Modeling Separation Dynamics in a Multi-Tray Bio-Ethanol Distillation Column

Publikation: Bidrag til bog/antologi/rapport/konference proceedingKonferenceartikel i proceedingForskningpeer review

Abstrakt

The high energy consumption of popularly used distillation columns has motivated development of energytracking dynamic models with the ultimate objective for potential better energy and quality control of these separation facilities. A dynamic model being able to explicitly describe both the product quality and energy consumption in a typical bio-ethanol distillation column is proposed in this paper. The proposed model is derived based on mass and energy balance principles, with an empirical model of the evaporation dynamics of liquids on column trays. The model parameters are identified based on some available test data. General consistencies between the developed model and field data are clearly observed, even though some further tuning and improvement of this developed model is still needed.
OriginalsprogEngelsk
TitelProceedings of the 2015 IEEE International Conference on Mechatronics and Automation (ICMA)
Antal sider6
UdgivelsesstedBeijing
ForlagIEEE Press
Publikationsdato2015
Sider1349 - 1354
Artikelnummer7237681
ISBN (Trykt)978-1-4799-7097-1, 9781479970964
DOI
StatusUdgivet - 2015
Begivenhed2015 IEEE International Conference on Mechatronics and Automation (ICMA) - Baijing, Kina
Varighed: 2 aug. 20155 aug. 2015

Konference

Konference2015 IEEE International Conference on Mechatronics and Automation (ICMA)
LandKina
ByBaijing
Periode02/08/201505/08/2015

Fingeraftryk

Dyk ned i forskningsemnerne om 'Modeling Separation Dynamics in a Multi-Tray Bio-Ethanol Distillation Column'. Sammen danner de et unikt fingeraftryk.

Citationsformater