Liquid + liquid) equilibrium tie-lines were measured for the two quaternary systems = 101.3 kPa. The experimental (liquid + liquid) equilibrium results have been satisfactorily correlated by modified and extended UNIQUAC models both with ternary and quaternary parameters in addition to binary ones.
Viscosity of (ethane-1,2-diol  +  1,2-dimethoxyethane  +  water) at temperatures from 263.15 K to 353.15 K
β Scribed by Marina Cocchi; Matteo Manfredini; Andrea Marchetti; Laura Pigani; Renato Seeber; Lorenzo Tassi; Alessandro Ulrici; Chiara Zanardi
- Publisher
- Elsevier Science
- Year
- 2002
- Tongue
- English
- Weight
- 288 KB
- Volume
- 34
- Category
- Article
- ISSN
- 0021-9614
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β¦ Synopsis
The kinematic viscosity Ξ½ for (ethane-1,2-diol + 1,2-dimethoxyethane + water) was measured at 14 different ternary compositions covering the whole miscibility field, and at 19 temperatures in the range 263.15
T / K 353.15. The experimental values were fitted using empirical equations of the type Ξ½ = Ξ½(T ) and Ξ½ = Ξ½(x i ), respectively, in order to provide reliable models to account for the behaviour of the system. The excess kinematic viscosity Ξ½ E has been determined and interpreted in terms of the type and nature of the interactions among the components of the mixture. Using the experimental Ξ½ data, the thermodynamic properties ( G * , H * , S * ) of the viscous flow have been obtained from the Eyring's approach and standard thermodynamic equations. Furthermore, excess mixing functions, such as G * E , have been determined, and found to evidence the existence of quite strong specific interactions among the components, probably due to the formation of hydrogen bonds and dipolar networks. However, all the calculated excess mixing properties suggest the absence of stable three-component adducts.
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