Mixture of 2-Octanol + Ethane, 1,2-dichloro-

Datasets

1. ρ_l - Mass density, kg/m3

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Octanol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0499	1215.156
288.15	0.1000	1175.115
288.15	0.1503	1139.012
288.15	0.2006	1106.432
288.15	0.2498	1077.37
288.15	0.3002	1050.056
288.15	0.3500	1025.535
288.15	0.3999	1002.854
288.15	0.4499	981.685
288.15	0.4999	962.134
288.15	0.5503	943.764
288.15	0.5992	927.273
288.15	0.6492	911.359
288.15	0.6989	896.738
288.15	0.7503	882.325
288.15	0.7989	869.78
288.15	0.8497	857.292
288.15	0.8990	845.686
288.15	0.9492	834.672
293.15	0.0499	1208.222
293.15	0.1000	1168.447
293.15	0.1503	1132.674
293.15	0.2006	1100.332
293.15	0.2498	1071.555
293.15	0.3002	1044.592
293.15	0.3500	1020.164
293.15	0.3999	997.633
293.15	0.4499	976.658
293.15	0.4999	957.22
293.15	0.5503	939.011
293.15	0.5992	922.663
293.15	0.6492	906.886
293.15	0.6989	892.39
293.15	0.7503	878.102
293.15	0.7989	865.66
293.15	0.8497	853.282
293.15	0.8990	841.775
293.15	0.9492	830.858
298.15	0.0499	1201.269
298.15	0.1000	1161.758
298.15	0.1503	1126.333
298.15	0.2006	1094.177
298.15	0.2498	1065.657
298.15	0.3002	1038.959
298.15	0.3500	1014.696
298.15	0.3999	992.342
298.15	0.4499	971.558
298.15	0.4999	952.273
298.15	0.5503	934.225
298.15	0.5992	918.023
298.15	0.6492	902.382
298.15	0.6989	888.013
298.15	0.7503	873.846
298.15	0.7989	861.514
298.15	0.8497	849.241
298.15	0.8990	837.835
298.15	0.9492	827.012
303.15	0.0499	1194.287
303.15	0.1000	1155.049
303.15	0.1503	1119.848
303.15	0.2006	1087.986
303.15	0.2498	1059.713
303.15	0.3002	1033.255
303.15	0.3500	1009.18
303.15	0.3999	987.014
303.15	0.4499	966.415
303.15	0.4999	947.296
303.15	0.5503	929.407
303.15	0.5992	913.351
303.15	0.6492	897.844
303.15	0.6989	883.603
303.15	0.7503	869.558
303.15	0.7989	857.336
303.15	0.8497	845.167
303.15	0.8990	833.858
303.15	0.9492	823.127
308.15	0.0499	1187.274
308.15	0.1000	1148.31
308.15	0.1503	1113.381
308.15	0.2006	1081.764
308.15	0.2498	1053.728
308.15	0.3000	1027.492
308.15	0.3500	1003.621
308.15	0.3999	981.649
308.15	0.4499	961.229
308.15	0.4999	942.282
308.15	0.5503	924.551
308.15	0.5992	908.639
308.15	0.6492	893.27
308.15	0.6989	879.157
308.15	0.7503	865.235
308.15	0.7989	853.118
308.15	0.8497	841.058
308.15	0.8990	829.849
308.15	0.9492	819.211
313.15	0.0499	1180.235
313.15	0.1000	1141.54
313.15	0.1503	1106.886
313.15	0.2006	1075.512
313.15	0.2498	1047.71
313.15	0.3002	1021.693
313.15	0.3500	998.027
313.15	0.3999	976.252
313.15	0.4499	956.01
313.15	0.4999	937.233
313.15	0.5503	919.661
313.15	0.5992	903.897
313.15	0.6492	888.66
313.15	0.6989	874.674
313.15	0.7503	860.873
313.15	0.7989	848.865
313.15	0.8497	836.912
313.15	0.8990	825.799
313.15	0.9492	815.252

Sources

• Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure

Note: These property values are available through the Cheméo API. A free account gives you an access key.