Datasets
-
Activity coefficient (2)
-
η - Viscosity, Pa*s (2)
-
n0 - Refractive index (Na D-line) (2)
-
ρl - Mass density, kg/m3 (4)
-
csound,fluid - Speed of Sound, m/s (2)
Activity coefficient of Benzene (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Benzene (1) - Liquid |
Activity coefficient of Benzene (1) - Liquid |
298.00 |
238.00 |
0.0000 |
2.4 |
Activity coefficient of Benzene (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Benzene (1) - Liquid |
Activity coefficient of Benzene (1) - Liquid |
298.00 |
238.00 |
0.0000 |
2.4 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-methoxy- (2) - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.0543 |
0.0006 |
298.15 |
0.1499 |
0.0007 |
298.15 |
0.2235 |
0.0007 |
298.15 |
0.3508 |
0.0008 |
298.15 |
0.4496 |
0.0009 |
298.15 |
0.4961 |
0.0009 |
298.15 |
0.5462 |
0.0009 |
298.15 |
0.6455 |
0.0010 |
298.15 |
0.7524 |
0.0012 |
298.15 |
0.8509 |
0.0013 |
298.15 |
0.9558 |
0.0015 |
308.15 |
0.0543 |
0.0005 |
308.15 |
0.1499 |
0.0006 |
308.15 |
0.2235 |
0.0006 |
308.15 |
0.3508 |
0.0007 |
308.15 |
0.4496 |
0.0007 |
308.15 |
0.4961 |
0.0007 |
308.15 |
0.5462 |
0.0008 |
308.15 |
0.6455 |
0.0008 |
308.15 |
0.7524 |
0.0009 |
308.15 |
0.8509 |
0.0010 |
308.15 |
0.9558 |
0.0012 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-methoxy- (2) - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.0543 |
0.0006 |
298.15 |
0.1499 |
0.0007 |
298.15 |
0.2235 |
0.0007 |
298.15 |
0.3508 |
0.0008 |
298.15 |
0.4496 |
0.0009 |
298.15 |
0.4961 |
0.0009 |
298.15 |
0.5462 |
0.0009 |
298.15 |
0.6455 |
0.0010 |
298.15 |
0.7524 |
0.0012 |
298.15 |
0.8509 |
0.0013 |
298.15 |
0.9558 |
0.0015 |
308.15 |
0.0543 |
0.0005 |
308.15 |
0.1499 |
0.0006 |
308.15 |
0.2235 |
0.0006 |
308.15 |
0.3508 |
0.0007 |
308.15 |
0.4496 |
0.0007 |
308.15 |
0.4961 |
0.0007 |
308.15 |
0.5462 |
0.0008 |
308.15 |
0.6455 |
0.0008 |
308.15 |
0.7524 |
0.0009 |
308.15 |
0.8509 |
0.0010 |
308.15 |
0.9558 |
0.0012 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mole fraction of Benzene (1) - Liquid |
Refractive index (Na D-line) - Liquid |
0.0500 |
1.4054 |
0.0998 |
1.4105 |
0.2001 |
1.4193 |
0.2998 |
1.4286 |
0.4000 |
1.4385 |
0.4999 |
1.4486 |
0.5999 |
1.4586 |
0.7000 |
1.4679 |
0.8000 |
1.477 |
0.8998 |
1.4864 |
0.9500 |
1.4916 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mole fraction of Benzene (1) - Liquid |
Refractive index (Na D-line) - Liquid |
0.0500 |
1.4054 |
0.0998 |
1.4105 |
0.2001 |
1.4193 |
0.2998 |
1.4286 |
0.4000 |
1.4385 |
0.4999 |
1.4486 |
0.5999 |
1.4586 |
0.7000 |
1.4679 |
0.8000 |
1.477 |
0.8998 |
1.4864 |
0.9500 |
1.4916 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mole fraction of Benzene (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0500 |
955.11 |
0.0998 |
950.35 |
0.2001 |
940.54 |
0.2998 |
930.95 |
0.4000 |
921.55 |
0.4999 |
912.55 |
0.5999 |
903.8 |
0.7000 |
895.3 |
0.8000 |
887.18 |
0.8998 |
879.76 |
0.9500 |
876.36 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-methoxy- (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0543 |
877.11 |
298.15 |
0.1499 |
883.76 |
298.15 |
0.2235 |
889.28 |
298.15 |
0.3508 |
899.62 |
298.15 |
0.4496 |
908.25 |
298.15 |
0.4961 |
912.47 |
298.15 |
0.5462 |
917.12 |
298.15 |
0.6455 |
926.55 |
298.15 |
0.7524 |
936.89 |
298.15 |
0.8509 |
946.4 |
298.15 |
0.9558 |
956.26 |
303.15 |
0.0543 |
871.63 |
303.15 |
0.1499 |
878.21 |
303.15 |
0.2235 |
883.78 |
303.15 |
0.3508 |
894.22 |
303.15 |
0.4496 |
902.86 |
303.15 |
0.4961 |
907.05 |
303.15 |
0.5462 |
911.64 |
303.15 |
0.6455 |
920.92 |
303.15 |
0.7524 |
931.12 |
303.15 |
0.8509 |
940.7 |
303.15 |
0.9558 |
951.11 |
308.15 |
0.0543 |
866.32 |
308.15 |
0.1499 |
873.02 |
308.15 |
0.2235 |
878.73 |
308.15 |
0.3508 |
889.54 |
308.15 |
0.4496 |
898.52 |
308.15 |
0.4961 |
902.89 |
308.15 |
0.5462 |
907.68 |
308.15 |
0.6455 |
917.36 |
308.15 |
0.7524 |
928.02 |
308.15 |
0.8509 |
938.03 |
308.15 |
0.9558 |
948.89 |
313.15 |
0.0543 |
861.18 |
313.15 |
0.1499 |
867.61 |
313.15 |
0.2235 |
873.12 |
313.15 |
0.3508 |
883.55 |
313.15 |
0.4496 |
892.23 |
313.15 |
0.4961 |
896.45 |
313.15 |
0.5462 |
901.09 |
313.15 |
0.6455 |
910.48 |
313.15 |
0.7524 |
920.89 |
313.15 |
0.8509 |
930.74 |
313.15 |
0.9558 |
941.61 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mole fraction of Benzene (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0500 |
955.11 |
0.0998 |
950.35 |
0.2001 |
940.54 |
0.2998 |
930.95 |
0.4000 |
921.55 |
0.4999 |
912.55 |
0.5999 |
903.8 |
0.7000 |
895.3 |
0.8000 |
887.18 |
0.8998 |
879.76 |
0.9500 |
876.36 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-methoxy- (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0543 |
877.11 |
298.15 |
0.1499 |
883.76 |
298.15 |
0.2235 |
889.28 |
298.15 |
0.3508 |
899.62 |
298.15 |
0.4496 |
908.25 |
298.15 |
0.4961 |
912.47 |
298.15 |
0.5462 |
917.12 |
298.15 |
0.6455 |
926.55 |
298.15 |
0.7524 |
936.89 |
298.15 |
0.8509 |
946.4 |
298.15 |
0.9558 |
956.26 |
303.15 |
0.0543 |
871.63 |
303.15 |
0.1499 |
878.21 |
303.15 |
0.2235 |
883.78 |
303.15 |
0.3508 |
894.22 |
303.15 |
0.4496 |
902.86 |
303.15 |
0.4961 |
907.05 |
303.15 |
0.5462 |
911.64 |
303.15 |
0.6455 |
920.92 |
303.15 |
0.7524 |
931.12 |
303.15 |
0.8509 |
940.7 |
303.15 |
0.9558 |
951.11 |
308.15 |
0.0543 |
866.32 |
308.15 |
0.1499 |
873.02 |
308.15 |
0.2235 |
878.73 |
308.15 |
0.3508 |
889.54 |
308.15 |
0.4496 |
898.52 |
308.15 |
0.4961 |
902.89 |
308.15 |
0.5462 |
907.68 |
308.15 |
0.6455 |
917.36 |
308.15 |
0.7524 |
928.02 |
308.15 |
0.8509 |
938.03 |
308.15 |
0.9558 |
948.89 |
313.15 |
0.0543 |
861.18 |
313.15 |
0.1499 |
867.61 |
313.15 |
0.2235 |
873.12 |
313.15 |
0.3508 |
883.55 |
313.15 |
0.4496 |
892.23 |
313.15 |
0.4961 |
896.45 |
313.15 |
0.5462 |
901.09 |
313.15 |
0.6455 |
910.48 |
313.15 |
0.7524 |
920.89 |
313.15 |
0.8509 |
930.74 |
313.15 |
0.9558 |
941.61 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-methoxy- (2) - Liquid |
Speed of sound, m/s - Liquid |
298.15 |
0.0543 |
1294.0 |
298.15 |
0.1499 |
1290.0 |
298.15 |
0.2235 |
1289.0 |
298.15 |
0.3508 |
1291.0 |
298.15 |
0.4496 |
1295.0 |
298.15 |
0.4961 |
1297.0 |
298.15 |
0.5462 |
1300.0 |
298.15 |
0.6455 |
1306.0 |
298.15 |
0.7524 |
1314.0 |
298.15 |
0.8509 |
1323.0 |
298.15 |
0.9558 |
1334.0 |
308.15 |
0.0543 |
1258.0 |
308.15 |
0.1499 |
1256.0 |
308.15 |
0.2235 |
1256.0 |
308.15 |
0.3508 |
1258.0 |
308.15 |
0.4496 |
1263.0 |
308.15 |
0.4961 |
1265.0 |
308.15 |
0.5462 |
1269.0 |
308.15 |
0.6455 |
1277.0 |
308.15 |
0.7524 |
1289.0 |
308.15 |
0.8509 |
1302.0 |
308.15 |
0.9558 |
1319.0 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-methoxy- (2) - Liquid |
Speed of sound, m/s - Liquid |
298.15 |
0.0543 |
1294.0 |
298.15 |
0.1499 |
1290.0 |
298.15 |
0.2235 |
1289.0 |
298.15 |
0.3508 |
1291.0 |
298.15 |
0.4496 |
1295.0 |
298.15 |
0.4961 |
1297.0 |
298.15 |
0.5462 |
1300.0 |
298.15 |
0.6455 |
1306.0 |
298.15 |
0.7524 |
1314.0 |
298.15 |
0.8509 |
1323.0 |
298.15 |
0.9558 |
1334.0 |
308.15 |
0.0543 |
1258.0 |
308.15 |
0.1499 |
1256.0 |
308.15 |
0.2235 |
1256.0 |
308.15 |
0.3508 |
1258.0 |
308.15 |
0.4496 |
1263.0 |
308.15 |
0.4961 |
1265.0 |
308.15 |
0.5462 |
1269.0 |
308.15 |
0.6455 |
1277.0 |
308.15 |
0.7524 |
1289.0 |
308.15 |
0.8509 |
1302.0 |
308.15 |
0.9558 |
1319.0 |
Sources
-
Liquid liquid equilibria in the ternary systems {hexadecane + BTX aromatics + 2-methoxyethanol or acetonitrile} at 298.15 K
-
Thermodynamics of solvation in propylene glycol and methyl cellosolve
-
Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for CmH2m+1(OCH2CH2)nOH (m ) 1 or 2 or 4 andn ) 1) + Benzene, + Toluene, + (o-, m-, and p-) Xylenes, + Ethylbenzene, and + Cyclohexane