Nonlinear Control of a High-Purity Ethylene Glycol Reactive Distillation Column

1997 ◽  
Vol 30 (9) ◽  
pp. 413-418 ◽  
Author(s):  
Aditya Kumar ◽  
Prodromos Daoutidis
2000 ◽  
Vol 55 (21) ◽  
pp. 4925-4937 ◽  
Author(s):  
Rosendo Monroy-Loperena ◽  
Eduardo Perez-Cisneros ◽  
Jose Alvarez-Ramirez

AIChE Journal ◽  
2009 ◽  
Vol 55 (8) ◽  
pp. 2106-2121 ◽  
Author(s):  
Kejin Huang ◽  
Fanghong Zhu ◽  
Wenming Ding ◽  
San-Jang Wang

1999 ◽  
Vol 23 ◽  
pp. S835-S838 ◽  
Author(s):  
Rosendo Monroy-Loperena ◽  
Eduardo Pérez-Cisneros ◽  
José Alvarez-Ramírez

2019 ◽  
Vol 21 (3) ◽  
pp. 1-7 ◽  
Author(s):  
Syed Sadiq Ali ◽  
Mohammad Asif ◽  
Avijit Basu

Abstract Biodiesel is a promising energy substitute of fossil fuels since it is produced from renewable and biodegradable sources. In the present work, reactive distillation (RD) process is designed and simulated using Aspen Plus process simulator to produce biodiesel of high purity through esterification reaction. The simultaneous reaction and separation in same unit enhances the biodiesel yield and composition in RD process. Two flowsheets are proposed in present work. In the first flowsheet, the unreacted methanol is recycled back to reactive distillation column. Biodiesel with 99.5 mol% purity is obtained in product stream while the byproduct stream comprises 95.2 mol% water, which has to be treated further. In the second flowsheet, a part of methanol recycle is split and purged. In this case, the biodiesel composition in product stream is 99.7 mol% whereas water composition is 99.9 mol% in byproduct stream, which can be reused for other process without treatment.


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