Separation of azeotropic mixture (acetone + n-heptane) by extractive distillation with intermediate and heavy boiling entrainers: Vapour-liquid equilibrium measurements and correlation

2021 ◽  
Vol 152 ◽  
pp. 106284 ◽  
Author(s):  
Tao Zhang ◽  
Ao Li ◽  
Xin Xu ◽  
Yixin Ma ◽  
Dongmei Xu ◽  
...  
Keyword(s):  
Extractive Distillation ◽  
Azeotropic Mixture ◽  
Liquid Equilibrium

Liquid-liquid equilibrium in the water-ethanol-toluene system. Experimental results

1989 ◽  
Vol 54 (3) ◽  
pp. 581-585 ◽  
Author(s):  
Květuše Říčná ◽  
Jaroslav Matouš ◽  
Josef P. Novák ◽  
Vladimír Kubíček
Keyword(s):  
Distribution Coefficient ◽  
Boiling Point ◽  
Normal Pressure ◽  
Experimental Results ◽  
Azeotropic Mixture ◽  
Liquid Equilibrium

Liquid-liquid equilibrium at 5, 25, and 50 °C was measured in the water-ethanol-toluene system. Special attention was paid to the determination of distribution coefficient of ethanol. Besides, the composition and boiling point of azeotropic mixture at normal pressure were determined.

Effect of Solvent Flow Rates on Controllability of Extractive Distillation for Separating Binary Azeotropic Mixture

2015 ◽  
Vol 54 (51) ◽  
pp. 12908-12919 ◽  
Author(s):  
Yinglong Wang ◽  
Shisheng Liang ◽  
Guangle Bu ◽  
Wei Liu ◽  
Zhen Zhang ◽  
...  
Keyword(s):  
Extractive Distillation ◽  
Azeotropic Mixture ◽  
Flow Rates ◽  
Effect Of Solvent ◽  
Solvent Flow
Sign in / Sign up

Export Citation Format

Share Document