholyte, membrane, supporting electrolyte, and temperature, on the electrochemical conversion of CO2 to oxalic acid has been studied. The first step in scaling-up has been taken, from a batch reactor (H-cell reactor) to a semi-continuous system (flow-cell reactor). In order to investigate the feasibility and its implementation in the industry, several options for the downstream processing of oxalic acid are discussed and a techno-economic analysis is performed on the proposed process design.

From the parametric study that was carried out, the parameters that had a considerable effect on the performance of the electrochemical reduction of CO2 to oxalic acid were cathode and anode material, catholyte and anolyte, membrane, applied potential and temperature. With the batch reactor optimal results in terms of faradaic efficiency and current density have been found, using lead as cathode, platinumas anode, propylene carbonate+0.7M tetraethylammonium chloride as catholyte and 0.5M H2SO4 as anolyte in which the cathodic and anodic compartment are separated by a Nafion 117 membrane. At higher temperatures, higher current densities were induced by reduction of mass transfer limitations. Within the range of -2.2V to -2.7V vs Ag/AgCl, increasing current densities and decreasing faradaic efficiencies were found with increasing applied potential. Semi-continuous flow-cell was investigated as a strategy to increase the mass transfer in the system. Although higher reduction currents were measured during CO2 reduction in a flow-cell compared
to the batch reactor, the faradaic efficiency towards oxalic acid was lower. The oxalic acid produced during CO2 reduction in the electrochemical reactor is dissolved in the liquid electrolyte. A further separation step of the oxalic acid from the liquid needs to be present to recover the product in a solid state. In order to assess the feasibility of the separation of oxalic acid, several technologies were addressed. Liquid-liquid extraction followed by crystallization is experimentally proved to be a suitable method for the separation and recovery
of oxalic acid from the electrolyte. Based on this separation method, a process design is proposed and a techno-economic analysis has been performed. The techno-economic analysis showed a favorable economic potential for this technology if certain key performance indicators can be achieved. However, the maturity level of this process is still in early stages. Some of those key performance indicators still need to be experimentally improved, further research should focus on increasing the obtained current densities and obtaining
stable faradaic efficiencies.