Optimization-Based Design of a Reactive Distillation Column for the Purification Process of Cyclohexanone Using Rigorous Simulation Model and Validated Using an Experimental Packed Column
Author:
Affiliation:
1. Dpto. Ingeniería Química, Facultad CC. Químicas. Universidad Complutense de Madrid. Avda. Complutense s/n 28040 Madrid, Spain
2. Department of Chemical Engineering. University College London, Torrington Place. London WC1E 7JE, U.K.
Funder
Ministerio de Educaci?n, Cultura y Deporte
Publisher
American Chemical Society (ACS)
Subject
Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/acs.iecr.8b03560
Reference46 articles.
1. Modelling of homogeneously catalysed reactive distillation processes in packed columns: Experimental model validation
2. Analysis of the Start-up Process for Reactive Distillation
3. Simulation of a plant scale reactive distillation column for esterification of acetic acid
4. Design and Control of Reactive Distillation System for Esterification of Levulinic Acid and n-Butanol
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1. Optimal design of superstructures for placing units and streams with multiple and ordered available locations. Part II: Rigorous design of catalytic distillation columns;Computers & Chemical Engineering;2020-08
2. Transformation of Cyclic Ketones as Impurities in Cyclohexanone in the Caprolactam Production Process;Industrial & Engineering Chemistry Research;2019-11-14
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