Phase equilibrium in the ternary system water–ethylene glycol–dimethyl sulfoxide

2021 ◽  
Vol 31 (6) ◽  
pp. 890-892
Author(s):  
Irina A. Solonina ◽  
Mikhail R. Kiselev ◽  
Sergey V. Makaev ◽  
Margarita N. Rodnikova
Keyword(s):  
Phase Equilibrium ◽  
Ternary System ◽  
Ethylene Glycol ◽  
Dimethyl Sulfoxide ◽  
System Water

102. Melting point equations for the ternary system water/sodium chloride/ethylene glycol revisited

Cryobiology ◽  
2008 ◽  
Vol 57 (3) ◽  
pp. 336 ◽  
Author(s):  
Erik J. Woods ◽  
Aniruddha Bagchi ◽  
James D. Benson ◽  
Xu Han ◽  
John K. Critser
Keyword(s):  
Sodium Chloride ◽  
Melting Point ◽  
Ternary System ◽  
Ethylene Glycol ◽  
System Water

Melting point equations for the ternary system water/sodium chloride/ethylene glycol revisited

Cryobiology ◽  
2010 ◽  
Vol 61 (3) ◽  
pp. 352-356 ◽  
Author(s):  
James D. Benson ◽  
Aniruddha Bagchi ◽  
Xu Han ◽  
John K. Critser ◽  
Erik J. Woods
Keyword(s):  
Sodium Chloride ◽  
Melting Point ◽  
Ternary System ◽  
Ethylene Glycol ◽  
System Water

Liquid−Liquid Phase Equilibrium in the Ternary System Poly(ethylene glycol) + Cs2CO3+ H2O

2005 ◽  
Vol 50 (3) ◽  
pp. 792-795 ◽  
Author(s):  
Biehou Ma ◽  
Mancheng Hu ◽  
Shuni Li ◽  
Yucheng Jiang ◽  
Zhihong Liu
Keyword(s):  
Phase Equilibrium ◽  
Liquid Phase ◽  
Ternary System ◽  
Ethylene Glycol ◽  
Poly Ethylene Glycol ◽  
Poly Ethylene

scholarly journals Simultaneous Prediction of the Density and Viscosity of the Ternary System Water-Ethanol-Ethylene Glycol Using Support Vector Machine

2020 ◽  
pp. 68-73
Author(s):  
Ehsan Kianfar
Keyword(s):  
Support Vector Machine ◽  
Ternary System ◽  
Ethylene Glycol ◽  
Physical Property ◽  
Extractive Distillation ◽  
Support Vector ◽  
Viscosity Data ◽  
Machine Model ◽  
Mean Square Errors ◽  
System Water

Ethylene glycol is an organic solvent used in extractive distillation to separate water-ethanol mixtures. An appropriate process description requires accurate physical property data. In this paper, experimental liquid densities and dynamic viscosities of pure ethylene glycol as well as the ternary system water-ethanol-ethylene glycol are presented over a wide temperature range (298.15 to 328.15 K) at atmospheric pressure. Density and viscosity data of the ternary system of water-ethanol-ethylene glycol solutions were obtained from the literature and a support vector machine model was used to predict the density and viscosity of this system. The determination coefficients for density and viscosity of the ternary system of water-ethanol-ethylene glycol are 0.9854 and 0.9892, respectively. The mean square errors of density and viscosity are obtained 4.6572×10-4 and 3.4920×10-4, respectively. The results confirmed that the proposed method can predict the density and viscosity of the ternary system of water-ethanol-ethylene glycol as a function of temperature, using a support vector machine.

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