• Vapor-Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil

Data

[{'id': 3894, 'desc': '23 datapoints in 1 series, <b>quantities:</b> Boiling point at pressure, <b>system:</b> ethyl acetate'}, {'id': 3895, 'desc': '3 datapoints in 1 series, <b>quantities:</b> Vapor pressure, <b>system:</b> ethyl acetate'}, {'id': 3896, 'desc': '12 datapoints in 1 series, <b>quantities:</b> Boiling point at pressure, <b>system:</b> isobutyl acetate'}, {'id': 3897, 'desc': '5 datapoints in 1 series, <b>quantities:</b> Vapor pressure, <b>system:</b> isobutyl acetate'}, {'id': 3898, 'desc': '15 datapoints in 1 series, <b>quantities:</b> Boiling point at pressure, <b>system:</b> isoamyl acetate'}, {'id': 3899, 'desc': '1 datapoints in 1 series, <b>quantities:</b> Vapor pressure, <b>system:</b> isoamyl acetate'}, {'id': 3900, 'desc': '37 datapoints in 3 series, <b>quantities:</b> Boiling point at pressure, <b>system:</b> 2-methylpropyl ethanoate + ethyl acetate'}, {'id': 3901, 'desc': '37 datapoints in 3 series, <b>quantities:</b> Mole fraction, <b>system:</b> 2-methylpropyl ethanoate + ethyl acetate'}, {'id': 3902, 'desc': '27 datapoints in 2 series, <b>quantities:</b> Boiling point at pressure, <b>system:</b> 2-methylpropyl ethanoate + 3-methylbutyl ethanoate'}, {'id': 3903, 'desc': '27 datapoints in 2 series, <b>quantities:</b> Mole fraction, <b>system:</b> 2-methylpropyl ethanoate + 3-methylbutyl ethanoate'}] temp"