vapor hold-up dynamics neglected, 4) pressure drop along the columns neglected, and 5) ideal mixing of the vapor and the liquid phase. The detailed mathematical model developed by Stojkovic et , containing mass balances on all the parts of the batch column (MES), is used. Equation ( ), P,P 𝑖 refers to total/partial pressure, respectively, whereas, 𝑥 𝑖 ,y 𝑖 refers to the molar concentrations of the respected component in the liquid/vapor phase, respectively.