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 p-Xylene (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of p-Xylene (1) - Liquid |
Activity coefficient of p-Xylene (1) - Liquid |
298.00 |
238.00 |
0.0000 |
5.2 |
Activity coefficient of p-Xylene (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of p-Xylene (1) - Liquid |
Activity coefficient of p-Xylene (1) - Liquid |
298.00 |
238.00 |
0.0000 |
5.2 |
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 |
0.0528 |
0.0006 |
298.15 |
0.1469 |
0.0007 |
298.15 |
0.2507 |
0.0007 |
298.15 |
0.3484 |
0.0007 |
298.15 |
0.4499 |
0.0008 |
298.15 |
0.4999 |
0.0008 |
298.15 |
0.5542 |
0.0009 |
298.15 |
0.6493 |
0.0010 |
298.15 |
0.7508 |
0.0011 |
298.15 |
0.8478 |
0.0013 |
298.15 |
0.9556 |
0.0015 |
308.15 |
0.0528 |
0.0005 |
308.15 |
0.1469 |
0.0006 |
308.15 |
0.2507 |
0.0006 |
308.15 |
0.3484 |
0.0006 |
308.15 |
0.4499 |
0.0007 |
308.15 |
0.4999 |
0.0007 |
308.15 |
0.5542 |
0.0008 |
308.15 |
0.6493 |
0.0008 |
308.15 |
0.7508 |
0.0009 |
308.15 |
0.8478 |
0.0010 |
308.15 |
0.9556 |
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 |
0.0528 |
0.0006 |
298.15 |
0.1469 |
0.0007 |
298.15 |
0.2507 |
0.0007 |
298.15 |
0.3484 |
0.0007 |
298.15 |
0.4499 |
0.0008 |
298.15 |
0.4999 |
0.0008 |
298.15 |
0.5542 |
0.0009 |
298.15 |
0.6493 |
0.0010 |
298.15 |
0.7508 |
0.0011 |
298.15 |
0.8478 |
0.0013 |
298.15 |
0.9556 |
0.0015 |
308.15 |
0.0528 |
0.0005 |
308.15 |
0.1469 |
0.0006 |
308.15 |
0.2507 |
0.0006 |
308.15 |
0.3484 |
0.0006 |
308.15 |
0.4499 |
0.0007 |
308.15 |
0.4999 |
0.0007 |
308.15 |
0.5542 |
0.0008 |
308.15 |
0.6493 |
0.0008 |
308.15 |
0.7508 |
0.0009 |
308.15 |
0.8478 |
0.0010 |
308.15 |
0.9556 |
0.0012 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mole fraction of p-Xylene (1) - Liquid |
Refractive index (Na D-line) - Liquid |
0.0499 |
1.4069 |
0.0999 |
1.4136 |
0.1999 |
1.4253 |
0.3000 |
1.4367 |
0.3999 |
1.4462 |
0.5001 |
1.4557 |
0.6000 |
1.4641 |
0.6999 |
1.4717 |
0.7999 |
1.4793 |
0.8999 |
1.4862 |
0.9499 |
1.4895 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mole fraction of p-Xylene (1) - Liquid |
Refractive index (Na D-line) - Liquid |
0.0499 |
1.4069 |
0.0999 |
1.4136 |
0.1999 |
1.4253 |
0.3000 |
1.4367 |
0.3999 |
1.4462 |
0.5001 |
1.4557 |
0.6000 |
1.4641 |
0.6999 |
1.4717 |
0.7999 |
1.4793 |
0.8999 |
1.4862 |
0.9499 |
1.4895 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mole fraction of p-Xylene (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0499 |
952.02 |
0.0999 |
944.39 |
0.1999 |
930.07 |
0.3000 |
917.28 |
0.3999 |
905.75 |
0.5001 |
895.38 |
0.6000 |
885.92 |
0.6999 |
877.19 |
0.7999 |
869.23 |
0.8999 |
862.2 |
0.9499 |
859.28 |
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 |
0.0528 |
859.41 |
298.15 |
0.1469 |
865.14 |
298.15 |
0.2507 |
872.58 |
298.15 |
0.3484 |
880.62 |
298.15 |
0.4499 |
890.02 |
298.15 |
0.4999 |
895.04 |
298.15 |
0.5542 |
900.79 |
298.15 |
0.6493 |
911.61 |
298.15 |
0.7508 |
924.23 |
298.15 |
0.8478 |
937.37 |
298.15 |
0.9556 |
953.27 |
303.15 |
0.0528 |
854.99 |
303.15 |
0.1469 |
860.67 |
303.15 |
0.2507 |
868.04 |
303.15 |
0.3484 |
876.02 |
303.15 |
0.4499 |
885.38 |
303.15 |
0.4999 |
890.38 |
303.15 |
0.5542 |
896.12 |
303.15 |
0.6493 |
906.92 |
303.15 |
0.7508 |
919.53 |
303.15 |
0.8478 |
932.67 |
303.15 |
0.9556 |
948.59 |
308.15 |
0.0528 |
850.64 |
308.15 |
0.1469 |
856.36 |
308.15 |
0.2507 |
863.8 |
308.15 |
0.3484 |
871.86 |
308.15 |
0.4499 |
881.33 |
308.15 |
0.4999 |
886.41 |
308.15 |
0.5542 |
892.23 |
308.15 |
0.6493 |
903.22 |
308.15 |
0.7508 |
916.11 |
308.15 |
0.8478 |
929.64 |
308.15 |
0.9556 |
946.21 |
313.15 |
0.0528 |
846.26 |
313.15 |
0.1469 |
851.72 |
313.15 |
0.2507 |
858.87 |
313.15 |
0.3484 |
866.67 |
313.15 |
0.4499 |
875.86 |
313.15 |
0.4999 |
880.79 |
313.15 |
0.5542 |
886.45 |
313.15 |
0.6493 |
897.16 |
313.15 |
0.7508 |
909.74 |
313.15 |
0.8478 |
922.96 |
313.15 |
0.9556 |
939.16 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mole fraction of p-Xylene (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0499 |
952.02 |
0.0999 |
944.39 |
0.1999 |
930.07 |
0.3000 |
917.28 |
0.3999 |
905.75 |
0.5001 |
895.38 |
0.6000 |
885.92 |
0.6999 |
877.19 |
0.7999 |
869.23 |
0.8999 |
862.2 |
0.9499 |
859.28 |
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 |
0.0528 |
859.41 |
298.15 |
0.1469 |
865.14 |
298.15 |
0.2507 |
872.58 |
298.15 |
0.3484 |
880.62 |
298.15 |
0.4499 |
890.02 |
298.15 |
0.4999 |
895.04 |
298.15 |
0.5542 |
900.79 |
298.15 |
0.6493 |
911.61 |
298.15 |
0.7508 |
924.23 |
298.15 |
0.8478 |
937.37 |
298.15 |
0.9556 |
953.27 |
303.15 |
0.0528 |
854.99 |
303.15 |
0.1469 |
860.67 |
303.15 |
0.2507 |
868.04 |
303.15 |
0.3484 |
876.02 |
303.15 |
0.4499 |
885.38 |
303.15 |
0.4999 |
890.38 |
303.15 |
0.5542 |
896.12 |
303.15 |
0.6493 |
906.92 |
303.15 |
0.7508 |
919.53 |
303.15 |
0.8478 |
932.67 |
303.15 |
0.9556 |
948.59 |
308.15 |
0.0528 |
850.64 |
308.15 |
0.1469 |
856.36 |
308.15 |
0.2507 |
863.8 |
308.15 |
0.3484 |
871.86 |
308.15 |
0.4499 |
881.33 |
308.15 |
0.4999 |
886.41 |
308.15 |
0.5542 |
892.23 |
308.15 |
0.6493 |
903.22 |
308.15 |
0.7508 |
916.11 |
308.15 |
0.8478 |
929.64 |
308.15 |
0.9556 |
946.21 |
313.15 |
0.0528 |
846.26 |
313.15 |
0.1469 |
851.72 |
313.15 |
0.2507 |
858.87 |
313.15 |
0.3484 |
866.67 |
313.15 |
0.4499 |
875.86 |
313.15 |
0.4999 |
880.79 |
313.15 |
0.5542 |
886.45 |
313.15 |
0.6493 |
897.16 |
313.15 |
0.7508 |
909.74 |
313.15 |
0.8478 |
922.96 |
313.15 |
0.9556 |
939.16 |
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 |
0.0528 |
1306.0 |
298.15 |
0.1469 |
1303.0 |
298.15 |
0.2507 |
1302.0 |
298.15 |
0.3484 |
1302.0 |
298.15 |
0.4499 |
1304.0 |
298.15 |
0.4999 |
1305.0 |
298.15 |
0.5542 |
1306.0 |
298.15 |
0.6493 |
1310.0 |
298.15 |
0.7508 |
1315.0 |
298.15 |
0.8478 |
1323.0 |
298.15 |
0.9556 |
1333.0 |
308.15 |
0.0528 |
1273.0 |
308.15 |
0.1469 |
1270.0 |
308.15 |
0.2507 |
1268.0 |
308.15 |
0.3484 |
1269.0 |
308.15 |
0.4499 |
1270.0 |
308.15 |
0.4999 |
1272.0 |
308.15 |
0.5542 |
1273.0 |
308.15 |
0.6493 |
1278.0 |
308.15 |
0.7508 |
1285.0 |
308.15 |
0.8478 |
1297.0 |
308.15 |
0.9556 |
1317.0 |
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 |
0.0528 |
1306.0 |
298.15 |
0.1469 |
1303.0 |
298.15 |
0.2507 |
1302.0 |
298.15 |
0.3484 |
1302.0 |
298.15 |
0.4499 |
1304.0 |
298.15 |
0.4999 |
1305.0 |
298.15 |
0.5542 |
1306.0 |
298.15 |
0.6493 |
1310.0 |
298.15 |
0.7508 |
1315.0 |
298.15 |
0.8478 |
1323.0 |
298.15 |
0.9556 |
1333.0 |
308.15 |
0.0528 |
1273.0 |
308.15 |
0.1469 |
1270.0 |
308.15 |
0.2507 |
1268.0 |
308.15 |
0.3484 |
1269.0 |
308.15 |
0.4499 |
1270.0 |
308.15 |
0.4999 |
1272.0 |
308.15 |
0.5542 |
1273.0 |
308.15 |
0.6493 |
1278.0 |
308.15 |
0.7508 |
1285.0 |
308.15 |
0.8478 |
1297.0 |
308.15 |
0.9556 |
1317.0 |
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