Mixture of Toluene + 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	0.0271	879.09
288.15	0.1555	917.4
288.15	0.2003	931.64
288.15	0.2513	948.51
288.15	0.2998	965.22
288.15	0.3489	982.93
288.15	0.4005	1002.49
288.15	0.4481	1021.37
288.15	0.4996	1042.87
288.15	0.5522	1066.09
288.15	0.5940	1085.51
288.15	0.6469	1111.44
288.15	0.7002	1139.2
288.15	0.7486	1166.0
288.15	0.7956	1193.51
288.15	0.8502	1227.59
288.15	0.9493	1295.7
288.15	0.9800	1318.61
293.15	0.0271	874.59
293.15	0.1555	912.71
293.15	0.2003	926.83
293.15	0.2513	943.54
293.15	0.2998	960.11
293.15	0.3489	977.63
293.15	0.4005	996.96
293.15	0.4481	1015.66
293.15	0.4996	1036.92
293.15	0.5522	1059.92
293.15	0.5940	1079.14
293.15	0.6469	1104.82
293.15	0.7002	1132.37
293.15	0.7486	1158.95
293.15	0.7956	1186.29
293.15	0.8502	1220.09
293.15	0.9493	1287.73
293.15	0.9800	1310.49
298.15	0.0271	869.5
298.15	0.1555	907.51
298.15	0.2003	921.52
298.15	0.2513	938.06
298.15	0.2998	954.44
298.15	0.3489	971.74
298.15	0.4005	990.84
298.15	0.4481	1009.3
298.15	0.4996	1030.32
298.15	0.5522	1053.04
298.15	0.5940	1072.11
298.15	0.6469	1097.55
298.15	0.7002	1124.86
298.15	0.7486	1151.23
298.15	0.7956	1178.38
298.15	0.8502	1211.97
298.15	0.9493	1279.01
298.15	0.9800	1301.5
303.15	0.0271	865.2
303.15	0.1555	903.09
303.15	0.2003	917.0
303.15	0.2513	933.27
303.15	0.2998	949.45
303.15	0.3489	966.55
303.15	0.4005	985.42
303.15	0.4481	1003.56
303.15	0.4996	1024.32
303.15	0.5522	1046.79
303.15	0.5940	1065.64
303.15	0.6469	1090.83
303.15	0.7002	1117.85
303.15	0.7486	1143.92
303.15	0.7956	1170.8
303.15	0.8502	1204.01
303.15	0.9493	1270.38
303.15	0.9800	1292.54

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	0.0271	879.09
288.15	0.1555	917.4
288.15	0.2003	931.64
288.15	0.2513	948.51
288.15	0.2998	965.22
288.15	0.3489	982.93
288.15	0.4005	1002.49
288.15	0.4481	1021.37
288.15	0.4996	1042.87
288.15	0.5522	1066.09
288.15	0.5940	1085.51
288.15	0.6469	1111.44
288.15	0.7002	1139.2
288.15	0.7486	1166.0
288.15	0.7956	1193.51
288.15	0.8502	1227.59
288.15	0.9493	1295.7
288.15	0.9800	1318.61
293.15	0.0271	874.59
293.15	0.1555	912.71
293.15	0.2003	926.83
293.15	0.2513	943.54
293.15	0.2998	960.11
293.15	0.3489	977.63
293.15	0.4005	996.96
293.15	0.4481	1015.66
293.15	0.4996	1036.92
293.15	0.5522	1059.92
293.15	0.5940	1079.14
293.15	0.6469	1104.82
293.15	0.7002	1132.37
293.15	0.7486	1158.95
293.15	0.7956	1186.29
293.15	0.8502	1220.09
293.15	0.9493	1287.73
293.15	0.9800	1310.49
298.15	0.0271	869.5
298.15	0.1555	907.51
298.15	0.2003	921.52
298.15	0.2513	938.06
298.15	0.2998	954.44
298.15	0.3489	971.74
298.15	0.4005	990.84
298.15	0.4481	1009.3
298.15	0.4996	1030.32
298.15	0.5522	1053.04
298.15	0.5940	1072.11
298.15	0.6469	1097.55
298.15	0.7002	1124.86
298.15	0.7486	1151.23
298.15	0.7956	1178.38
298.15	0.8502	1211.97
298.15	0.9493	1279.01
298.15	0.9800	1301.5
303.15	0.0271	865.2
303.15	0.1555	903.09
303.15	0.2003	917.0
303.15	0.2513	933.27
303.15	0.2998	949.45
303.15	0.3489	966.55
303.15	0.4005	985.42
303.15	0.4481	1003.56
303.15	0.4996	1024.32
303.15	0.5522	1046.79
303.15	0.5940	1065.64
303.15	0.6469	1090.83
303.15	0.7002	1117.85
303.15	0.7486	1143.92
303.15	0.7956	1170.8
303.15	0.8502	1204.01
303.15	0.9493	1270.38
303.15	0.9800	1292.54

Sources

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