Mixture of Propanoic acid, butyl ester + Ethane, 1,2-dichloro-

Datasets

1. ρ_l - Mass density, kg/m3 (2)

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of Propanoic acid, butyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
0.0334	1222.24
0.0679	1199.39
0.1032	1177.4
0.1419	1154.78
0.1821	1132.96
0.2255	1110.88
0.2719	1088.82
0.3218	1066.84
0.3754	1044.9
0.4321	1023.34
0.4959	1001.02
0.5617	979.72
0.6360	957.49
0.7142	936.1
0.8040	913.62
0.8938	893.14

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of Propanoic acid, butyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
0.0334	1222.24
0.0679	1199.39
0.1032	1177.4
0.1419	1154.78
0.1821	1132.96
0.2255	1110.88
0.2719	1088.82
0.3218	1066.84
0.3754	1044.9
0.4321	1023.34
0.4959	1001.02
0.5617	979.72
0.6360	957.49
0.7142	936.1
0.8040	913.62
0.8938	893.14

Sources

• Thermodynamic study of (alkyl esters + a,x-alkyl dihalides)III. HE m and V E m for 20 binary mixtures {xCu-1H2u-1CO2C4H9 + (1 - x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 4, a = 1 and v = x = 2 to 6