TY - JOUR
T1 - CAMD for entrainer screening of extractive distillation process based on new thermodynamic criteria
AU - Cignitti, Stefano
AU - Rodriguez-Donis, Ivonne
AU - Abildskov, Jens
AU - You, Xinqiang
AU - Shcherbakova, Nataliya
AU - Gerbaud, Vincent
PY - 2019
Y1 - 2019
N2 - This paper presents a preliminary design framework for finding suitable homogeneous entrainers E to separate minimum boiling azeotropic mixtures AB by extractive distillation. The framework incorporates techniques such as Computer Aided Molecular Design (CAMD), addressing process needs and targeted thermodynamic properties. New thermodynamic criteria are considered for the entrainer design based on both, the thermodynamic properties of the binary mixtures AE and BE and the isovolatility curves in the ternary mixture ABE. In the CAMD problem, energy related property constraints on the boiling point and the vaporization enthalpy are also considered, leading to a mixed integer non-linear programming problem. Entrainer candidates are ranked by the maximization of the driving force of separation of A and B from their respective mixtures AE and BE under constraints limiting the entrainer composition for fixed values of the relative volatility. Further process optimization is done for validating the entrainer ranking by using Aspen plus V7.3, which minimizes the energy consumption and computes the total annual cost to compare different designs. The new thermodynamic criteria perform better than selectivity alone or a combined selectivity — capacity criterion, as proposed in the literature. The framework is illustrated through an entrainer problem design for the separation of acetone–methanol. Ethylene glycol is obtained as the best design solution. Comparison with conventional entrainers water and DMSO is carried out to validate the performance of the new criteria based on optimal process design study.
AB - This paper presents a preliminary design framework for finding suitable homogeneous entrainers E to separate minimum boiling azeotropic mixtures AB by extractive distillation. The framework incorporates techniques such as Computer Aided Molecular Design (CAMD), addressing process needs and targeted thermodynamic properties. New thermodynamic criteria are considered for the entrainer design based on both, the thermodynamic properties of the binary mixtures AE and BE and the isovolatility curves in the ternary mixture ABE. In the CAMD problem, energy related property constraints on the boiling point and the vaporization enthalpy are also considered, leading to a mixed integer non-linear programming problem. Entrainer candidates are ranked by the maximization of the driving force of separation of A and B from their respective mixtures AE and BE under constraints limiting the entrainer composition for fixed values of the relative volatility. Further process optimization is done for validating the entrainer ranking by using Aspen plus V7.3, which minimizes the energy consumption and computes the total annual cost to compare different designs. The new thermodynamic criteria perform better than selectivity alone or a combined selectivity — capacity criterion, as proposed in the literature. The framework is illustrated through an entrainer problem design for the separation of acetone–methanol. Ethylene glycol is obtained as the best design solution. Comparison with conventional entrainers water and DMSO is carried out to validate the performance of the new criteria based on optimal process design study.
KW - CAMD
KW - Driving force
KW - Entrainer selection
KW - Extractive distillation
KW - Isovolatility curves
U2 - 10.1016/j.cherd.2019.04.038
DO - 10.1016/j.cherd.2019.04.038
M3 - Journal article
SN - 0263-8762
VL - 147
SP - 721
EP - 733
JO - Chemical Engineering Research and Design
JF - Chemical Engineering Research and Design
ER -