Mixture of Isopropyl Alcohol + Ethane, 1,2-dichloro-

Datasets

1. ρ_l - Mass density, kg/m3 (4)

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Isopropyl Alcohol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0500	1235.817
288.15	0.1004	1211.741
288.15	0.1497	1188.259
288.15	0.2000	1164.606
288.15	0.2500	1141.224
288.15	0.3002	1117.875
288.15	0.3502	1094.706
288.15	0.4001	1071.465
288.15	0.4503	1048.285
288.15	0.4996	1025.407
288.15	0.5502	1002.001
288.15	0.6000	978.769
288.15	0.6498	955.713
288.15	0.7000	932.242
288.15	0.7500	908.934
288.15	0.7996	885.608
288.15	0.8495	861.973
288.15	0.8998	837.957
288.15	0.9497	813.892
293.15	0.0500	1228.611
293.15	0.1004	1204.56
293.15	0.1497	1181.191
293.15	0.2000	1157.641
293.15	0.2500	1134.37
293.15	0.3002	1111.145
293.15	0.3502	1088.108
293.15	0.4001	1065.131
293.15	0.4503	1042.071
293.15	0.4996	1019.317
293.15	0.5502	996.011
293.15	0.6000	972.943
293.15	0.6498	950.066
293.15	0.7000	926.773
293.15	0.7500	903.601
293.15	0.7996	880.568
293.15	0.8495	857.114
293.15	0.8998	833.329
293.15	0.9497	809.502
298.15	0.0500	1221.385
298.15	0.1004	1197.377
298.15	0.1497	1174.093
298.15	0.2000	1150.63
298.15	0.2500	1127.473
298.15	0.3002	1104.368
298.15	0.3502	1081.459
298.15	0.4001	1058.718
298.15	0.4503	1035.704
298.15	0.4996	1013.104
298.15	0.5502	989.957
298.15	0.6000	967.056
298.15	0.6498	944.351
298.15	0.7000	921.244
298.15	0.7500	898.262
298.15	0.7996	875.378
298.15	0.8495	852.182
298.15	0.8998	828.632
298.15	0.9497	805.032
303.15	0.0500	1214.129
303.15	0.1004	1190.169
303.15	0.1497	1166.955
303.15	0.2000	1143.585
303.15	0.2500	1120.533
303.15	0.3002	1097.544
303.15	0.3502	1074.758
303.15	0.4001	1052.152
303.15	0.4503	1029.279
303.15	0.4996	1006.83
303.15	0.5502	983.831
303.15	0.6000	961.099
303.15	0.6498	938.562
303.15	0.7000	915.641
303.15	0.7500	892.85
303.15	0.7996	870.212
303.15	0.8495	847.228
303.15	0.8998	823.858
303.15	0.9497	800.505
308.15	0.0500	1206.714
308.15	0.1004	1182.927
308.15	0.1497	1159.78
308.15	0.2000	1136.498
308.15	0.2500	1113.536
308.15	0.3002	1090.671
308.15	0.3502	1068.003
308.15	0.4001	1045.522
308.15	0.4503	1022.791
308.15	0.4996	1000.488
308.15	0.5502	977.648
308.15	0.6000	955.079
308.15	0.6498	932.714
308.15	0.7000	909.966
308.15	0.7500	887.36
308.15	0.7996	864.918
308.15	0.8495	842.144
308.15	0.8998	819.006
308.15	0.9497	795.891
313.15	0.0500	1199.456
313.15	0.1004	1175.66
313.15	0.1497	1152.57
313.15	0.2000	1129.371
313.15	0.2500	1106.499
313.15	0.3002	1083.745
313.15	0.3502	1061.19
313.15	0.4001	1038.828
313.15	0.4503	1016.232
313.15	0.4996	994.079
313.15	0.5502	971.39
313.15	0.6000	948.987
313.15	0.6498	926.783
313.15	0.7000	904.209
313.15	0.7500	881.789
313.15	0.7996	859.549
313.15	0.8495	836.984
313.15	0.8998	814.085
313.15	0.9497	791.195

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Isopropyl Alcohol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	1260.35
288.15	0.0500	1235.77
288.15	0.1500	1188.35
288.15	0.2500	1141.45
288.15	0.3500	1094.84
288.15	0.4500	1048.69
288.15	0.5000	1025.43
288.15	0.5500	1001.94
288.15	0.6500	955.61
288.15	0.7500	908.94
288.15	0.8490	862.18
288.15	0.9490	814.66
288.15	0.9500	814.18
288.15	1.0000	789.68
298.15	0.0000	1245.75
298.15	0.0500	1221.42
298.15	0.1500	1174.26
298.15	0.2500	1127.77
298.15	0.3500	1081.66
298.15	0.4500	1036.08
298.15	0.5000	1013.12
298.15	0.5500	989.96
298.15	0.6500	944.31
298.15	0.7500	898.38
298.15	0.8490	852.45
298.15	0.9490	805.84
298.15	0.9500	805.36
298.15	1.0000	781.08
308.15	0.0000	1231.16
308.15	0.0500	1206.94
308.15	0.1500	1160.0
308.15	0.2500	1113.89
308.15	0.3500	1068.25
308.15	0.4500	1023.22
308.15	0.5000	1000.56
308.15	0.5500	977.71
308.15	0.6500	932.73
308.15	0.7500	887.54
308.15	0.8490	842.41
308.15	0.9490	796.72
308.15	0.9500	796.25
308.15	1.0000	772.48
318.15	0.0000	1216.56
318.15	0.0500	1192.32
318.15	0.1500	1145.58
318.15	0.2500	1099.81
318.15	0.3500	1054.61
318.15	0.4500	1010.09
318.15	0.5000	987.72
318.15	0.5500	965.17
318.15	0.6500	920.85
318.15	0.7500	876.36
318.15	0.8490	832.03
318.15	0.9490	787.26
318.15	0.9500	786.79
318.15	1.0000	763.88

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Isopropyl Alcohol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0500	1235.817
288.15	0.1004	1211.741
288.15	0.1497	1188.259
288.15	0.2000	1164.606
288.15	0.2500	1141.224
288.15	0.3002	1117.875
288.15	0.3502	1094.706
288.15	0.4001	1071.465
288.15	0.4503	1048.285
288.15	0.4996	1025.407
288.15	0.5502	1002.001
288.15	0.6000	978.769
288.15	0.6498	955.713
288.15	0.7000	932.242
288.15	0.7500	908.934
288.15	0.7996	885.608
288.15	0.8495	861.973
288.15	0.8998	837.957
288.15	0.9497	813.892
293.15	0.0500	1228.611
293.15	0.1004	1204.56
293.15	0.1497	1181.191
293.15	0.2000	1157.641
293.15	0.2500	1134.37
293.15	0.3002	1111.145
293.15	0.3502	1088.108
293.15	0.4001	1065.131
293.15	0.4503	1042.071
293.15	0.4996	1019.317
293.15	0.5502	996.011
293.15	0.6000	972.943
293.15	0.6498	950.066
293.15	0.7000	926.773
293.15	0.7500	903.601
293.15	0.7996	880.568
293.15	0.8495	857.114
293.15	0.8998	833.329
293.15	0.9497	809.502
298.15	0.0500	1221.385
298.15	0.1004	1197.377
298.15	0.1497	1174.093
298.15	0.2000	1150.63
298.15	0.2500	1127.473
298.15	0.3002	1104.368
298.15	0.3502	1081.459
298.15	0.4001	1058.718
298.15	0.4503	1035.704
298.15	0.4996	1013.104
298.15	0.5502	989.957
298.15	0.6000	967.056
298.15	0.6498	944.351
298.15	0.7000	921.244
298.15	0.7500	898.262
298.15	0.7996	875.378
298.15	0.8495	852.182
298.15	0.8998	828.632
298.15	0.9497	805.032
303.15	0.0500	1214.129
303.15	0.1004	1190.169
303.15	0.1497	1166.955
303.15	0.2000	1143.585
303.15	0.2500	1120.533
303.15	0.3002	1097.544
303.15	0.3502	1074.758
303.15	0.4001	1052.152
303.15	0.4503	1029.279
303.15	0.4996	1006.83
303.15	0.5502	983.831
303.15	0.6000	961.099
303.15	0.6498	938.562
303.15	0.7000	915.641
303.15	0.7500	892.85
303.15	0.7996	870.212
303.15	0.8495	847.228
303.15	0.8998	823.858
303.15	0.9497	800.505
308.15	0.0500	1206.714
308.15	0.1004	1182.927
308.15	0.1497	1159.78
308.15	0.2000	1136.498
308.15	0.2500	1113.536
308.15	0.3002	1090.671
308.15	0.3502	1068.003
308.15	0.4001	1045.522
308.15	0.4503	1022.791
308.15	0.4996	1000.488
308.15	0.5502	977.648
308.15	0.6000	955.079
308.15	0.6498	932.714
308.15	0.7000	909.966
308.15	0.7500	887.36
308.15	0.7996	864.918
308.15	0.8495	842.144
308.15	0.8998	819.006
308.15	0.9497	795.891
313.15	0.0500	1199.456
313.15	0.1004	1175.66
313.15	0.1497	1152.57
313.15	0.2000	1129.371
313.15	0.2500	1106.499
313.15	0.3002	1083.745
313.15	0.3502	1061.19
313.15	0.4001	1038.828
313.15	0.4503	1016.232
313.15	0.4996	994.079
313.15	0.5502	971.39
313.15	0.6000	948.987
313.15	0.6498	926.783
313.15	0.7000	904.209
313.15	0.7500	881.789
313.15	0.7996	859.549
313.15	0.8495	836.984
313.15	0.8998	814.085
313.15	0.9497	791.195

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Isopropyl Alcohol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	1260.35
288.15	0.0500	1235.77
288.15	0.1500	1188.35
288.15	0.2500	1141.45
288.15	0.3500	1094.84
288.15	0.4500	1048.69
288.15	0.5000	1025.43
288.15	0.5500	1001.94
288.15	0.6500	955.61
288.15	0.7500	908.94
288.15	0.8490	862.18
288.15	0.9490	814.66
288.15	0.9500	814.18
288.15	1.0000	789.68
298.15	0.0000	1245.75
298.15	0.0500	1221.42
298.15	0.1500	1174.26
298.15	0.2500	1127.77
298.15	0.3500	1081.66
298.15	0.4500	1036.08
298.15	0.5000	1013.12
298.15	0.5500	989.96
298.15	0.6500	944.31
298.15	0.7500	898.38
298.15	0.8490	852.45
298.15	0.9490	805.84
298.15	0.9500	805.36
298.15	1.0000	781.08
308.15	0.0000	1231.16
308.15	0.0500	1206.94
308.15	0.1500	1160.0
308.15	0.2500	1113.89
308.15	0.3500	1068.25
308.15	0.4500	1023.22
308.15	0.5000	1000.56
308.15	0.5500	977.71
308.15	0.6500	932.73
308.15	0.7500	887.54
308.15	0.8490	842.41
308.15	0.9490	796.72
308.15	0.9500	796.25
308.15	1.0000	772.48
318.15	0.0000	1216.56
318.15	0.0500	1192.32
318.15	0.1500	1145.58
318.15	0.2500	1099.81
318.15	0.3500	1054.61
318.15	0.4500	1010.09
318.15	0.5000	987.72
318.15	0.5500	965.17
318.15	0.6500	920.85
318.15	0.7500	876.36
318.15	0.8490	832.03
318.15	0.9490	787.26
318.15	0.9500	786.79
318.15	1.0000	763.88

Sources

• Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
• Densities and Excess Molar Volumes for the Binary and Ternary Systems of (1,4-Dioxane, 1-Propanol or 2-Propanol, and 1,2-Dichloroethane) at T = (288.15 to 318.15) K. Experimental Measurements and Prigogine-Flory-Patterson Modeling