Datasets
-
Activity coefficient (2)
-
Mole fraction (2)
-
η - Viscosity, Pa*s (2)
-
ρl - Mass density, kg/m3 (2)
-
csound,fluid - Speed of Sound, m/s (2)
-
Tboil - Boiling temperature at pressure P, K (2)
Activity coefficient of Ethylbenzene (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethylbenzene (2) - Liquid |
Activity coefficient of Ethylbenzene (2) - Liquid |
298.00 |
238.00 |
0.0000 |
4.9 |
Activity coefficient of Ethylbenzene (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethylbenzene (2) - Liquid |
Activity coefficient of Ethylbenzene (2) - Liquid |
298.00 |
238.00 |
0.0000 |
4.9 |
Mole fraction of Ethanol, 2-methoxy- (1)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Mole fraction of Ethanol, 2-methoxy- (1) - Gas |
0.9806 |
0.9499 |
0.9538 |
0.8951 |
0.9187 |
0.8419 |
0.8999 |
0.8187 |
0.8239 |
0.7379 |
0.7533 |
0.6878 |
0.6974 |
0.6543 |
0.6540 |
0.6418 |
0.5751 |
0.5998 |
0.5069 |
0.5712 |
0.4298 |
0.5426 |
0.2749 |
0.4821 |
0.1755 |
0.4167 |
0.1094 |
0.3412 |
0.0803 |
0.2913 |
0.0421 |
0.1938 |
Mole fraction of Ethanol, 2-methoxy- (1)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Mole fraction of Ethanol, 2-methoxy- (1) - Gas |
0.9806 |
0.9499 |
0.9538 |
0.8951 |
0.9187 |
0.8419 |
0.8999 |
0.8187 |
0.8239 |
0.7379 |
0.7533 |
0.6878 |
0.6974 |
0.6543 |
0.6540 |
0.6418 |
0.5751 |
0.5998 |
0.5069 |
0.5712 |
0.4298 |
0.5426 |
0.2749 |
0.4821 |
0.1755 |
0.4167 |
0.1094 |
0.3412 |
0.0803 |
0.2913 |
0.0421 |
0.1938 |
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 |
0.0558 |
0.0006 |
298.15 |
0.1525 |
0.0007 |
298.15 |
0.2511 |
0.0007 |
298.15 |
0.3504 |
0.0008 |
298.15 |
0.4525 |
0.0008 |
298.15 |
0.5021 |
0.0009 |
298.15 |
0.5522 |
0.0009 |
298.15 |
0.6499 |
0.0010 |
298.15 |
0.7500 |
0.0011 |
298.15 |
0.8530 |
0.0013 |
298.15 |
0.9546 |
0.0015 |
308.15 |
0.0558 |
0.0005 |
308.15 |
0.1525 |
0.0006 |
308.15 |
0.2511 |
0.0006 |
308.15 |
0.3504 |
0.0007 |
308.15 |
0.4525 |
0.0007 |
308.15 |
0.5021 |
0.0007 |
308.15 |
0.5522 |
0.0008 |
308.15 |
0.6499 |
0.0008 |
308.15 |
0.7500 |
0.0009 |
308.15 |
0.8530 |
0.0010 |
308.15 |
0.9546 |
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 |
0.0558 |
0.0006 |
298.15 |
0.1525 |
0.0007 |
298.15 |
0.2511 |
0.0007 |
298.15 |
0.3504 |
0.0008 |
298.15 |
0.4525 |
0.0008 |
298.15 |
0.5021 |
0.0009 |
298.15 |
0.5522 |
0.0009 |
298.15 |
0.6499 |
0.0010 |
298.15 |
0.7500 |
0.0011 |
298.15 |
0.8530 |
0.0013 |
298.15 |
0.9546 |
0.0015 |
308.15 |
0.0558 |
0.0005 |
308.15 |
0.1525 |
0.0006 |
308.15 |
0.2511 |
0.0006 |
308.15 |
0.3504 |
0.0007 |
308.15 |
0.4525 |
0.0007 |
308.15 |
0.5021 |
0.0007 |
308.15 |
0.5522 |
0.0008 |
308.15 |
0.6499 |
0.0008 |
308.15 |
0.7500 |
0.0009 |
308.15 |
0.8530 |
0.0010 |
308.15 |
0.9546 |
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 |
0.0558 |
865.14 |
298.15 |
0.1525 |
870.63 |
298.15 |
0.2511 |
877.35 |
298.15 |
0.3504 |
885.12 |
298.15 |
0.4525 |
894.08 |
298.15 |
0.5021 |
898.77 |
298.15 |
0.5522 |
903.72 |
298.15 |
0.6499 |
914.04 |
298.15 |
0.7500 |
925.58 |
298.15 |
0.8530 |
938.68 |
298.15 |
0.9546 |
953.16 |
303.15 |
0.0558 |
860.77 |
303.15 |
0.1525 |
866.09 |
303.15 |
0.2511 |
872.71 |
303.15 |
0.3504 |
880.46 |
303.15 |
0.4525 |
889.43 |
303.15 |
0.5021 |
894.13 |
303.15 |
0.5522 |
899.1 |
303.15 |
0.6499 |
909.44 |
303.15 |
0.7500 |
920.99 |
303.15 |
0.8530 |
934.07 |
303.15 |
0.9546 |
948.49 |
308.15 |
0.0558 |
856.53 |
308.15 |
0.1525 |
861.8 |
308.15 |
0.2511 |
868.48 |
308.15 |
0.3504 |
876.36 |
308.15 |
0.4525 |
885.52 |
308.15 |
0.5021 |
890.33 |
308.15 |
0.5522 |
895.42 |
308.15 |
0.6499 |
906.01 |
308.15 |
0.7500 |
917.85 |
308.15 |
0.8530 |
931.3 |
308.15 |
0.9546 |
946.21 |
313.15 |
0.0558 |
851.73 |
313.15 |
0.1525 |
856.78 |
313.15 |
0.2511 |
863.19 |
313.15 |
0.3504 |
870.77 |
313.15 |
0.4525 |
879.62 |
313.15 |
0.5021 |
884.28 |
313.15 |
0.5522 |
889.23 |
313.15 |
0.6499 |
899.57 |
313.15 |
0.7500 |
911.18 |
313.15 |
0.8530 |
924.42 |
313.15 |
0.9546 |
939.11 |
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 |
0.0558 |
865.14 |
298.15 |
0.1525 |
870.63 |
298.15 |
0.2511 |
877.35 |
298.15 |
0.3504 |
885.12 |
298.15 |
0.4525 |
894.08 |
298.15 |
0.5021 |
898.77 |
298.15 |
0.5522 |
903.72 |
298.15 |
0.6499 |
914.04 |
298.15 |
0.7500 |
925.58 |
298.15 |
0.8530 |
938.68 |
298.15 |
0.9546 |
953.16 |
303.15 |
0.0558 |
860.77 |
303.15 |
0.1525 |
866.09 |
303.15 |
0.2511 |
872.71 |
303.15 |
0.3504 |
880.46 |
303.15 |
0.4525 |
889.43 |
303.15 |
0.5021 |
894.13 |
303.15 |
0.5522 |
899.1 |
303.15 |
0.6499 |
909.44 |
303.15 |
0.7500 |
920.99 |
303.15 |
0.8530 |
934.07 |
303.15 |
0.9546 |
948.49 |
308.15 |
0.0558 |
856.53 |
308.15 |
0.1525 |
861.8 |
308.15 |
0.2511 |
868.48 |
308.15 |
0.3504 |
876.36 |
308.15 |
0.4525 |
885.52 |
308.15 |
0.5021 |
890.33 |
308.15 |
0.5522 |
895.42 |
308.15 |
0.6499 |
906.01 |
308.15 |
0.7500 |
917.85 |
308.15 |
0.8530 |
931.3 |
308.15 |
0.9546 |
946.21 |
313.15 |
0.0558 |
851.73 |
313.15 |
0.1525 |
856.78 |
313.15 |
0.2511 |
863.19 |
313.15 |
0.3504 |
870.77 |
313.15 |
0.4525 |
879.62 |
313.15 |
0.5021 |
884.28 |
313.15 |
0.5522 |
889.23 |
313.15 |
0.6499 |
899.57 |
313.15 |
0.7500 |
911.18 |
313.15 |
0.8530 |
924.42 |
313.15 |
0.9546 |
939.11 |
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 |
0.0558 |
1317.0 |
298.15 |
0.1525 |
1317.0 |
298.15 |
0.2511 |
1318.0 |
298.15 |
0.3504 |
1321.0 |
298.15 |
0.4525 |
1324.0 |
298.15 |
0.5021 |
1326.0 |
298.15 |
0.5522 |
1328.0 |
298.15 |
0.6499 |
1331.0 |
298.15 |
0.7500 |
1335.0 |
298.15 |
0.8530 |
1338.0 |
298.15 |
0.9546 |
1339.0 |
308.15 |
0.0558 |
1273.0 |
308.15 |
0.1525 |
1269.0 |
308.15 |
0.2511 |
1269.0 |
308.15 |
0.3504 |
1269.0 |
308.15 |
0.4525 |
1271.0 |
308.15 |
0.5021 |
1273.0 |
308.15 |
0.5522 |
1274.0 |
308.15 |
0.6499 |
1279.0 |
308.15 |
0.7500 |
1286.0 |
308.15 |
0.8530 |
1298.0 |
308.15 |
0.9546 |
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- (1) - Liquid |
Speed of sound, m/s - Liquid |
298.15 |
0.0558 |
1317.0 |
298.15 |
0.1525 |
1317.0 |
298.15 |
0.2511 |
1318.0 |
298.15 |
0.3504 |
1321.0 |
298.15 |
0.4525 |
1324.0 |
298.15 |
0.5021 |
1326.0 |
298.15 |
0.5522 |
1328.0 |
298.15 |
0.6499 |
1331.0 |
298.15 |
0.7500 |
1335.0 |
298.15 |
0.8530 |
1338.0 |
298.15 |
0.9546 |
1339.0 |
308.15 |
0.0558 |
1273.0 |
308.15 |
0.1525 |
1269.0 |
308.15 |
0.2511 |
1269.0 |
308.15 |
0.3504 |
1269.0 |
308.15 |
0.4525 |
1271.0 |
308.15 |
0.5021 |
1273.0 |
308.15 |
0.5522 |
1274.0 |
308.15 |
0.6499 |
1279.0 |
308.15 |
0.7500 |
1286.0 |
308.15 |
0.8530 |
1298.0 |
308.15 |
0.9546 |
1317.0 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.9806 |
396.20 |
0.9538 |
395.05 |
0.9187 |
393.91 |
0.8999 |
393.43 |
0.8239 |
392.09 |
0.7533 |
391.41 |
0.6974 |
391.12 |
0.6540 |
391.09 |
0.5751 |
391.08 |
0.5069 |
391.12 |
0.4298 |
391.32 |
0.2749 |
392.50 |
0.1755 |
394.38 |
0.1094 |
397.02 |
0.0803 |
398.70 |
0.0421 |
402.18 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mole fraction of Ethanol, 2-methoxy- (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.9806 |
396.20 |
0.9538 |
395.05 |
0.9187 |
393.91 |
0.8999 |
393.43 |
0.8239 |
392.09 |
0.7533 |
391.41 |
0.6974 |
391.12 |
0.6540 |
391.09 |
0.5751 |
391.08 |
0.5069 |
391.12 |
0.4298 |
391.32 |
0.2749 |
392.50 |
0.1755 |
394.38 |
0.1094 |
397.02 |
0.0803 |
398.70 |
0.0421 |
402.18 |
Sources
-
Thermodynamics of solvation in propylene glycol and methyl cellosolve
-
Isobaric Vapor-Liquid Equilibrium for Binary and Ternary Systems of 2-Methoxyethanol, Ethylbenzene, and Dimethyl Sulfoxide at 100.00 kPa
-
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