Mixture of Benzene + Methylene chloride

Datasets

1. ρ_l - Mass density, kg/m3 (2)

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methylene chloride (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0200	889.94
288.15	0.0513	899.72
288.15	0.1044	916.64
288.15	0.2131	953.62
288.15	0.3031	986.31
288.15	0.3524	1005.06
288.15	0.4026	1024.96
288.15	0.4491	1043.89
288.15	0.5040	1067.28
288.15	0.5505	1087.81
288.15	0.6466	1132.61
288.15	0.6873	1152.87
288.15	0.7494	1184.83
288.15	0.7851	1204.13
288.15	0.8533	1242.63
288.15	0.9002	1270.51
288.15	0.9497	1301.1
288.15	0.9791	1320.29
293.15	0.0200	882.89
293.15	0.0513	892.67
293.15	0.1044	909.62
293.15	0.2131	946.68
293.15	0.3031	979.53
293.15	0.3524	998.46
293.15	0.4026	1018.41
293.15	0.4491	1037.4
293.15	0.5040	1060.86
293.15	0.5505	1081.45
293.15	0.6466	1126.25
293.15	0.6873	1146.32
293.15	0.7494	1178.27
293.15	0.7851	1197.44
293.15	0.8533	1235.48
293.15	0.9002	1262.93
293.15	0.9497	1293.21
293.15	0.9791	1312.15
298.15	0.0200	879.5
298.15	0.0513	889.37
298.15	0.1044	906.38
298.15	0.2131	943.14
298.15	0.3031	975.81
298.15	0.3524	994.6
298.15	0.4026	1014.35
298.15	0.4491	1033.4
298.15	0.5040	1056.74
298.15	0.5505	1077.19
298.15	0.6466	1121.8
298.15	0.6873	1141.74
298.15	0.7494	1173.15
298.15	0.7851	1191.93
298.15	0.8533	1228.96
298.15	0.9002	1255.94
298.15	0.9497	1285.57
298.15	0.9791	1303.63
303.15	0.0200	874.89
303.15	0.0513	884.69
303.15	0.1044	901.72
303.15	0.2131	938.58
303.15	0.3031	971.12
303.15	0.3524	989.89
303.15	0.4026	1009.59
303.15	0.4491	1028.47
303.15	0.5040	1051.58
303.15	0.5505	1071.86
303.15	0.6466	1115.95
303.15	0.6873	1135.54
303.15	0.7494	1166.53
303.15	0.7851	1185.03
303.15	0.8533	1221.63
303.15	0.9002	1248.01
303.15	0.9497	1276.83
303.15	0.9791	1294.56

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methylene chloride (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0200	889.94
288.15	0.0513	899.72
288.15	0.1044	916.64
288.15	0.2131	953.62
288.15	0.3031	986.31
288.15	0.3524	1005.06
288.15	0.4026	1024.96
288.15	0.4491	1043.89
288.15	0.5040	1067.28
288.15	0.5505	1087.81
288.15	0.6466	1132.61
288.15	0.6873	1152.87
288.15	0.7494	1184.83
288.15	0.7851	1204.13
288.15	0.8533	1242.63
288.15	0.9002	1270.51
288.15	0.9497	1301.1
288.15	0.9791	1320.29
293.15	0.0200	882.89
293.15	0.0513	892.67
293.15	0.1044	909.62
293.15	0.2131	946.68
293.15	0.3031	979.53
293.15	0.3524	998.46
293.15	0.4026	1018.41
293.15	0.4491	1037.4
293.15	0.5040	1060.86
293.15	0.5505	1081.45
293.15	0.6466	1126.25
293.15	0.6873	1146.32
293.15	0.7494	1178.27
293.15	0.7851	1197.44
293.15	0.8533	1235.48
293.15	0.9002	1262.93
293.15	0.9497	1293.21
293.15	0.9791	1312.15
298.15	0.0200	879.5
298.15	0.0513	889.37
298.15	0.1044	906.38
298.15	0.2131	943.14
298.15	0.3031	975.81
298.15	0.3524	994.6
298.15	0.4026	1014.35
298.15	0.4491	1033.4
298.15	0.5040	1056.74
298.15	0.5505	1077.19
298.15	0.6466	1121.8
298.15	0.6873	1141.74
298.15	0.7494	1173.15
298.15	0.7851	1191.93
298.15	0.8533	1228.96
298.15	0.9002	1255.94
298.15	0.9497	1285.57
298.15	0.9791	1303.63
303.15	0.0200	874.89
303.15	0.0513	884.69
303.15	0.1044	901.72
303.15	0.2131	938.58
303.15	0.3031	971.12
303.15	0.3524	989.89
303.15	0.4026	1009.59
303.15	0.4491	1028.47
303.15	0.5040	1051.58
303.15	0.5505	1071.86
303.15	0.6466	1115.95
303.15	0.6873	1135.54
303.15	0.7494	1166.53
303.15	0.7851	1185.03
303.15	0.8533	1221.63
303.15	0.9002	1248.01
303.15	0.9497	1276.83
303.15	0.9791	1294.56

Sources

• Volumetric properties of binary liquid mixtures: Application of the Prigogine Flory Patterson theory to excess molar volumes of dichloromethane with benzene or toluene