Optimisation of a Methyl Acetate Production Process by Reactive Batch Distillation

Author(s):  
S. Elgue ◽  
L. Prat ◽  
M. Cabassud ◽  
J.M. Le Lann ◽  
J. Cézerac
Fuel ◽  
2021 ◽  
pp. 122408
Author(s):  
Wonho Jung ◽  
Seulah Lee ◽  
Hyeona Kim ◽  
Woo-Jae Kim ◽  
Jinwon Lee

2018 ◽  
Vol 154 ◽  
pp. 01008 ◽  
Author(s):  
Ahmad Misfa Kurniawan ◽  
Renanto Handogo ◽  
Hao-Yeh Lee ◽  
Juwari Purwo Sutikno

The development of mathematics model especially non-square open-loop dynamic model has grown rapidly since four decades. Because of the need of simplicity and accuracy, industrial world is demanding a dynamic mathematical model as simple as possible but it still can represent the whole real process. Therefore, to meet those needs, an open-loop dynamic model of methyl acetate production process by using reactive distillation column has been built. Feed ratio, reflux ratio and reboiler duty were chosen to be the manipulated variables to make a better performance rather than only reflux flowrate and reboiler duty. Methyl acetate fraction in distillate and water fraction in bottom were still be selected as controlled variables, so a non-square open-loop dynamic model was formed.


2001 ◽  
Vol 34 (3) ◽  
pp. 312-318 ◽  
Author(s):  
SABINE GIESSLER ◽  
SHINJI HASEBE ◽  
IORI HASHIMOTO

1999 ◽  
Vol 23 ◽  
pp. S423-S426 ◽  
Author(s):  
R. Schneider ◽  
C. Noeres ◽  
L.U. Kreul ◽  
A. Górak

2003 ◽  
Vol 27 (12) ◽  
pp. 1855-1866 ◽  
Author(s):  
Robert S. Huss ◽  
Fengrong Chen ◽  
Michael F. Malone ◽  
Michael F. Doherty

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