Optimal synthesis and design of catalytic distillation columns: A rate-based modeling approach

This work presents the optimal synthesis and design of a rigorous catalytic distillation (CD) column that explicitly considers the multiscale and multiphase nature of this intensification process. A rate-based model that couples micro and macroscale events taking place inside the CD column is explicitly considered. The direct solution of such intensive optimization problems is challenging due to nonlinearities introduced by heterogeneous reactions, transport phenomena, and interactions between discrete and continuous variables. Also, combinatorial complexity involved in the selection of multiple structural decisions complicates the problem, e.g., distribution of reactive stages along the column, location of feed stages, and total number of stages. A discrete-steepest descent-based optimization framework recently developed is used to address the optimal synthesis and design of rate-based CD columns. A case study involving the production of ethyl tert-butyl ether (ETBE) has been considered. The results show that the multiscale events occurring in this process intensification (PI) unit cannot be ignored since they produce process designs different from those obtained with an equilibrium-based CD model. The results also show that neglecting multiscale phenomena may result in infeasible CD designs. The outcomes gained through this study illustrate the critical need to systematically consider multiscale and multiphase events in CD columns for the optimal design of realistic, cost-effective, and attractive process intensification (PI) systems. (C) 2020 Elsevier Ltd. All rights reserved.

Automated summary

This work presents the optimal synthesis and design of a rigorous catalytic distillation column by explicitly considering the multiscale and multiphase nature of the intensification process. A rate-based model and a discrete-steepest descent-based optimization framework are utilized to address intensive optimization problems. A case study involving the production of ethyl tert-butyl ether (ETBE) is discussed, showing the critical need to systematically consider multiscale and multiphase events for the optimal design of process intensification systems.