Mixture of 2-Propanol + Acetic acid, propyl ester

Datasets

1. Mole fraction (2)
2. T_boil(P) - Boiling temperature at pressure P, K

Mole fraction of 2-Propanol (1) [ref]

Operational condition: Pressure, kPa = 101 (Gas)

Mole fraction of 2-Propanol (1) - Liquid	Mole fraction of 2-Propanol (1) - Gas
0.0000	0.0000
0.0548	0.1150
0.1067	0.2359
0.2287	0.4070
0.3510	0.5461
0.3918	0.5756
0.4477	0.6356
0.5490	0.6889
0.6332	0.7432
0.7759	0.8232
0.8448	0.8699
0.8945	0.9144
0.9357	0.9460
0.9692	0.9690
0.9781	0.9764
1.0000	1.0000

Azeotropic composition: mole fraction of 2-Propanol (1) [ref]

Temperature, K - Liquid	Azeotropic composition: mole fraction of 2-Propanol (1) - Liquid
355.30	0.9690

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of 2-Propanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	374.20
0.0548	371.80
0.1067	369.50
0.2287	364.60
0.3510	361.70
0.3918	360.30
0.4477	359.30
0.5490	357.80
0.6332	357.20
0.7759	356.10
0.8448	355.90
0.8945	355.50
0.9357	355.40
0.9692	355.30
0.9781	355.30
1.0000	355.40

Sources

• Experimental studies and thermodynamic analysis of isobaric vapor-liquid-liquid equilibria of 2-propanol + water system using n-propyl acetate and isopropyl acetate as entrainers

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