Operation and control of a new pressure swing batch distillation system

Arpad Kopasz, Gabor Modla, Peter Lang

Research output: Chapter in Book/Report/Conference proceedingConference contribution

2 Citations (Scopus)

Abstract

The pressure swing separation of a binary minimum azeotrope in a double column batch stripper is studied by rigorous simulation. For controlling the product compositions a simple scheme is presented. The parameters of PID controllers are determined. Influence of the most important parameter (division ratio of liquid leaving the top vessel) is investigated. The calculations were made for the mixture n-pentane-acetone by using a professional dynamic simulator.

Original languageEnglish
Title of host publication12th International Conference on Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction, PRES'09
PublisherItalian Association of Chemical Engineering - AIDIC
Pages707-712
Number of pages6
Volume18
ISBN (Print)9788895608044
DOIs
Publication statusPublished - Jan 1 2009
Event12th International Conference on Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction, PRES'09 - Rome, Italy
Duration: May 10 2009May 13 2009

Other

Other12th International Conference on Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction, PRES'09
CountryItaly
CityRome
Period5/10/095/13/09

ASJC Scopus subject areas

  • Chemical Engineering(all)

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  • Cite this

    Kopasz, A., Modla, G., & Lang, P. (2009). Operation and control of a new pressure swing batch distillation system. In 12th International Conference on Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction, PRES'09 (Vol. 18, pp. 707-712). Italian Association of Chemical Engineering - AIDIC. https://doi.org/10.3303/CET0918115