Mixture of Benzyl alcohol + 1-Butanol
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 (1) - Liquid |
Viscosity, Pa*s - Liquid |
0.0000 |
0.0026 |
0.0799 |
0.0027 |
0.1607 |
0.0028 |
0.2390 |
0.0029 |
0.3199 |
0.0031 |
0.3995 |
0.0032 |
0.4799 |
0.0034 |
0.5597 |
0.0037 |
0.6396 |
0.0039 |
0.7205 |
0.0042 |
0.8005 |
0.0045 |
0.8800 |
0.0049 |
0.9594 |
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 (1) - Liquid |
Viscosity, Pa*s - Liquid |
0.0000 |
0.0026 |
0.0799 |
0.0027 |
0.1607 |
0.0028 |
0.2390 |
0.0029 |
0.3199 |
0.0031 |
0.3995 |
0.0032 |
0.4799 |
0.0034 |
0.5597 |
0.0037 |
0.6396 |
0.0039 |
0.7205 |
0.0042 |
0.8005 |
0.0045 |
0.8800 |
0.0049 |
0.9594 |
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 (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0976 |
0.0849 |
0.1973 |
0.1489 |
0.2950 |
0.1961 |
0.3960 |
0.2211 |
0.4931 |
0.2311 |
0.6029 |
0.2121 |
0.7039 |
0.1790 |
0.8026 |
0.1328 |
0.9017 |
0.0726 |
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 (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0976 |
0.0849 |
0.1973 |
0.1489 |
0.2950 |
0.1961 |
0.3960 |
0.2211 |
0.4931 |
0.2311 |
0.6029 |
0.2121 |
0.7039 |
0.1790 |
0.8026 |
0.1328 |
0.9017 |
0.0726 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 81.5 (Liquid)
Mole fraction of Benzyl alcohol (1) - Liquid |
Refractive index (Na D-line) - Liquid |
0.0000 |
1.3969 |
0.0799 |
1.4097 |
0.1607 |
1.4224 |
0.2390 |
1.4346 |
0.3199 |
1.4469 |
0.3995 |
1.4588 |
0.4799 |
1.4705 |
0.5597 |
1.4816 |
0.6396 |
1.4924 |
0.7205 |
1.5032 |
0.8005 |
1.5137 |
0.8800 |
1.5238 |
0.9594 |
1.5333 |
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 (1) - Liquid |
Refractive index (Na D-line) - Liquid |
0.0000 |
1.3969 |
0.0799 |
1.4097 |
0.1607 |
1.4224 |
0.2390 |
1.4346 |
0.3199 |
1.4469 |
0.3995 |
1.4588 |
0.4799 |
1.4705 |
0.5597 |
1.4816 |
0.6396 |
1.4924 |
0.7205 |
1.5032 |
0.8005 |
1.5137 |
0.8800 |
1.5238 |
0.9594 |
1.5333 |
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 (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
806.07 |
0.0824 |
828.7 |
0.1602 |
849.52 |
0.2392 |
870.06 |
0.3206 |
890.78 |
0.3990 |
910.07 |
0.4803 |
929.52 |
0.5586 |
947.83 |
0.6394 |
966.22 |
0.7198 |
983.97 |
0.7993 |
1001.09 |
0.8813 |
1018.24 |
0.9604 |
1034.25 |
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 (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
806.07 |
0.0824 |
828.7 |
0.1602 |
849.52 |
0.2392 |
870.06 |
0.3206 |
890.78 |
0.3990 |
910.07 |
0.4803 |
929.52 |
0.5586 |
947.83 |
0.6394 |
966.22 |
0.7198 |
983.97 |
0.7993 |
1001.09 |
0.8813 |
1018.24 |
0.9604 |
1034.25 |
1.0000 |
1042.1 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1-Butanol (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
293.15 |
0.0000 |
0.0391 |
293.15 |
0.0034 |
0.0379 |
293.15 |
0.0044 |
0.0377 |
293.15 |
0.0071 |
0.0371 |
293.15 |
0.0117 |
0.0369 |
293.15 |
0.0213 |
0.0366 |
293.15 |
0.0303 |
0.0365 |
293.15 |
0.0492 |
0.0359 |
293.15 |
1.0000 |
0.0242 |
298.15 |
0.0000 |
0.0386 |
298.15 |
0.0034 |
0.0374 |
298.15 |
0.0044 |
0.0372 |
298.15 |
0.0071 |
0.0367 |
298.15 |
0.0117 |
0.0365 |
298.15 |
0.0213 |
0.0362 |
298.15 |
0.0303 |
0.0360 |
298.15 |
0.0492 |
0.0355 |
298.15 |
1.0000 |
0.0237 |
303.15 |
0.0000 |
0.0381 |
303.15 |
0.0034 |
0.0369 |
303.15 |
0.0044 |
0.0368 |
303.15 |
0.0071 |
0.0362 |
303.15 |
0.0117 |
0.0360 |
303.15 |
0.0213 |
0.0357 |
303.15 |
0.0303 |
0.0355 |
303.15 |
0.0492 |
0.0351 |
303.15 |
1.0000 |
0.0233 |
308.15 |
0.0000 |
0.0376 |
308.15 |
0.0034 |
0.0365 |
308.15 |
0.0044 |
0.0364 |
308.15 |
0.0071 |
0.0358 |
308.15 |
0.0117 |
0.0356 |
308.15 |
0.0213 |
0.0352 |
308.15 |
0.0303 |
0.0350 |
308.15 |
0.0492 |
0.0346 |
308.15 |
1.0000 |
0.0228 |
313.15 |
0.0000 |
0.0372 |
313.15 |
0.0034 |
0.0361 |
313.15 |
0.0044 |
0.0359 |
313.15 |
0.0071 |
0.0353 |
313.15 |
0.0117 |
0.0351 |
313.15 |
0.0213 |
0.0347 |
313.15 |
0.0303 |
0.0346 |
313.15 |
0.0492 |
0.0342 |
313.15 |
1.0000 |
0.0224 |
318.15 |
0.0000 |
0.0366 |
318.15 |
0.0034 |
0.0356 |
318.15 |
0.0044 |
0.0355 |
318.15 |
0.0071 |
0.0348 |
318.15 |
0.0117 |
0.0347 |
318.15 |
0.0213 |
0.0343 |
318.15 |
0.0303 |
0.0340 |
318.15 |
0.0492 |
0.0337 |
318.15 |
1.0000 |
0.0220 |
323.15 |
0.0000 |
0.0362 |
323.15 |
0.0034 |
0.0352 |
323.15 |
0.0044 |
0.0351 |
323.15 |
0.0071 |
0.0344 |
323.15 |
0.0117 |
0.0342 |
323.15 |
0.0213 |
0.0338 |
323.15 |
0.0303 |
0.0336 |
323.15 |
0.0492 |
0.0333 |
323.15 |
1.0000 |
0.0215 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1-Butanol (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
293.15 |
0.0000 |
0.0391 |
293.15 |
0.0034 |
0.0379 |
293.15 |
0.0044 |
0.0377 |
293.15 |
0.0071 |
0.0371 |
293.15 |
0.0117 |
0.0369 |
293.15 |
0.0213 |
0.0366 |
293.15 |
0.0303 |
0.0365 |
293.15 |
0.0492 |
0.0359 |
293.15 |
1.0000 |
0.0242 |
298.15 |
0.0000 |
0.0386 |
298.15 |
0.0034 |
0.0374 |
298.15 |
0.0044 |
0.0372 |
298.15 |
0.0071 |
0.0367 |
298.15 |
0.0117 |
0.0365 |
298.15 |
0.0213 |
0.0362 |
298.15 |
0.0303 |
0.0360 |
298.15 |
0.0492 |
0.0355 |
298.15 |
1.0000 |
0.0237 |
303.15 |
0.0000 |
0.0381 |
303.15 |
0.0034 |
0.0369 |
303.15 |
0.0044 |
0.0368 |
303.15 |
0.0071 |
0.0362 |
303.15 |
0.0117 |
0.0360 |
303.15 |
0.0213 |
0.0357 |
303.15 |
0.0303 |
0.0355 |
303.15 |
0.0492 |
0.0351 |
303.15 |
1.0000 |
0.0233 |
308.15 |
0.0000 |
0.0376 |
308.15 |
0.0034 |
0.0365 |
308.15 |
0.0044 |
0.0364 |
308.15 |
0.0071 |
0.0358 |
308.15 |
0.0117 |
0.0356 |
308.15 |
0.0213 |
0.0352 |
308.15 |
0.0303 |
0.0350 |
308.15 |
0.0492 |
0.0346 |
308.15 |
1.0000 |
0.0228 |
313.15 |
0.0000 |
0.0372 |
313.15 |
0.0034 |
0.0361 |
313.15 |
0.0044 |
0.0359 |
313.15 |
0.0071 |
0.0353 |
313.15 |
0.0117 |
0.0351 |
313.15 |
0.0213 |
0.0347 |
313.15 |
0.0303 |
0.0346 |
313.15 |
0.0492 |
0.0342 |
313.15 |
1.0000 |
0.0224 |
318.15 |
0.0000 |
0.0366 |
318.15 |
0.0034 |
0.0356 |
318.15 |
0.0044 |
0.0355 |
318.15 |
0.0071 |
0.0348 |
318.15 |
0.0117 |
0.0347 |
318.15 |
0.0213 |
0.0343 |
318.15 |
0.0303 |
0.0340 |
318.15 |
0.0492 |
0.0337 |
318.15 |
1.0000 |
0.0220 |
323.15 |
0.0000 |
0.0362 |
323.15 |
0.0034 |
0.0352 |
323.15 |
0.0044 |
0.0351 |
323.15 |
0.0071 |
0.0344 |
323.15 |
0.0117 |
0.0342 |
323.15 |
0.0213 |
0.0338 |
323.15 |
0.0303 |
0.0336 |
323.15 |
0.0492 |
0.0333 |
323.15 |
1.0000 |
0.0215 |
Sources