New double column system for heteroazeotropic batch distillation
| Autor: | Peter Lang, Gabor Modla, Ferenc Denes, Xavier Joulia |
|---|---|
| Přispěvatelé: | Centre National de la Recherche Scientifique - CNRS (FRANCE), Institut National Polytechnique de Toulouse - Toulouse INP (FRANCE), Université Toulouse III - Paul Sabatier - UT3 (FRANCE), Budapest University of Technology and Economics - BME (HUNGARY), Laboratoire de Génie Chimique - LGC (Toulouse, France) |
| Jazyk: | angličtina |
| Rok vydání: | 2009 |
| Předmět: |
Engineering
Heteroazeotrope Batch distillation business.industry General Chemical Engineering Binary number One-Step Feasibility study Double column Computer Science Applications law.invention Dynamic simulation law Scientific method Génie chimique Process engineering business Ternary operation Génie des procédés Distillation Simulation |
| Popis: | A new double column system (DCS) operated in closed mode is suggested for heterogeneous batch distillation. This configuration is investigated by feasibility studies based on the assumption of maximal separation and is compared with the traditional batch rectifier (BR). We study the configurations also by dynamic simulation based on a detailed model using a professional simulator. For the new configuration the minimal duration of the process is determined. The influence of the most important operational parameters is studied. The calculations and the simulations are performed for a binary (n-butanol–water) and for a ternary heteroazeotropic mixture (isopropanol–water + benzene as entrainer). One of the advantages of the DCS is that distillation of binary and ternary systems is performed in only one step. Furthermore the recovery of components is usually higher and the amount of byproducts is lower. |
| Databáze: | OpenAIRE |
| Externí odkaz: |
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