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Liquid extraction equilibria of type 2: (tert-amyl methyl ether + 1-octonal + water) atT=(298.15 and 308.15) K

✍ Scribed by Alberto Arce; Manuel Blanco

Publisher: Elsevier Science
Year: 1998
Tongue: English
Weight: 144 KB
Volume: 30
Category: Article
ISSN: 0021-9614
DOI: 10.1006/jcht.1998.0346

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✦ Synopsis

Ž

. Ž Experimental liquid q liquid equilibrium data for tert-amyl methyl ether q 1-octanol q . Ž . water at T s 298.15 and 308.15 K were satisfactorily fitted with UNIQUAC, TK-Wilson, and NRTL equations, and predicted by the UNIFAC group contribution method.

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Extraction equilibria of the type 2: ter

Extraction equilibria of the type 2: ternary liquid mixture {x1tert-butyl methyl ether +x2water + (1 −x1−x2)1-octanol} at 298.15 K and 308.15 K

✍ Alberto Arce; Manuel Blanco; Ana Soto; Isabel Vidal 📂 Article 📅 1996 🏛 Elsevier Science 🌐 English ⚖ 337 KB

We report liquid-liquid equilibrium data for the ternary system {x1tert-butyl methyl ether(C5H12O)+x2water+(1-x1-x2)1-octanol} at 298.15 and 308.15 K. The data were satisfactorily fitted with UNIQUAC and NRTL equations, and were satisfactorily predicted by the UNIFAC group contribution method.