The CO2 capture via MAMG proceeds with the migration of the bicarbonate ions at the migration current densities of 15mA/cm 2 in the mixtures containing RTIL and EG. The pH drop in Figure shows the rate of bicarbonate ions entering the aqueous compartment and decomposing to CO2, as discussed earlier in Section 2.2. Also, based on HCO3 -CO3 2-water equilibrium, the concentration of the aqueous CO2 was determined, as shown in Figure . Since the aqueous solution was pre-equilibrated, the solution initially contained ~7mM CO2. However, in the presence of an external electric field, the CO2 concentration quickly rises from 7 mM to 33 mM, reaching its maximum solubility in water. To highlight the role of conductivity in the MAMG process, we use the metric energy consumed per mol of CO2 ( 2