Spreadsheet to illustrate the application of relaxation methods for multicomponent distillation separations

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Título: Spreadsheet to illustrate the application of relaxation methods for multicomponent distillation separations
Autor/es: Gómez-Siurana, Amparo | Font, Alicia
Grupo/s de investigación o GITE: Procesado y Pirólisis de Polímeros | Equilibrio entre Fases
Centro, Departamento o Servicio: Universidad de Alicante. Departamento de Ingeniería Química
Palabras clave: Spreadsheets | Multicomponent distillation | Batch distillation | Relaxation method | Continuous column | Total reflux
Fecha de publicación: 26-jul-2023
Editor: Elsevier
Cita bibliográfica: Education for Chemical Engineers. 2023, 45: 161-172. https://doi.org/10.1016/j.ece.2023.06.005
Resumen: Rigorous calculation methods to simulate multicomponent distillation processes involve large number of variables and equations that are difficult to solve by hand and require the use of specific software. With this purpose, commercial process simulators have been included for years as learning tools in the syllabus of Chemical Engineering degrees. Nevertheless, there is thus a possibility of using these packages as a black box and strategies to mitigate that risk have been developed, as the use of spreadsheets where students can follow and check the calculation algorithms and the details of such calculations. One alternative to solve multicomponent distillation problems is the use of relaxation methods, that find the steady-state solution of a continuous distillation column by solving unsteady-state equations from a specified initial condition, thus providing an analogy with the column startup. In this work, a novel spreadsheet to apply a relaxation method is proposed. Calculation begins with the simulation of a distillation column at total reflux, which is a common way to start up these processes. In order to facilitate the development of unsteady-state equations and operation, a batch distillation column is also simulated. Finally, the evolution of a continuous distillation column from a specified starting condition to steady-state is simulated.
URI: http://hdl.handle.net/10045/136506
ISSN: 1749-7728
DOI: 10.1016/j.ece.2023.06.005
Idioma: eng
Tipo: info:eu-repo/semantics/article
Derechos: © 2023 The Authors. Published by Elsevier Ltd on behalf of Institution of Chemical Engineers. This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/4.0/).
Revisión científica: si
Versión del editor: https://doi.org/10.1016/j.ece.2023.06.005
Aparece en las colecciones:INV - GTP3 - Artículos de Investigación sobre Equilibrio entre Fases
INV - EQF - Artículos de Revistas

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