Measurement of vapour-liquid equilibrium data of liquids with low vapour pressure

1987 ◽  
Vol 52 (2) ◽  
pp. 264-270
Author(s):  
Július Surový ◽  
Elena Graczová ◽  
Ján Dojčanský

A semimicrostill for measuring vapour-liquid equilibrium data suitable especially for the determination at pressures about 100 Pa is described. The still operates isothermally on the principle of differential distillation. The composition of equilibrium phases is determined chromatographically. The error caused by unstationariness of the apparatus was studied. As an example of its use, the vapour-liquid equilibrium data of the N-methylpyrrolidone-ethylene glycol solution at 50 °C are reported. The dependence of excess Gibbs energy on composition was expressed by means of the fourth-order Redlich-Kister and NRTL equations. The system exhibits negative deviation from ideal behaviour. Thermodynamic treatment proves a good consistency of the equilibrium data measured.

1989 ◽  
Vol 54 (11) ◽  
pp. 2856-2862 ◽  
Author(s):  
Július Surový ◽  
Elena Graczová ◽  
Jana Ovečková

Vapour-liquid equilibrium data are given for the binary systems ethylene glycol (EG)-N-methylpyrrolidone (NMP), ethylene glycol-diethylene glycol (DEG), and N-methylpyrrolidone-diethylene glycol at 50°C. The measurement of vapour-liquid equilibrium was carried out in a modified version of semimicrostill from foregoing paper. This still makes it possible to measure even at the pressures of the order 101 Pa. The dependence of the excess Gibbs energy on composition was expressed by the 4th order Redlich-Kister, Wilson, and NRTL equations. The systems EG-NMP and DEG-NMP exhibit negative deviations from ideal behaviour, EG with DEG form practically ideal solution.


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