Abstract
Densities and viscosities have been measured for the binary mixtures of triethylene glycol with + 2-propanol, 2-butanol and 2-pentanol over the entire range of mole fraction at T = 293.15–323.15 K. From experimental data, the excess molar volume, thermal expansion coefficient, excess thermal expansion coefficient and deviation in viscosity were calculated. The experimental results have been discussed in terms of molecular interactions and formation of molecular complexes between unlike molecules. Influence of temperature and carbon chain length of alcohols on mentioned properties was discussed. Moreover, the friction theory coupled with PC-SAFT equation of state was applied to produce the viscosities of pure data and binary mixtures.
Similar content being viewed by others
Abbreviations
- MW i :
-
Molecular weight of component i
- p a :
-
Attraction pressure
- p r :
-
Repulsion pressure
- z :
-
Mass-weighted fraction of component
- η :
-
Total viscosity
- η 0 :
-
Dilute gas viscosity
- η f :
-
Friction viscosity
- η a :
-
Attractive viscosity scaling parameter
- η r :
-
Reduced viscosity
- \( \kappa_{\text{a}} \) :
-
Linear attractive viscous friction coefficient
- \( \kappa_{\text{r}} \) :
-
Linear repulsive viscous friction coefficient
- \( \kappa_{\text{rr}} \) :
-
Quadratic repulsive viscous friction coefficient
- A :
-
Helmholtz energy
- \( a_{0} \) :
-
Segment molar Helmholtz energy (seg), per mole of segments
- k :
-
Boltzmann’s constant
- m :
-
Effective number of segments within the molecule
- \( \in^{\text{AB}} \) :
-
Association energy of interaction between sites A and B
- \( k_{\text{ij}} \) :
-
Binary interaction parameter
- ε :
-
Molecular segment energy parameter
- ω :
-
Acentric factor
References
Raghuram N, Suresh R, Ramesh G, Sowjanya G, Jyostna ST. Excess parameters for the binary mixtures of sulfolane with chloroethanes at different temperatures. J Therm Anal Calorim. 2015;119:2107–17.
Guo Z, Zhang J, Zhang T, Li C, Zhang Y, Bai J. Liquid viscosities, excess properties, and viscous flow thermodynamics of triethylene glycol + water mixtures at T = 298.15, 303.15, 308.15, 313.15, and 318.15 K. J Mol Liq. 2012;165:27–31.
Almasi M. Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols: application of the ERAS model and cubic EOS. Thermochim Acta. 2013;554:25–31.
Almasi M. Thermodynamic properties of binary mixtures containing N,N-dimethylacetamide + 2-alkanol: experimental data and modeling. J Chem Eng Data. 2014;59:275–81.
Valtz A, Teodorescu M, Wichterle I, Richon D. Liquid densities and excess molar volumes for water + diethylene glycolamine, and water, methanol, ethanol, 1-propanol + triethylene glycol binary systems at atmospheric pressure and temperatures in the range of 28.315–36.315 K. Fluid Phase Equilib. 2004;215:129–42.
Kondaiah M, Sreekanth K, Sravana Kumar D, Nayeem MS, Krishna Rao D. Densities, viscosities, and excess properties for binary mixtures of ethylene glycol with amides at 30815 K. J Therm Anal Calorim. 2014;118:475–83.
Riddick JA, Bunger WB, Sakano TK. Organic solvents: physical properties and methods of purification. 4th ed. New York: Wiley; 1986.
Viswanath DS, Ghosh TK, Prasad DHL, Dutt NK, Rani KY. Viscosity of liquids: theory, estimation, experiment and data. Netherlands: Springer; 2007.
Lide RD, Handbook of Chemistry and Physics. Boca Raton: CRC Press; 2000. Section 6, p. 180–184.
Redlich OJ, Kister AT. Thermodynamic of nonelectrolyte solutions: algebraic representation of thermodynamic properties and the classification of solutions. Ind Eng Chem. 1948;40:345–8.
Quiñones-Cisneros SE, Zéberg-Mikkelsen CK, Stenby EH. The friction theory (f-theory) for viscosity modeling. Fluid Phase Equilib. 2000;169:249–76.
Chung TH, Ajlan M, Lee LL, Starling KE. Generalized multiparameter correlation for nonpolar and polar fluid transport-properties. Ind Eng Chem Res. 1988;27:671–9.
Zéberg-Mikkelsen CK, Quiñones-Cisneros SE, Stenby EH. Viscosity modeling of associating fluids based on the friction theory: pure alcohols. Fluid Phase Equilib. 2002;194–197:1191–203.
Gross J, Sadowski G. Perturbed-chain SAFT: an equation of state based on a perturbation theory for chain molecules. Ind Eng Chem Res. 2001;40:1244–60.
Gross J, Sadowski G. Application of the perturbed-chain SAFT equation of state to associating systems. Ind Eng Chem Res. 2002;41:5510–5.
Kontogeorgis MG, Folas GK. Thermodynamic models for industrial applications. 1st ed. United Kingdom: Wiley; 2010.
Acknowledgements
The author thanks the Islamic Azad University (Ahvaz Branch, Ahvaz) for providing the facilities to carry out this work.
Author information
Authors and Affiliations
Corresponding author
Electronic supplementary material
Below is the link to the electronic supplementary material.
Rights and permissions
About this article
Cite this article
Almasi, M. Thermophysical and transport properties of binary mixtures containing triethylene glycol and alcohols at different temperatures. J Therm Anal Calorim 124, 399–405 (2016). https://doi.org/10.1007/s10973-015-5127-6
Received:
Accepted:
Published:
Issue Date:
DOI: https://doi.org/10.1007/s10973-015-5127-6