Mixture of Benzyl alcohol + 1-Pentanol
Datasets
-
Excess molar enthalpy (molar enthalpy (2)
-
γ - Surface tension liquid-gas, N/m (2)
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 |
0.1044 |
0.0957 |
0.1968 |
0.1685 |
0.2902 |
0.2260 |
0.3864 |
0.2655 |
0.4838 |
0.2848 |
0.5999 |
0.2712 |
0.6988 |
0.2409 |
0.7995 |
0.1857 |
0.8992 |
0.1057 |
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 |
0.1044 |
0.0957 |
0.1968 |
0.1685 |
0.2902 |
0.2260 |
0.3864 |
0.2655 |
0.4838 |
0.2848 |
0.5999 |
0.2712 |
0.6988 |
0.2409 |
0.7995 |
0.1857 |
0.8992 |
0.1057 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1-Pentanol (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
293.15 |
0.0000 |
0.0391 |
293.15 |
0.0037 |
0.0369 |
293.15 |
0.0052 |
0.0367 |
293.15 |
0.0083 |
0.0366 |
293.15 |
0.0117 |
0.0364 |
293.15 |
0.0213 |
0.0359 |
293.15 |
0.0336 |
0.0356 |
293.15 |
0.0536 |
0.0352 |
293.15 |
1.0000 |
0.0257 |
298.15 |
0.0000 |
0.0386 |
298.15 |
0.0037 |
0.0364 |
298.15 |
0.0052 |
0.0363 |
298.15 |
0.0083 |
0.0361 |
298.15 |
0.0117 |
0.0359 |
298.15 |
0.0213 |
0.0355 |
298.15 |
0.0336 |
0.0352 |
298.15 |
0.0536 |
0.0348 |
298.15 |
1.0000 |
0.0253 |
303.15 |
0.0000 |
0.0381 |
303.15 |
0.0037 |
0.0360 |
303.15 |
0.0052 |
0.0359 |
303.15 |
0.0083 |
0.0357 |
303.15 |
0.0117 |
0.0355 |
303.15 |
0.0213 |
0.0350 |
303.15 |
0.0336 |
0.0348 |
303.15 |
0.0536 |
0.0343 |
303.15 |
1.0000 |
0.0249 |
308.15 |
0.0000 |
0.0376 |
308.15 |
0.0037 |
0.0356 |
308.15 |
0.0052 |
0.0355 |
308.15 |
0.0083 |
0.0353 |
308.15 |
0.0117 |
0.0351 |
308.15 |
0.0213 |
0.0346 |
308.15 |
0.0336 |
0.0343 |
308.15 |
0.0536 |
0.0338 |
308.15 |
1.0000 |
0.0245 |
313.15 |
0.0000 |
0.0372 |
313.15 |
0.0037 |
0.0353 |
313.15 |
0.0052 |
0.0351 |
313.15 |
0.0083 |
0.0349 |
313.15 |
0.0117 |
0.0347 |
313.15 |
0.0213 |
0.0342 |
313.15 |
0.0336 |
0.0340 |
313.15 |
0.0536 |
0.0333 |
313.15 |
1.0000 |
0.0241 |
318.15 |
0.0000 |
0.0366 |
318.15 |
0.0037 |
0.0349 |
318.15 |
0.0052 |
0.0347 |
318.15 |
0.0083 |
0.0345 |
318.15 |
0.0117 |
0.0343 |
318.15 |
0.0213 |
0.0338 |
318.15 |
0.0336 |
0.0335 |
318.15 |
0.0536 |
0.0330 |
318.15 |
1.0000 |
0.0237 |
323.15 |
0.0000 |
0.0362 |
323.15 |
0.0037 |
0.0345 |
323.15 |
0.0052 |
0.0343 |
323.15 |
0.0083 |
0.0340 |
323.15 |
0.0117 |
0.0339 |
323.15 |
0.0213 |
0.0334 |
323.15 |
0.0336 |
0.0331 |
323.15 |
0.0536 |
0.0324 |
323.15 |
1.0000 |
0.0233 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1-Pentanol (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
293.15 |
0.0000 |
0.0391 |
293.15 |
0.0037 |
0.0369 |
293.15 |
0.0052 |
0.0367 |
293.15 |
0.0083 |
0.0366 |
293.15 |
0.0117 |
0.0364 |
293.15 |
0.0213 |
0.0359 |
293.15 |
0.0336 |
0.0356 |
293.15 |
0.0536 |
0.0352 |
293.15 |
1.0000 |
0.0257 |
298.15 |
0.0000 |
0.0386 |
298.15 |
0.0037 |
0.0364 |
298.15 |
0.0052 |
0.0363 |
298.15 |
0.0083 |
0.0361 |
298.15 |
0.0117 |
0.0359 |
298.15 |
0.0213 |
0.0355 |
298.15 |
0.0336 |
0.0352 |
298.15 |
0.0536 |
0.0348 |
298.15 |
1.0000 |
0.0253 |
303.15 |
0.0000 |
0.0381 |
303.15 |
0.0037 |
0.0360 |
303.15 |
0.0052 |
0.0359 |
303.15 |
0.0083 |
0.0357 |
303.15 |
0.0117 |
0.0355 |
303.15 |
0.0213 |
0.0350 |
303.15 |
0.0336 |
0.0348 |
303.15 |
0.0536 |
0.0343 |
303.15 |
1.0000 |
0.0249 |
308.15 |
0.0000 |
0.0376 |
308.15 |
0.0037 |
0.0356 |
308.15 |
0.0052 |
0.0355 |
308.15 |
0.0083 |
0.0353 |
308.15 |
0.0117 |
0.0351 |
308.15 |
0.0213 |
0.0346 |
308.15 |
0.0336 |
0.0343 |
308.15 |
0.0536 |
0.0338 |
308.15 |
1.0000 |
0.0245 |
313.15 |
0.0000 |
0.0372 |
313.15 |
0.0037 |
0.0353 |
313.15 |
0.0052 |
0.0351 |
313.15 |
0.0083 |
0.0349 |
313.15 |
0.0117 |
0.0347 |
313.15 |
0.0213 |
0.0342 |
313.15 |
0.0336 |
0.0340 |
313.15 |
0.0536 |
0.0333 |
313.15 |
1.0000 |
0.0241 |
318.15 |
0.0000 |
0.0366 |
318.15 |
0.0037 |
0.0349 |
318.15 |
0.0052 |
0.0347 |
318.15 |
0.0083 |
0.0345 |
318.15 |
0.0117 |
0.0343 |
318.15 |
0.0213 |
0.0338 |
318.15 |
0.0336 |
0.0335 |
318.15 |
0.0536 |
0.0330 |
318.15 |
1.0000 |
0.0237 |
323.15 |
0.0000 |
0.0362 |
323.15 |
0.0037 |
0.0345 |
323.15 |
0.0052 |
0.0343 |
323.15 |
0.0083 |
0.0340 |
323.15 |
0.0117 |
0.0339 |
323.15 |
0.0213 |
0.0334 |
323.15 |
0.0336 |
0.0331 |
323.15 |
0.0536 |
0.0324 |
323.15 |
1.0000 |
0.0233 |
Sources