Mixture of Ethanol + Benzene, chloro-

Datasets

1. ρ_l - Mass density, kg/m3 (2)

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	1111.811
288.15	0.0602	1100.531
288.15	0.0931	1094.316
288.15	0.1472	1083.66
288.15	0.1996	1072.894
288.15	0.2987	1051.093
288.15	0.3744	1032.841
288.15	0.4348	1017.246
288.15	0.4820	1004.395
288.15	0.4999	999.254
288.15	0.5964	969.834
288.15	0.6158	963.433
288.15	0.6990	934.443
288.15	0.7229	925.431
288.15	0.8006	893.996
288.15	0.8596	867.744
288.15	0.9091	843.565
288.15	0.9495	822.458
288.15	1.0000	793.721
293.15	0.0000	1106.428
293.15	0.0602	1095.098
293.15	0.0931	1088.877
293.15	0.1472	1078.236
293.15	0.1996	1067.48
293.15	0.2987	1045.725
293.15	0.3744	1027.521
293.15	0.4348	1011.974
293.15	0.4820	999.167
293.15	0.4999	994.043
293.15	0.5964	964.736
293.15	0.6158	958.357
293.15	0.6990	929.489
293.15	0.7229	920.521
293.15	0.8006	889.228
293.15	0.8596	863.105
293.15	0.9091	839.044
293.15	0.9495	818.046
293.15	1.0000	789.454
298.15	0.0000	1101.038
298.15	0.0602	1089.655
298.15	0.0931	1083.423
298.15	0.1472	1072.787
298.15	0.1996	1062.04
298.15	0.2987	1040.328
298.15	0.3744	1022.174
298.15	0.4348	1006.674
298.15	0.4820	993.907
298.15	0.4999	988.802
298.15	0.5964	959.603
298.15	0.6158	953.253
298.15	0.6990	924.505
298.15	0.7229	915.575
298.15	0.8006	884.43
298.15	0.8596	858.438
298.15	0.9091	834.501
298.15	0.9495	813.607
298.15	1.0000	785.164
303.15	0.0000	1095.64
303.15	0.0602	1084.2
303.15	0.0931	1077.955
303.15	0.1472	1067.316
303.15	0.1996	1056.58
303.15	0.2987	1034.905
303.15	0.3744	1016.793
303.15	0.4348	1001.338
303.15	0.4820	988.613
303.15	0.4999	983.525
303.15	0.5964	954.435
303.15	0.6158	948.111
303.15	0.6990	919.483
303.15	0.7229	910.595
303.15	0.8006	879.597
303.15	0.8596	853.737
303.15	0.9091	829.925
303.15	0.9495	809.136
303.15	1.0000	780.853
308.15	0.0000	1090.234
308.15	0.0602	1078.727
308.15	0.0931	1072.466
308.15	0.1472	1061.821
308.15	0.1996	1051.089
308.15	0.2987	1029.444
308.15	0.3744	1011.377
308.15	0.4348	995.963
308.15	0.4820	983.277
308.15	0.4999	978.206
308.15	0.5964	949.225
308.15	0.6158	942.928
308.15	0.6990	914.416
308.15	0.7229	905.569
308.15	0.8006	874.719
308.15	0.8596	848.997
308.15	0.9091	825.312
308.15	0.9495	804.63
308.15	1.0000	776.51
313.15	0.0000	1084.82
313.15	0.0602	1073.253
313.15	0.0931	1066.972
313.15	0.1472	1056.307
313.15	0.1996	1045.572
313.15	0.2987	1023.964
313.15	0.3744	1005.934
313.15	0.4348	990.561
313.15	0.4820	977.912
313.15	0.4999	972.862
313.15	0.5964	943.986
313.15	0.6158	937.714
313.15	0.6990	909.322
313.15	0.7229	900.513
313.15	0.8006	869.806
313.15	0.8596	844.234
313.15	0.9091	820.674
313.15	0.9495	800.088
313.15	1.0000	772.138

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	1111.811
288.15	0.0602	1100.531
288.15	0.0931	1094.316
288.15	0.1472	1083.66
288.15	0.1996	1072.894
288.15	0.2987	1051.093
288.15	0.3744	1032.841
288.15	0.4348	1017.246
288.15	0.4820	1004.395
288.15	0.4999	999.254
288.15	0.5964	969.834
288.15	0.6158	963.433
288.15	0.6990	934.443
288.15	0.7229	925.431
288.15	0.8006	893.996
288.15	0.8596	867.744
288.15	0.9091	843.565
288.15	0.9495	822.458
288.15	1.0000	793.721
293.15	0.0000	1106.428
293.15	0.0602	1095.098
293.15	0.0931	1088.877
293.15	0.1472	1078.236
293.15	0.1996	1067.48
293.15	0.2987	1045.725
293.15	0.3744	1027.521
293.15	0.4348	1011.974
293.15	0.4820	999.167
293.15	0.4999	994.043
293.15	0.5964	964.736
293.15	0.6158	958.357
293.15	0.6990	929.489
293.15	0.7229	920.521
293.15	0.8006	889.228
293.15	0.8596	863.105
293.15	0.9091	839.044
293.15	0.9495	818.046
293.15	1.0000	789.454
298.15	0.0000	1101.038
298.15	0.0602	1089.655
298.15	0.0931	1083.423
298.15	0.1472	1072.787
298.15	0.1996	1062.04
298.15	0.2987	1040.328
298.15	0.3744	1022.174
298.15	0.4348	1006.674
298.15	0.4820	993.907
298.15	0.4999	988.802
298.15	0.5964	959.603
298.15	0.6158	953.253
298.15	0.6990	924.505
298.15	0.7229	915.575
298.15	0.8006	884.43
298.15	0.8596	858.438
298.15	0.9091	834.501
298.15	0.9495	813.607
298.15	1.0000	785.164
303.15	0.0000	1095.64
303.15	0.0602	1084.2
303.15	0.0931	1077.955
303.15	0.1472	1067.316
303.15	0.1996	1056.58
303.15	0.2987	1034.905
303.15	0.3744	1016.793
303.15	0.4348	1001.338
303.15	0.4820	988.613
303.15	0.4999	983.525
303.15	0.5964	954.435
303.15	0.6158	948.111
303.15	0.6990	919.483
303.15	0.7229	910.595
303.15	0.8006	879.597
303.15	0.8596	853.737
303.15	0.9091	829.925
303.15	0.9495	809.136
303.15	1.0000	780.853
308.15	0.0000	1090.234
308.15	0.0602	1078.727
308.15	0.0931	1072.466
308.15	0.1472	1061.821
308.15	0.1996	1051.089
308.15	0.2987	1029.444
308.15	0.3744	1011.377
308.15	0.4348	995.963
308.15	0.4820	983.277
308.15	0.4999	978.206
308.15	0.5964	949.225
308.15	0.6158	942.928
308.15	0.6990	914.416
308.15	0.7229	905.569
308.15	0.8006	874.719
308.15	0.8596	848.997
308.15	0.9091	825.312
308.15	0.9495	804.63
308.15	1.0000	776.51
313.15	0.0000	1084.82
313.15	0.0602	1073.253
313.15	0.0931	1066.972
313.15	0.1472	1056.307
313.15	0.1996	1045.572
313.15	0.2987	1023.964
313.15	0.3744	1005.934
313.15	0.4348	990.561
313.15	0.4820	977.912
313.15	0.4999	972.862
313.15	0.5964	943.986
313.15	0.6158	937.714
313.15	0.6990	909.322
313.15	0.7229	900.513
313.15	0.8006	869.806
313.15	0.8596	844.234
313.15	0.9091	820.674
313.15	0.9495	800.088
313.15	1.0000	772.138

Sources

• Effect of temperature on the excess molar volumes of some alcohol + aromatic mixtures and modelling by cubic EOS mixing rules