Datasets
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Activity coefficient (2)
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η - Viscosity, Pa*s (2)
-
ρl - Mass density, kg/m3 (2)
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csound,fluid - Speed of Sound, m/s (2)
Activity coefficient of o-Xylene (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of o-Xylene (2) - Liquid |
Activity coefficient of o-Xylene (2) - Liquid |
298.00 |
238.00 |
0.0000 |
5.0 |
Activity coefficient of o-Xylene (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of o-Xylene (2) - Liquid |
Activity coefficient of o-Xylene (2) - Liquid |
298.00 |
238.00 |
0.0000 |
5.0 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.0517 |
0.0008 |
298.15 |
0.1491 |
0.0008 |
298.15 |
0.2491 |
0.0008 |
298.15 |
0.3509 |
0.0009 |
298.15 |
0.4485 |
0.0009 |
298.15 |
0.4919 |
0.0010 |
298.15 |
0.5537 |
0.0010 |
298.15 |
0.6432 |
0.0011 |
298.15 |
0.7525 |
0.0012 |
298.15 |
0.8492 |
0.0013 |
298.15 |
0.9547 |
0.0015 |
308.15 |
0.0517 |
0.0007 |
308.15 |
0.1491 |
0.0007 |
308.15 |
0.2491 |
0.0007 |
308.15 |
0.3509 |
0.0007 |
308.15 |
0.4485 |
0.0008 |
308.15 |
0.4919 |
0.0008 |
308.15 |
0.5537 |
0.0008 |
308.15 |
0.6432 |
0.0009 |
308.15 |
0.7525 |
0.0010 |
308.15 |
0.8492 |
0.0011 |
308.15 |
0.9547 |
0.0012 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.0517 |
0.0008 |
298.15 |
0.1491 |
0.0008 |
298.15 |
0.2491 |
0.0008 |
298.15 |
0.3509 |
0.0009 |
298.15 |
0.4485 |
0.0009 |
298.15 |
0.4919 |
0.0010 |
298.15 |
0.5537 |
0.0010 |
298.15 |
0.6432 |
0.0011 |
298.15 |
0.7525 |
0.0012 |
298.15 |
0.8492 |
0.0013 |
298.15 |
0.9547 |
0.0015 |
308.15 |
0.0517 |
0.0007 |
308.15 |
0.1491 |
0.0007 |
308.15 |
0.2491 |
0.0007 |
308.15 |
0.3509 |
0.0007 |
308.15 |
0.4485 |
0.0008 |
308.15 |
0.4919 |
0.0008 |
308.15 |
0.5537 |
0.0008 |
308.15 |
0.6432 |
0.0009 |
308.15 |
0.7525 |
0.0010 |
308.15 |
0.8492 |
0.0011 |
308.15 |
0.9547 |
0.0012 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0517 |
877.85 |
298.15 |
0.1491 |
882.3 |
298.15 |
0.2491 |
887.92 |
298.15 |
0.3509 |
894.66 |
298.15 |
0.4485 |
902.02 |
298.15 |
0.4919 |
905.58 |
298.15 |
0.5537 |
910.92 |
298.15 |
0.6432 |
919.25 |
298.15 |
0.7525 |
930.41 |
298.15 |
0.8492 |
941.25 |
298.15 |
0.9547 |
954.25 |
303.15 |
0.0517 |
873.31 |
303.15 |
0.1491 |
877.45 |
303.15 |
0.2491 |
882.99 |
303.15 |
0.3509 |
889.79 |
303.15 |
0.4485 |
897.23 |
303.15 |
0.4919 |
900.8 |
303.15 |
0.5537 |
906.15 |
303.15 |
0.6432 |
914.44 |
303.15 |
0.7525 |
925.48 |
303.15 |
0.8492 |
936.23 |
303.15 |
0.9547 |
949.36 |
308.15 |
0.0517 |
869.04 |
308.15 |
0.1491 |
873.23 |
308.15 |
0.2491 |
878.8 |
308.15 |
0.3509 |
885.63 |
308.15 |
0.4485 |
893.14 |
308.15 |
0.4919 |
896.77 |
308.15 |
0.5537 |
902.22 |
308.15 |
0.6432 |
910.72 |
308.15 |
0.7525 |
922.15 |
308.15 |
0.8492 |
933.36 |
308.15 |
0.9547 |
947.07 |
313.15 |
0.0517 |
864.67 |
313.15 |
0.1491 |
868.58 |
313.15 |
0.2491 |
873.86 |
313.15 |
0.3509 |
880.35 |
313.15 |
0.4485 |
887.49 |
313.15 |
0.4919 |
890.93 |
313.15 |
0.5537 |
896.11 |
313.15 |
0.6432 |
904.2 |
313.15 |
0.7525 |
915.16 |
313.15 |
0.8492 |
926.06 |
313.15 |
0.9547 |
939.73 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0517 |
877.85 |
298.15 |
0.1491 |
882.3 |
298.15 |
0.2491 |
887.92 |
298.15 |
0.3509 |
894.66 |
298.15 |
0.4485 |
902.02 |
298.15 |
0.4919 |
905.58 |
298.15 |
0.5537 |
910.92 |
298.15 |
0.6432 |
919.25 |
298.15 |
0.7525 |
930.41 |
298.15 |
0.8492 |
941.25 |
298.15 |
0.9547 |
954.25 |
303.15 |
0.0517 |
873.31 |
303.15 |
0.1491 |
877.45 |
303.15 |
0.2491 |
882.99 |
303.15 |
0.3509 |
889.79 |
303.15 |
0.4485 |
897.23 |
303.15 |
0.4919 |
900.8 |
303.15 |
0.5537 |
906.15 |
303.15 |
0.6432 |
914.44 |
303.15 |
0.7525 |
925.48 |
303.15 |
0.8492 |
936.23 |
303.15 |
0.9547 |
949.36 |
308.15 |
0.0517 |
869.04 |
308.15 |
0.1491 |
873.23 |
308.15 |
0.2491 |
878.8 |
308.15 |
0.3509 |
885.63 |
308.15 |
0.4485 |
893.14 |
308.15 |
0.4919 |
896.77 |
308.15 |
0.5537 |
902.22 |
308.15 |
0.6432 |
910.72 |
308.15 |
0.7525 |
922.15 |
308.15 |
0.8492 |
933.36 |
308.15 |
0.9547 |
947.07 |
313.15 |
0.0517 |
864.67 |
313.15 |
0.1491 |
868.58 |
313.15 |
0.2491 |
873.86 |
313.15 |
0.3509 |
880.35 |
313.15 |
0.4485 |
887.49 |
313.15 |
0.4919 |
890.93 |
313.15 |
0.5537 |
896.11 |
313.15 |
0.6432 |
904.2 |
313.15 |
0.7525 |
915.16 |
313.15 |
0.8492 |
926.06 |
313.15 |
0.9547 |
939.73 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Speed of sound, m/s - Liquid |
298.15 |
0.0517 |
1342.0 |
298.15 |
0.1491 |
1337.0 |
298.15 |
0.2491 |
1333.0 |
298.15 |
0.3509 |
1330.0 |
298.15 |
0.4485 |
1328.0 |
298.15 |
0.4919 |
1328.0 |
298.15 |
0.5537 |
1328.0 |
298.15 |
0.6432 |
1329.0 |
298.15 |
0.7525 |
1331.0 |
298.15 |
0.8492 |
1333.0 |
298.15 |
0.9547 |
1337.0 |
308.15 |
0.0517 |
1314.0 |
308.15 |
0.1491 |
1303.0 |
308.15 |
0.2491 |
1298.0 |
308.15 |
0.3509 |
1295.0 |
308.15 |
0.4485 |
1295.0 |
308.15 |
0.4919 |
1295.0 |
308.15 |
0.5537 |
1295.0 |
308.15 |
0.6432 |
1297.0 |
308.15 |
0.7525 |
1301.0 |
308.15 |
0.8492 |
1308.0 |
308.15 |
0.9547 |
1320.0 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Speed of sound, m/s - Liquid |
298.15 |
0.0517 |
1342.0 |
298.15 |
0.1491 |
1337.0 |
298.15 |
0.2491 |
1333.0 |
298.15 |
0.3509 |
1330.0 |
298.15 |
0.4485 |
1328.0 |
298.15 |
0.4919 |
1328.0 |
298.15 |
0.5537 |
1328.0 |
298.15 |
0.6432 |
1329.0 |
298.15 |
0.7525 |
1331.0 |
298.15 |
0.8492 |
1333.0 |
298.15 |
0.9547 |
1337.0 |
308.15 |
0.0517 |
1314.0 |
308.15 |
0.1491 |
1303.0 |
308.15 |
0.2491 |
1298.0 |
308.15 |
0.3509 |
1295.0 |
308.15 |
0.4485 |
1295.0 |
308.15 |
0.4919 |
1295.0 |
308.15 |
0.5537 |
1295.0 |
308.15 |
0.6432 |
1297.0 |
308.15 |
0.7525 |
1301.0 |
308.15 |
0.8492 |
1308.0 |
308.15 |
0.9547 |
1320.0 |
Sources
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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