Datasets
-
Activity coefficient (2)
-
η - Viscosity, Pa*s (2)
-
ρl - Mass density, kg/m3 (2)
-
csound,fluid - Speed of Sound, m/s (2)
Activity coefficient of Benzene, 1,3-dimethyl- (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Benzene, 1,3-dimethyl- (2) - Liquid |
Activity coefficient of Benzene, 1,3-dimethyl- (2) - Liquid |
298.00 |
238.00 |
0.0000 |
5.2 |
Activity coefficient of Benzene, 1,3-dimethyl- (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Benzene, 1,3-dimethyl- (2) - Liquid |
Activity coefficient of Benzene, 1,3-dimethyl- (2) - 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- (1) - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.0519 |
0.0006 |
298.15 |
0.1498 |
0.0006 |
298.15 |
0.2504 |
0.0007 |
298.15 |
0.3476 |
0.0007 |
298.15 |
0.4520 |
0.0008 |
298.15 |
0.4991 |
0.0008 |
298.15 |
0.5538 |
0.0009 |
298.15 |
0.6476 |
0.0010 |
298.15 |
0.7504 |
0.0011 |
298.15 |
0.8491 |
0.0013 |
298.15 |
0.9558 |
0.0015 |
308.15 |
0.0519 |
0.0005 |
308.15 |
0.1498 |
0.0005 |
308.15 |
0.2504 |
0.0006 |
308.15 |
0.3476 |
0.0006 |
308.15 |
0.4520 |
0.0007 |
308.15 |
0.4991 |
0.0007 |
308.15 |
0.5538 |
0.0007 |
308.15 |
0.6476 |
0.0008 |
308.15 |
0.7504 |
0.0009 |
308.15 |
0.8491 |
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- (1) - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.0519 |
0.0006 |
298.15 |
0.1498 |
0.0006 |
298.15 |
0.2504 |
0.0007 |
298.15 |
0.3476 |
0.0007 |
298.15 |
0.4520 |
0.0008 |
298.15 |
0.4991 |
0.0008 |
298.15 |
0.5538 |
0.0009 |
298.15 |
0.6476 |
0.0010 |
298.15 |
0.7504 |
0.0011 |
298.15 |
0.8491 |
0.0013 |
298.15 |
0.9558 |
0.0015 |
308.15 |
0.0519 |
0.0005 |
308.15 |
0.1498 |
0.0005 |
308.15 |
0.2504 |
0.0006 |
308.15 |
0.3476 |
0.0006 |
308.15 |
0.4520 |
0.0007 |
308.15 |
0.4991 |
0.0007 |
308.15 |
0.5538 |
0.0007 |
308.15 |
0.6476 |
0.0008 |
308.15 |
0.7504 |
0.0009 |
308.15 |
0.8491 |
0.0010 |
308.15 |
0.9558 |
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 |
0.0519 |
862.4 |
298.15 |
0.1498 |
867.96 |
298.15 |
0.2504 |
874.92 |
298.15 |
0.3476 |
882.7 |
298.15 |
0.4520 |
892.1 |
298.15 |
0.4991 |
896.68 |
298.15 |
0.5538 |
902.24 |
298.15 |
0.6476 |
912.44 |
298.15 |
0.7504 |
924.64 |
298.15 |
0.8491 |
937.54 |
298.15 |
0.9558 |
953.14 |
303.15 |
0.0519 |
857.98 |
303.15 |
0.1498 |
863.28 |
303.15 |
0.2504 |
870.13 |
303.15 |
0.3476 |
877.91 |
303.15 |
0.4520 |
887.36 |
303.15 |
0.4991 |
891.97 |
303.15 |
0.5538 |
897.57 |
303.15 |
0.6476 |
907.82 |
303.15 |
0.7504 |
920.03 |
303.15 |
0.8491 |
932.9 |
303.15 |
0.9558 |
948.47 |
308.15 |
0.0519 |
853.64 |
308.15 |
0.1498 |
858.88 |
308.15 |
0.2504 |
865.82 |
308.15 |
0.3476 |
873.78 |
308.15 |
0.4520 |
883.47 |
308.15 |
0.4991 |
888.19 |
308.15 |
0.5538 |
893.92 |
308.15 |
0.6476 |
904.38 |
308.15 |
0.7504 |
916.84 |
308.15 |
0.8491 |
930.02 |
308.15 |
0.9558 |
946.12 |
313.15 |
0.0519 |
848.65 |
313.15 |
0.1498 |
853.65 |
313.15 |
0.2504 |
860.3 |
313.15 |
0.3476 |
867.96 |
313.15 |
0.4520 |
877.33 |
313.15 |
0.4991 |
881.91 |
313.15 |
0.5538 |
887.49 |
313.15 |
0.6476 |
897.71 |
313.15 |
0.7504 |
909.96 |
313.15 |
0.8491 |
922.98 |
313.15 |
0.9558 |
938.95 |
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 |
0.0519 |
862.4 |
298.15 |
0.1498 |
867.96 |
298.15 |
0.2504 |
874.92 |
298.15 |
0.3476 |
882.7 |
298.15 |
0.4520 |
892.1 |
298.15 |
0.4991 |
896.68 |
298.15 |
0.5538 |
902.24 |
298.15 |
0.6476 |
912.44 |
298.15 |
0.7504 |
924.64 |
298.15 |
0.8491 |
937.54 |
298.15 |
0.9558 |
953.14 |
303.15 |
0.0519 |
857.98 |
303.15 |
0.1498 |
863.28 |
303.15 |
0.2504 |
870.13 |
303.15 |
0.3476 |
877.91 |
303.15 |
0.4520 |
887.36 |
303.15 |
0.4991 |
891.97 |
303.15 |
0.5538 |
897.57 |
303.15 |
0.6476 |
907.82 |
303.15 |
0.7504 |
920.03 |
303.15 |
0.8491 |
932.9 |
303.15 |
0.9558 |
948.47 |
308.15 |
0.0519 |
853.64 |
308.15 |
0.1498 |
858.88 |
308.15 |
0.2504 |
865.82 |
308.15 |
0.3476 |
873.78 |
308.15 |
0.4520 |
883.47 |
308.15 |
0.4991 |
888.19 |
308.15 |
0.5538 |
893.92 |
308.15 |
0.6476 |
904.38 |
308.15 |
0.7504 |
916.84 |
308.15 |
0.8491 |
930.02 |
308.15 |
0.9558 |
946.12 |
313.15 |
0.0519 |
848.65 |
313.15 |
0.1498 |
853.65 |
313.15 |
0.2504 |
860.3 |
313.15 |
0.3476 |
867.96 |
313.15 |
0.4520 |
877.33 |
313.15 |
0.4991 |
881.91 |
313.15 |
0.5538 |
887.49 |
313.15 |
0.6476 |
897.71 |
313.15 |
0.7504 |
909.96 |
313.15 |
0.8491 |
922.98 |
313.15 |
0.9558 |
938.95 |
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 |
0.0519 |
1317.0 |
298.15 |
0.1498 |
1312.0 |
298.15 |
0.2504 |
1309.0 |
298.15 |
0.3476 |
1309.0 |
298.15 |
0.4520 |
1310.0 |
298.15 |
0.4991 |
1311.0 |
298.15 |
0.5538 |
1312.0 |
298.15 |
0.6476 |
1316.0 |
298.15 |
0.7504 |
1321.0 |
298.15 |
0.8491 |
1327.0 |
298.15 |
0.9558 |
1335.0 |
308.15 |
0.0519 |
1279.0 |
308.15 |
0.1498 |
1275.0 |
308.15 |
0.2504 |
1273.0 |
308.15 |
0.3476 |
1273.0 |
308.15 |
0.4520 |
1275.0 |
308.15 |
0.4991 |
1277.0 |
308.15 |
0.5538 |
1279.0 |
308.15 |
0.6476 |
1285.0 |
308.15 |
0.7504 |
1293.0 |
308.15 |
0.8491 |
1304.0 |
308.15 |
0.9558 |
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 |
0.0519 |
1317.0 |
298.15 |
0.1498 |
1312.0 |
298.15 |
0.2504 |
1309.0 |
298.15 |
0.3476 |
1309.0 |
298.15 |
0.4520 |
1310.0 |
298.15 |
0.4991 |
1311.0 |
298.15 |
0.5538 |
1312.0 |
298.15 |
0.6476 |
1316.0 |
298.15 |
0.7504 |
1321.0 |
298.15 |
0.8491 |
1327.0 |
298.15 |
0.9558 |
1335.0 |
308.15 |
0.0519 |
1279.0 |
308.15 |
0.1498 |
1275.0 |
308.15 |
0.2504 |
1273.0 |
308.15 |
0.3476 |
1273.0 |
308.15 |
0.4520 |
1275.0 |
308.15 |
0.4991 |
1277.0 |
308.15 |
0.5538 |
1279.0 |
308.15 |
0.6476 |
1285.0 |
308.15 |
0.7504 |
1293.0 |
308.15 |
0.8491 |
1304.0 |
308.15 |
0.9558 |
1320.0 |
Sources
-
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