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Exploiting Residue Curve Maps to Assess Thermodynamic Feasibility Boundaries under Uncertain Operating Conditions

Authors :
Flavio Manenti
Alessandro Di Pretoro
Ludovic Montastruc
Xavier Joulia
Laboratoire de génie chimique [ancien site de Basso-Cambo] (LGC)
Université Toulouse III - Paul Sabatier (UT3)
Université Fédérale Toulouse Midi-Pyrénées-Université Fédérale Toulouse Midi-Pyrénées-Centre National de la Recherche Scientifique (CNRS)-Institut National Polytechnique (Toulouse) (Toulouse INP)
Université Fédérale Toulouse Midi-Pyrénées
DIpartimento di Scienza dei Materiali e Ingegneria Chimica
Politecnico di Torino = Polytechnic of Turin (Polito)
Dipartimento di Fisica [Politecnico Milano]
Politecnico di Milano [Milan] (POLIMI)
Centre National de la Recherche Scientifique - CNRS (FRANCE)
Institut National Polytechnique de Toulouse - Toulouse INP (FRANCE)
Université Toulouse III - Paul Sabatier - UT3 (FRANCE)
Politecnico di Milano (ITALY)
Source :
Industrial and engineering chemistry research, Industrial and engineering chemistry research, American Chemical Society, 2020, 59 (36), pp.16004-16016. ⟨10.1021/acs.iecr.0c02383⟩
Publication Year :
2020
Publisher :
HAL CCSD, 2020.

Abstract

International audience; The very first step of almost any separation process design procedure is the thermodynamic feasibility analysis. In the case of distillation, residue curve maps (RCMs) represent an essential tool to assess whether the separation is feasible or not. However, the analysis is generally carried out by referring to nominal operating conditions and product purities as specification. This means that, when process parameters are likely to undergo fluctuations, the prediction of the system response is not that obvious. An ABE/W (acetone−butanol−ethanol/water) mixture was then selected as a case study since it allows us to discuss several non-ideal thermodynamic behaviors and because of the renewed interest in biorefinery and sustainable processes during recent years. Residue curve mapping was then exploited to determine the thermodynamic feasibility range for multicomponent distillation processes as well as for distillation trains and process-intensified solutions taking into account both product purity and product recovery specifications. The final product of this study is a thorough procedure to determine the flexibility boundaries of feed and product compositions as well as an immediate and intuitive graphical representation from a binary standard distillation column to a complex multicomponent dividing wall column application

Details

Language :
English
ISSN :
08885885 and 15205045
Database :
OpenAIRE
Journal :
Industrial and engineering chemistry research, Industrial and engineering chemistry research, American Chemical Society, 2020, 59 (36), pp.16004-16016. ⟨10.1021/acs.iecr.0c02383⟩
Accession number :
edsair.doi.dedup.....b1b755253f186ce7438f0b2855bace72
Full Text :
https://doi.org/10.1021/acs.iecr.0c02383⟩