“…For example, some authors have proposed a framework for the integrated design of a solvent and extractive distillation process by solving a multi-objective optimization problem addressing constraints related to thermodynamic process feasibility, along with process operation, a process model, and molecular constraints, 49 or a more rigorous rate-based model. 50 In these studies, the property prediction in a molecular scale is addressed using COSMO approaches while the process model can be a pinch-based model based on a minimum solvent flow rate and minimum energy demand 49 or a more rigorous rate-based model. 50 The use of such process models is relevant for an accurate process design but there exist simpler criteria for assessing extractive distillation feasibility, such as solvent capacity and selectivity, 51 which are further related to infinite dilution activity coefficients (IDAC), and univolatility curves.…”