Abstract
A model for an internally heat-integrated batch distillation column (batch or semibatch HIDiC) was developed, and the separation of a benzene-toluene binary mixture was simulated. The applicability of the model was examined using the commercial process simulator Aspen Plus Dynamics®. With the semi-batch HIDiC, the model has the potential to reduce process time and energy consumption more precisely than the conventional batch distillation model. This is an abstract of a paper presented at the CHISA 2012 - 20th International Congress of Chemical and Process Engineering and PRES 2012 - 15th Conference PRES (Prague, Czech Republic 8/25-29/2012).
Original language | English |
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Publication status | Published - 2012 |
Externally published | Yes |
Event | 20th International Congress of Chemical and Process Engineering, CHISA 2012 and 15th Conference on Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction, PRES 2012 - Prague, Czech Republic Duration: 2012 Aug 25 → 2012 Aug 29 |
Conference
Conference | 20th International Congress of Chemical and Process Engineering, CHISA 2012 and 15th Conference on Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction, PRES 2012 |
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Country/Territory | Czech Republic |
City | Prague |
Period | 12/8/25 → 12/8/29 |
ASJC Scopus subject areas
- Chemical Engineering (miscellaneous)