Datasets
-
Liquid-liquid equilibrium temperature, K (2)
-
γ - Surface tension liquid-gas, N/m (2)
Liquid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Mole fraction of Benzyl alcohol (1) - Liquid mixture 1 |
Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
| 0.2897 |
321.00 |
| 0.2968 |
321.39 |
| 0.3159 |
321.99 |
| 0.3319 |
322.37 |
| 0.3536 |
322.88 |
| 0.3537 |
322.89 |
| 0.3832 |
323.24 |
| 0.3923 |
323.37 |
| 0.3957 |
323.40 |
| 0.3984 |
323.41 |
| 0.4059 |
323.52 |
| 0.4336 |
323.63 |
| 0.4384 |
323.73 |
| 0.4478 |
323.64 |
| 0.4638 |
323.76 |
| 0.4683 |
323.70 |
| 0.4744 |
323.74 |
| 0.4875 |
323.71 |
| 0.4953 |
323.72 |
| 0.5019 |
323.68 |
| 0.5223 |
323.63 |
| 0.5384 |
323.54 |
| 0.5520 |
323.48 |
| 0.5657 |
323.36 |
| 0.5702 |
323.35 |
| 0.5822 |
323.25 |
| 0.5988 |
322.89 |
| 0.6036 |
322.89 |
| 0.6214 |
322.50 |
| 0.6297 |
322.13 |
| 0.6685 |
319.74 |
Liquid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Mole fraction of Benzyl alcohol (1) - Liquid mixture 1 |
Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
| 0.2897 |
321.00 |
| 0.2968 |
321.39 |
| 0.3159 |
321.99 |
| 0.3319 |
322.37 |
| 0.3536 |
322.88 |
| 0.3537 |
322.89 |
| 0.3832 |
323.24 |
| 0.3923 |
323.37 |
| 0.3957 |
323.40 |
| 0.3984 |
323.41 |
| 0.4059 |
323.52 |
| 0.4336 |
323.63 |
| 0.4384 |
323.73 |
| 0.4478 |
323.64 |
| 0.4638 |
323.76 |
| 0.4683 |
323.70 |
| 0.4744 |
323.74 |
| 0.4875 |
323.71 |
| 0.4953 |
323.72 |
| 0.5019 |
323.68 |
| 0.5223 |
323.63 |
| 0.5384 |
323.54 |
| 0.5520 |
323.48 |
| 0.5657 |
323.36 |
| 0.5702 |
323.35 |
| 0.5822 |
323.25 |
| 0.5988 |
322.89 |
| 0.6036 |
322.89 |
| 0.6214 |
322.50 |
| 0.6297 |
322.13 |
| 0.6685 |
319.74 |
Surface tension liquid-gas, N/m
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Heptane (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
| 293.15 |
0.0000 |
0.0391 |
| 293.15 |
0.0065 |
0.0378 |
| 293.15 |
0.0090 |
0.0371 |
| 293.15 |
0.0112 |
0.0344 |
| 293.15 |
0.0238 |
0.0336 |
| 293.15 |
0.0306 |
0.0324 |
| 293.15 |
0.0445 |
0.0288 |
| 293.15 |
0.0670 |
0.0261 |
| 293.15 |
1.0000 |
0.0200 |
| 298.15 |
0.0000 |
0.0386 |
| 298.15 |
0.0065 |
0.0375 |
| 298.15 |
0.0090 |
0.0369 |
| 298.15 |
0.0112 |
0.0347 |
| 298.15 |
0.0238 |
0.0338 |
| 298.15 |
0.0306 |
0.0326 |
| 298.15 |
0.0445 |
0.0292 |
| 298.15 |
0.0670 |
0.0265 |
| 298.15 |
1.0000 |
0.0195 |
| 303.15 |
0.0000 |
0.0381 |
| 303.15 |
0.0065 |
0.0371 |
| 303.15 |
0.0090 |
0.0366 |
| 303.15 |
0.0112 |
0.0350 |
| 303.15 |
0.0238 |
0.0340 |
| 303.15 |
0.0306 |
0.0328 |
| 303.15 |
0.0445 |
0.0294 |
| 303.15 |
0.0670 |
0.0269 |
| 303.15 |
1.0000 |
0.0191 |
| 308.15 |
0.0000 |
0.0376 |
| 308.15 |
0.0065 |
0.0368 |
| 308.15 |
0.0090 |
0.0364 |
| 308.15 |
0.0112 |
0.0353 |
| 308.15 |
0.0238 |
0.0343 |
| 308.15 |
0.0306 |
0.0330 |
| 308.15 |
0.0445 |
0.0297 |
| 308.15 |
0.0670 |
0.0273 |
| 308.15 |
1.0000 |
0.0186 |
| 313.15 |
0.0000 |
0.0372 |
| 313.15 |
0.0065 |
0.0365 |
| 313.15 |
0.0090 |
0.0362 |
| 313.15 |
0.0112 |
0.0355 |
| 313.15 |
0.0238 |
0.0345 |
| 313.15 |
0.0306 |
0.0332 |
| 313.15 |
0.0445 |
0.0300 |
| 313.15 |
0.0670 |
0.0277 |
| 313.15 |
1.0000 |
0.0181 |
| 318.15 |
0.0000 |
0.0366 |
| 318.15 |
0.0065 |
0.0362 |
| 318.15 |
0.0090 |
0.0360 |
| 318.15 |
0.0112 |
0.0358 |
| 318.15 |
0.0238 |
0.0347 |
| 318.15 |
0.0306 |
0.0335 |
| 318.15 |
0.0445 |
0.0303 |
| 318.15 |
0.0670 |
0.0281 |
| 318.15 |
1.0000 |
0.0176 |
| 323.15 |
0.0000 |
0.0362 |
| 323.15 |
0.0065 |
0.0359 |
| 323.15 |
0.0090 |
0.0357 |
| 323.15 |
0.0112 |
0.0361 |
| 323.15 |
0.0238 |
0.0350 |
| 323.15 |
0.0306 |
0.0337 |
| 323.15 |
0.0445 |
0.0306 |
| 323.15 |
0.0670 |
0.0285 |
| 323.15 |
1.0000 |
0.0171 |
Surface tension liquid-gas, N/m
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Heptane (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
| 293.15 |
0.0000 |
0.0391 |
| 293.15 |
0.0065 |
0.0378 |
| 293.15 |
0.0090 |
0.0371 |
| 293.15 |
0.0112 |
0.0344 |
| 293.15 |
0.0238 |
0.0336 |
| 293.15 |
0.0306 |
0.0324 |
| 293.15 |
0.0445 |
0.0288 |
| 293.15 |
0.0670 |
0.0261 |
| 293.15 |
1.0000 |
0.0200 |
| 298.15 |
0.0000 |
0.0386 |
| 298.15 |
0.0065 |
0.0375 |
| 298.15 |
0.0090 |
0.0369 |
| 298.15 |
0.0112 |
0.0347 |
| 298.15 |
0.0238 |
0.0338 |
| 298.15 |
0.0306 |
0.0326 |
| 298.15 |
0.0445 |
0.0292 |
| 298.15 |
0.0670 |
0.0265 |
| 298.15 |
1.0000 |
0.0195 |
| 303.15 |
0.0000 |
0.0381 |
| 303.15 |
0.0065 |
0.0371 |
| 303.15 |
0.0090 |
0.0366 |
| 303.15 |
0.0112 |
0.0350 |
| 303.15 |
0.0238 |
0.0340 |
| 303.15 |
0.0306 |
0.0328 |
| 303.15 |
0.0445 |
0.0294 |
| 303.15 |
0.0670 |
0.0269 |
| 303.15 |
1.0000 |
0.0191 |
| 308.15 |
0.0000 |
0.0376 |
| 308.15 |
0.0065 |
0.0368 |
| 308.15 |
0.0090 |
0.0364 |
| 308.15 |
0.0112 |
0.0353 |
| 308.15 |
0.0238 |
0.0343 |
| 308.15 |
0.0306 |
0.0330 |
| 308.15 |
0.0445 |
0.0297 |
| 308.15 |
0.0670 |
0.0273 |
| 308.15 |
1.0000 |
0.0186 |
| 313.15 |
0.0000 |
0.0372 |
| 313.15 |
0.0065 |
0.0365 |
| 313.15 |
0.0090 |
0.0362 |
| 313.15 |
0.0112 |
0.0355 |
| 313.15 |
0.0238 |
0.0345 |
| 313.15 |
0.0306 |
0.0332 |
| 313.15 |
0.0445 |
0.0300 |
| 313.15 |
0.0670 |
0.0277 |
| 313.15 |
1.0000 |
0.0181 |
| 318.15 |
0.0000 |
0.0366 |
| 318.15 |
0.0065 |
0.0362 |
| 318.15 |
0.0090 |
0.0360 |
| 318.15 |
0.0112 |
0.0358 |
| 318.15 |
0.0238 |
0.0347 |
| 318.15 |
0.0306 |
0.0335 |
| 318.15 |
0.0445 |
0.0303 |
| 318.15 |
0.0670 |
0.0281 |
| 318.15 |
1.0000 |
0.0176 |
| 323.15 |
0.0000 |
0.0362 |
| 323.15 |
0.0065 |
0.0359 |
| 323.15 |
0.0090 |
0.0357 |
| 323.15 |
0.0112 |
0.0361 |
| 323.15 |
0.0238 |
0.0350 |
| 323.15 |
0.0306 |
0.0337 |
| 323.15 |
0.0445 |
0.0306 |
| 323.15 |
0.0670 |
0.0285 |
| 323.15 |
1.0000 |
0.0171 |
Sources