Liquid + liquid) equilibrium data of (tert amyl ethyl ether + ethanol + water) were determined experimentally at T = (298. 15, 308.15, and 318.15) K. The experimental results were correlated with the NRTL and UNIQUAC equations. The correlations were made at each temperature and for the three tempera
(Vapour  +  liquid) equilibria in (methanol  +  ethyl tert -butyl ether) and (methanol  +  ethyl tert -butyl ether +  toluene) at T =  328.15 K
β Scribed by Tatsuhiko Ohta; Masanori Takemura; Toshiro Yamada
- Publisher
- Elsevier Science
- Year
- 2002
- Tongue
- English
- Weight
- 94 KB
- Volume
- 34
- Category
- Article
- ISSN
- 0021-9614
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β¦ Synopsis
Vapour + liquid) equilibrium data are presented for (methanol + ethyl tert-butyl ether) and (methanol + ethyl tert-butyl ether + toluene) at T = 328.15 K. The experimental results were measured by using a Boublik recirculation still. The binary results for (methanol + ethyl tert-butyl ether) and for the two other binary mixtures constituting the ternary mixture are well correlated by the Peng-Robinson equation of state modified by Stryjek and Vera with the modified Huron-Vidal first-order and Wong-Sandler mixing rules. The ternary experimental results are also reproduced with good accuracy by the equation of state.
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