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.
(Vapour + liquid) equilibria in (ethanol + 1,1-dimethylpropyl methyl ether) and (methanol + ethanol + 1,1-dimethylpropyl methyl ether) atT=333.15 K
β Scribed by Tatsuhiko Ohta; Masanari Ishio; Toshiro Yamada
- Publisher
- Elsevier Science
- Year
- 1998
- Tongue
- English
- Weight
- 104 KB
- Volume
- 30
- Category
- Article
- ISSN
- 0021-9614
No coin nor oath required. For personal study only.
β¦ Synopsis
Ε½
. Ε½ Vapour q liquid equilibrium data are presented for ethanol q 1,1-dimethylpropyl methyl . Ε½ . ether and methanol q ethanol q 1,1-dimethylpropyl methyl ether at T s 333.15 K. The Ε½ . binary results for ethanol q 1,1-dimethylpropyl methyl ether and for the two other binary mixtures constituting the ternary mixture are correlated with good accuracy by the PengαRobinson equation of state modified by Stryjek and Vera with the modified HuronαVidal first order mixing rule. The ternary experimental results are also well reproduced by the equation of state.
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