Mixture of Acetic acid, propyl ester + Mesitylene

Datasets

1. ρ_l - Mass density, kg/m3
2. γ - Surface tension liquid-gas, N/m

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetic acid, propyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	861.04
298.15	0.0498	861.7
298.15	0.0996	862.38
298.15	0.1504	863.1
298.15	0.2006	863.85
298.15	0.2502	864.63
298.15	0.3006	865.46
298.15	0.3499	866.32
298.15	0.4003	867.23
298.15	0.4498	868.17
298.15	0.4985	869.14
298.15	0.5526	870.28
298.15	0.6001	871.33
298.15	0.6500	872.49
298.15	0.6987	873.7
298.15	0.7369	874.66
298.15	0.7983	876.31
298.15	0.8504	877.83
298.15	0.8995	879.31
298.15	0.9397	880.63
298.15	1.0000	882.64
303.15	0.0000	856.96
303.15	0.1000	857.96
303.15	0.2012	859.34
303.15	0.2995	860.81
303.15	0.3998	862.5
303.15	0.4996	864.32
303.15	0.6004	866.41
303.15	0.7007	868.63
303.15	0.7987	871.2
303.15	0.9009	874.11
303.15	1.0000	876.99
308.15	0.0000	852.84
308.15	0.0985	853.66
308.15	0.1992	854.81
308.15	0.3018	856.13
308.15	0.3991	857.53
308.15	0.5009	859.15
308.15	0.6012	861.08
308.15	0.6997	863.19
308.15	0.7983	865.52
308.15	0.8997	868.19
308.15	1.0000	871.33
313.15	0.0000	848.74
313.15	0.0503	848.97
313.15	0.1004	849.28
313.15	0.1501	849.65
313.15	0.1999	850.05
313.15	0.2499	850.49
313.15	0.3004	851.02
313.15	0.3502	851.58
313.15	0.3998	852.18
313.15	0.4490	852.83
313.15	0.5001	853.57
313.15	0.5502	854.4
313.15	0.6000	855.29
313.15	0.6503	856.26
313.15	0.7005	857.33
313.15	0.7499	858.44
313.15	0.8003	859.87
313.15	0.8499	861.27
313.15	0.9003	862.85
313.15	0.9504	864.3
313.15	1.0000	865.68

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetic acid, propyl ester (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
298.15	0.0000	0.0281
298.15	0.0996	0.0276
298.15	0.2006	0.0272
298.15	0.3006	0.0267
298.15	0.4003	0.0263
298.15	0.4985	0.0259
298.15	0.6001	0.0255
298.15	0.6987	0.0251
298.15	0.7983	0.0247
298.15	0.8995	0.0244
298.15	1.0000	0.0240
303.15	0.0000	0.0277
303.15	0.1000	0.0272
303.15	0.2012	0.0267
303.15	0.2995	0.0262
303.15	0.3998	0.0257
303.15	0.4996	0.0253
303.15	0.6004	0.0249
303.15	0.7007	0.0245
303.15	0.7987	0.0241
303.15	0.9009	0.0237
303.15	1.0000	0.0233
308.15	0.0000	0.0272
308.15	0.0985	0.0267
308.15	0.1992	0.0262
308.15	0.3018	0.0257
308.15	0.3991	0.0252
308.15	0.5009	0.0248
308.15	0.6012	0.0243
308.15	0.6997	0.0239
308.15	0.7983	0.0235
308.15	0.8997	0.0231
308.15	1.0000	0.0227
313.15	0.0000	0.0268
313.15	0.1004	0.0263
313.15	0.1999	0.0257
313.15	0.3004	0.0252
313.15	0.3998	0.0247
313.15	0.5001	0.0242
313.15	0.6000	0.0238
313.15	0.7005	0.0233
313.15	0.8003	0.0229
313.15	0.9003	0.0225
313.15	1.0000	0.0221

Sources

• Densities, surface tensions, and derived surface thermodynamics properties of (trimethylbenzene + propyl acetate, or butyl acetate) from T = 298.15 K to 313.15 K

Note: These property values are available through the Cheméo API. A free account gives you an access key.