Article ID Journal Published Year Pages File Type
6659694 The Journal of Chemical Thermodynamics 2018 20 Pages PDF
Abstract
This work reports the experimental vapor-liquid equilibrium data of {ethanol(1) + glycerol(2)} and {tert-butanol(1) + glycerol(2)} systems. Boiling pressures were measured using a static synthetic method over the temperature range of 423-523 K. The experimental data were fitted using the Peng Robinson equation of state (PR-EoS) coupled to classical van der Waals mixing rules, quadratic regarding the composition. Results presented in this work may be relevant in process design of glycerol etherification.
Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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