Mixture of Benzene, nitro- + Methylene chloride

Datasets

1. ρ_l - Mass density, kg/m3 (2)

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Methylene chloride (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0210	288.15	1213.16
0.0210	293.15	1204.27
0.0210	298.15	1199.65
0.0210	303.15	1195.1
0.1053	288.15	1219.99
0.1053	293.15	1211.21
0.1053	298.15	1206.52
0.1053	303.15	1201.87
0.2003	288.15	1228.35
0.2003	293.15	1219.76
0.2003	298.15	1214.95
0.2003	303.15	1210.13
0.2499	288.15	1233.02
0.2499	293.15	1224.51
0.2499	298.15	1219.62
0.2499	303.15	1214.69
0.3003	288.15	1238.01
0.3003	293.15	1229.63
0.3003	298.15	1224.61
0.3003	303.15	1219.55
0.3521	288.15	1243.35
0.3521	293.15	1235.09
0.3521	298.15	1229.95
0.3521	303.15	1224.73
0.4025	288.15	1248.78
0.4025	293.15	1240.64
0.4025	298.15	1235.37
0.4025	303.15	1229.98
0.4492	288.15	1254.01
0.4492	293.15	1245.99
0.4492	298.15	1240.56
0.4492	303.15	1235.01
0.4975	288.15	1259.65
0.4975	293.15	1251.71
0.4975	298.15	1246.14
0.4975	303.15	1240.37
0.5512	288.15	1266.13
0.5512	293.15	1258.32
0.5512	298.15	1252.51
0.5512	303.15	1246.51
0.5995	288.15	1272.2
0.5995	293.15	1264.47
0.5995	298.15	1258.48
0.5995	303.15	1252.21
0.6495	288.15	1278.7
0.6495	293.15	1271.04
0.6495	298.15	1264.8
0.6495	303.15	1258.26
0.6999	288.15	1285.45
0.6999	293.15	1277.91
0.6999	298.15	1271.39
0.6999	303.15	1264.55
0.7496	288.15	1292.42
0.7496	293.15	1284.93
0.7496	298.15	1278.12
0.7496	303.15	1270.91
0.7990	288.15	1299.65
0.7990	293.15	1292.18
0.7990	298.15	1285.0
0.7990	303.15	1277.46
0.8501	288.15	1307.44
0.8501	293.15	1299.97
0.8501	298.15	1292.47
0.8501	303.15	1284.49
0.8975	288.15	1315.12
0.8975	293.15	1307.6
0.8975	298.15	1299.69
0.8975	303.15	1291.27
0.9798	288.15	1329.58
0.9798	293.15	1321.91
0.9798	298.15	1313.24
0.9798	303.15	1303.98

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Methylene chloride (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0210	288.15	1213.16
0.0210	293.15	1204.27
0.0210	298.15	1199.65
0.0210	303.15	1195.1
0.1053	288.15	1219.99
0.1053	293.15	1211.21
0.1053	298.15	1206.52
0.1053	303.15	1201.87
0.2003	288.15	1228.35
0.2003	293.15	1219.76
0.2003	298.15	1214.95
0.2003	303.15	1210.13
0.2499	288.15	1233.02
0.2499	293.15	1224.51
0.2499	298.15	1219.62
0.2499	303.15	1214.69
0.3003	288.15	1238.01
0.3003	293.15	1229.63
0.3003	298.15	1224.61
0.3003	303.15	1219.55
0.3521	288.15	1243.35
0.3521	293.15	1235.09
0.3521	298.15	1229.95
0.3521	303.15	1224.73
0.4025	288.15	1248.78
0.4025	293.15	1240.64
0.4025	298.15	1235.37
0.4025	303.15	1229.98
0.4492	288.15	1254.01
0.4492	293.15	1245.99
0.4492	298.15	1240.56
0.4492	303.15	1235.01
0.4975	288.15	1259.65
0.4975	293.15	1251.71
0.4975	298.15	1246.14
0.4975	303.15	1240.37
0.5512	288.15	1266.13
0.5512	293.15	1258.32
0.5512	298.15	1252.51
0.5512	303.15	1246.51
0.5995	288.15	1272.2
0.5995	293.15	1264.47
0.5995	298.15	1258.48
0.5995	303.15	1252.21
0.6495	288.15	1278.7
0.6495	293.15	1271.04
0.6495	298.15	1264.8
0.6495	303.15	1258.26
0.6999	288.15	1285.45
0.6999	293.15	1277.91
0.6999	298.15	1271.39
0.6999	303.15	1264.55
0.7496	288.15	1292.42
0.7496	293.15	1284.93
0.7496	298.15	1278.12
0.7496	303.15	1270.91
0.7990	288.15	1299.65
0.7990	293.15	1292.18
0.7990	298.15	1285.0
0.7990	303.15	1277.46
0.8501	288.15	1307.44
0.8501	293.15	1299.97
0.8501	298.15	1292.47
0.8501	303.15	1284.49
0.8975	288.15	1315.12
0.8975	293.15	1307.6
0.8975	298.15	1299.69
0.8975	303.15	1291.27
0.9798	288.15	1329.58
0.9798	293.15	1321.91
0.9798	298.15	1313.24
0.9798	303.15	1303.98

Sources

• Volumetric properties of dichloromethane with aniline or nitrobenzene at different temperatures: A theoretical and experimental study