Liquid−Liquid Equilibria for the Ternary Systems Acetic Acid + Water + Butyl Acetate and Acetic Acid + Water + 2-Methyl Propyl Acetate at 304.15 K, 332.15 K, and 366.15 K

Liquid−Liquid Equilibria for the Ternary Systems Acetic Acid + Water + Butyl Acetate and Acetic Acid + Water + 2-Methyl Propyl Acetate at 304.15 K, 332.15 K, and 366.15 K

Liquid−liquid equilibria (LLE) for the ternary acetic acid + water + butyl acetate and acetic acid + water + 2-methyl propyl acetate systems were measured at 304.15 K, 332.15 K, and 366.15 K under atmospheric pressure. LLE phase diagrams with binodal curves and tie lines were obtained. The experimen...

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Veröffentlicht in:Journal of chemical and engineering data 2007-07, Vol.52 (4), p.1255-1257
Hauptverfasser: Wang, Lijun, Cheng, Youwei, Xiao, Xianjiang, Li, Xi
Format: Artikel
Sprache:eng
Schlagworte:
Chemistry
Exact sciences and technology
General and physical chemistry
Liquid-liquid equilibria
Phase equilibria
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Zusammenfassung:Liquid−liquid equilibria (LLE) for the ternary acetic acid + water + butyl acetate and acetic acid + water + 2-methyl propyl acetate systems were measured at 304.15 K, 332.15 K, and 366.15 K under atmospheric pressure. LLE phase diagrams with binodal curves and tie lines were obtained. The experimental data were used to estimate the LLE interaction parameters in the NRTL model.
ISSN:0021-9568
1520-5134
DOI:10.1021/je6005746