Mixture of 1-Propanol + Benzyl alcohol
Datasets
-
η - Viscosity, Pa*s (2)
-
Excess molar enthalpy (molar enthalpy (2)
-
n0 - Refractive index (Na D-line) (2)
-
ρl - Mass density, kg/m3 (2)
-
γ - Surface tension liquid-gas, N/m (2)
Viscosity, Pa*s
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 81.5 (Liquid)
Mole fraction of Benzyl alcohol (2) - Liquid |
Viscosity, Pa*s - Liquid |
0.0000 |
0.0019 |
0.0799 |
0.0021 |
0.1596 |
0.0023 |
0.2399 |
0.0025 |
0.3202 |
0.0027 |
0.3990 |
0.0029 |
0.4800 |
0.0032 |
0.5598 |
0.0035 |
0.6388 |
0.0038 |
0.7189 |
0.0041 |
0.7995 |
0.0045 |
0.8800 |
0.0048 |
0.9601 |
0.0052 |
1.0000 |
0.0054 |
Viscosity, Pa*s
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 81.5 (Liquid)
Mole fraction of Benzyl alcohol (2) - Liquid |
Viscosity, Pa*s - Liquid |
0.0000 |
0.0019 |
0.0799 |
0.0021 |
0.1596 |
0.0023 |
0.2399 |
0.0025 |
0.3202 |
0.0027 |
0.3990 |
0.0029 |
0.4800 |
0.0032 |
0.5598 |
0.0035 |
0.6388 |
0.0038 |
0.7189 |
0.0041 |
0.7995 |
0.0045 |
0.8800 |
0.0048 |
0.9601 |
0.0052 |
1.0000 |
0.0054 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Benzyl alcohol (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0984 |
0.0486 |
0.1964 |
0.0847 |
0.2873 |
0.1065 |
0.3999 |
0.1236 |
0.4987 |
0.1190 |
0.5993 |
0.1072 |
0.6983 |
0.0867 |
0.7996 |
0.0614 |
0.8988 |
0.0323 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Benzyl alcohol (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0984 |
0.0486 |
0.1964 |
0.0847 |
0.2873 |
0.1065 |
0.3999 |
0.1236 |
0.4987 |
0.1190 |
0.5993 |
0.1072 |
0.6983 |
0.0867 |
0.7996 |
0.0614 |
0.8988 |
0.0323 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 81.5 (Liquid)
Mole fraction of Benzyl alcohol (2) - Liquid |
Refractive index (Na D-line) - Liquid |
0.0000 |
1.3824 |
0.0799 |
1.3998 |
0.1596 |
1.416 |
0.2399 |
1.4315 |
0.3202 |
1.4462 |
0.3990 |
1.4596 |
0.4800 |
1.4722 |
0.5598 |
1.4841 |
0.6388 |
1.4953 |
0.7189 |
1.5058 |
0.7995 |
1.5158 |
0.8800 |
1.5255 |
0.9601 |
1.5342 |
1.0000 |
1.5381 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 81.5 (Liquid)
Mole fraction of Benzyl alcohol (2) - Liquid |
Refractive index (Na D-line) - Liquid |
0.0000 |
1.3824 |
0.0799 |
1.3998 |
0.1596 |
1.416 |
0.2399 |
1.4315 |
0.3202 |
1.4462 |
0.3990 |
1.4596 |
0.4800 |
1.4722 |
0.5598 |
1.4841 |
0.6388 |
1.4953 |
0.7189 |
1.5058 |
0.7995 |
1.5158 |
0.8800 |
1.5255 |
0.9601 |
1.5342 |
1.0000 |
1.5381 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 81.5 (Liquid)
Mole fraction of Benzyl alcohol (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
799.54 |
0.0794 |
827.12 |
0.1588 |
852.72 |
0.2407 |
877.46 |
0.3192 |
899.36 |
0.4006 |
920.71 |
0.4799 |
940.19 |
0.5591 |
958.41 |
0.6396 |
975.82 |
0.7200 |
992.09 |
0.8011 |
1007.73 |
0.8803 |
1022.02 |
0.9583 |
1035.3 |
1.0000 |
1042.1 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 81.5 (Liquid)
Mole fraction of Benzyl alcohol (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
799.54 |
0.0794 |
827.12 |
0.1588 |
852.72 |
0.2407 |
877.46 |
0.3192 |
899.36 |
0.4006 |
920.71 |
0.4799 |
940.19 |
0.5591 |
958.41 |
0.6396 |
975.82 |
0.7200 |
992.09 |
0.8011 |
1007.73 |
0.8803 |
1022.02 |
0.9583 |
1035.3 |
1.0000 |
1042.1 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1-Propanol (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
293.15 |
0.0000 |
0.0391 |
293.15 |
0.0030 |
0.0376 |
293.15 |
0.0062 |
0.0370 |
293.15 |
0.0077 |
0.0369 |
293.15 |
0.0116 |
0.0367 |
293.15 |
0.0212 |
0.0364 |
293.15 |
0.0326 |
0.0360 |
293.15 |
0.0498 |
0.0356 |
293.15 |
1.0000 |
0.0237 |
298.15 |
0.0000 |
0.0386 |
298.15 |
0.0030 |
0.0371 |
298.15 |
0.0062 |
0.0366 |
298.15 |
0.0077 |
0.0365 |
298.15 |
0.0116 |
0.0364 |
298.15 |
0.0212 |
0.0360 |
298.15 |
0.0326 |
0.0356 |
298.15 |
0.0498 |
0.0352 |
298.15 |
1.0000 |
0.0233 |
303.15 |
0.0000 |
0.0381 |
303.15 |
0.0030 |
0.0366 |
303.15 |
0.0062 |
0.0362 |
303.15 |
0.0077 |
0.0361 |
303.15 |
0.0116 |
0.0360 |
303.15 |
0.0212 |
0.0356 |
303.15 |
0.0326 |
0.0353 |
303.15 |
0.0498 |
0.0349 |
303.15 |
1.0000 |
0.0229 |
308.15 |
0.0000 |
0.0376 |
308.15 |
0.0030 |
0.0362 |
308.15 |
0.0062 |
0.0358 |
308.15 |
0.0077 |
0.0357 |
308.15 |
0.0116 |
0.0356 |
308.15 |
0.0212 |
0.0352 |
308.15 |
0.0326 |
0.0350 |
308.15 |
0.0498 |
0.0345 |
308.15 |
1.0000 |
0.0225 |
313.15 |
0.0000 |
0.0372 |
313.15 |
0.0030 |
0.0356 |
313.15 |
0.0062 |
0.0354 |
313.15 |
0.0077 |
0.0354 |
313.15 |
0.0116 |
0.0352 |
313.15 |
0.0212 |
0.0348 |
313.15 |
0.0326 |
0.0347 |
313.15 |
0.0498 |
0.0341 |
313.15 |
1.0000 |
0.0221 |
318.15 |
0.0000 |
0.0366 |
318.15 |
0.0030 |
0.0352 |
318.15 |
0.0062 |
0.0351 |
318.15 |
0.0077 |
0.0350 |
318.15 |
0.0116 |
0.0348 |
318.15 |
0.0212 |
0.0345 |
318.15 |
0.0326 |
0.0344 |
318.15 |
0.0498 |
0.0338 |
318.15 |
1.0000 |
0.0217 |
323.15 |
0.0000 |
0.0362 |
323.15 |
0.0030 |
0.0347 |
323.15 |
0.0062 |
0.0347 |
323.15 |
0.0077 |
0.0346 |
323.15 |
0.0116 |
0.0344 |
323.15 |
0.0212 |
0.0341 |
323.15 |
0.0326 |
0.0340 |
323.15 |
0.0498 |
0.0334 |
323.15 |
1.0000 |
0.0213 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1-Propanol (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
293.15 |
0.0000 |
0.0391 |
293.15 |
0.0030 |
0.0376 |
293.15 |
0.0062 |
0.0370 |
293.15 |
0.0077 |
0.0369 |
293.15 |
0.0116 |
0.0367 |
293.15 |
0.0212 |
0.0364 |
293.15 |
0.0326 |
0.0360 |
293.15 |
0.0498 |
0.0356 |
293.15 |
1.0000 |
0.0237 |
298.15 |
0.0000 |
0.0386 |
298.15 |
0.0030 |
0.0371 |
298.15 |
0.0062 |
0.0366 |
298.15 |
0.0077 |
0.0365 |
298.15 |
0.0116 |
0.0364 |
298.15 |
0.0212 |
0.0360 |
298.15 |
0.0326 |
0.0356 |
298.15 |
0.0498 |
0.0352 |
298.15 |
1.0000 |
0.0233 |
303.15 |
0.0000 |
0.0381 |
303.15 |
0.0030 |
0.0366 |
303.15 |
0.0062 |
0.0362 |
303.15 |
0.0077 |
0.0361 |
303.15 |
0.0116 |
0.0360 |
303.15 |
0.0212 |
0.0356 |
303.15 |
0.0326 |
0.0353 |
303.15 |
0.0498 |
0.0349 |
303.15 |
1.0000 |
0.0229 |
308.15 |
0.0000 |
0.0376 |
308.15 |
0.0030 |
0.0362 |
308.15 |
0.0062 |
0.0358 |
308.15 |
0.0077 |
0.0357 |
308.15 |
0.0116 |
0.0356 |
308.15 |
0.0212 |
0.0352 |
308.15 |
0.0326 |
0.0350 |
308.15 |
0.0498 |
0.0345 |
308.15 |
1.0000 |
0.0225 |
313.15 |
0.0000 |
0.0372 |
313.15 |
0.0030 |
0.0356 |
313.15 |
0.0062 |
0.0354 |
313.15 |
0.0077 |
0.0354 |
313.15 |
0.0116 |
0.0352 |
313.15 |
0.0212 |
0.0348 |
313.15 |
0.0326 |
0.0347 |
313.15 |
0.0498 |
0.0341 |
313.15 |
1.0000 |
0.0221 |
318.15 |
0.0000 |
0.0366 |
318.15 |
0.0030 |
0.0352 |
318.15 |
0.0062 |
0.0351 |
318.15 |
0.0077 |
0.0350 |
318.15 |
0.0116 |
0.0348 |
318.15 |
0.0212 |
0.0345 |
318.15 |
0.0326 |
0.0344 |
318.15 |
0.0498 |
0.0338 |
318.15 |
1.0000 |
0.0217 |
323.15 |
0.0000 |
0.0362 |
323.15 |
0.0030 |
0.0347 |
323.15 |
0.0062 |
0.0347 |
323.15 |
0.0077 |
0.0346 |
323.15 |
0.0116 |
0.0344 |
323.15 |
0.0212 |
0.0341 |
323.15 |
0.0326 |
0.0340 |
323.15 |
0.0498 |
0.0334 |
323.15 |
1.0000 |
0.0213 |
Sources