Operational conditions:
| Mole fraction of Acetic acid, butyl ester (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.1520 | -0.0292 |
| 0.1873 | -0.0360 |
| 0.2873 | -0.0500 |
| 0.3922 | -0.0571 |
| 0.4465 | -0.0600 |
| 0.5020 | -0.0618 |
| 0.5430 | -0.0630 |
| 0.6000 | -0.0620 |
| 0.7435 | -0.0520 |
| 0.8705 | -0.0360 |
| 0.8898 | -0.0320 |
Operational conditions:
| Mole fraction of Acetic acid, butyl ester (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.1520 | -0.0292 |
| 0.1873 | -0.0360 |
| 0.2873 | -0.0500 |
| 0.3922 | -0.0571 |
| 0.4465 | -0.0600 |
| 0.5020 | -0.0618 |
| 0.5430 | -0.0630 |
| 0.6000 | -0.0620 |
| 0.7435 | -0.0520 |
| 0.8705 | -0.0360 |
| 0.8898 | -0.0320 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Acetic acid, butyl ester (2) - Liquid | Temperature, K - Liquid | Refractive index (Na D-line) - Liquid |
| 0.0499 | 293.15 | 1.4904 |
| 0.0499 | 298.15 | 1.4876 |
| 0.0499 | 303.15 | 1.4847 |
| 0.0499 | 308.15 | 1.4818 |
| 0.0499 | 313.15 | 1.4789 |
| 0.0998 | 293.15 | 1.4843 |
| 0.0998 | 298.15 | 1.4815 |
| 0.0998 | 303.15 | 1.4786 |
| 0.0998 | 308.15 | 1.4757 |
| 0.0998 | 313.15 | 1.4728 |
| 0.1500 | 293.15 | 1.4782 |
| 0.1500 | 298.15 | 1.4754 |
| 0.1500 | 303.15 | 1.4725 |
| 0.1500 | 308.15 | 1.4697 |
| 0.1500 | 313.15 | 1.4668 |
| 0.2001 | 293.15 | 1.4722 |
| 0.2001 | 298.15 | 1.4695 |
| 0.2001 | 303.15 | 1.4667 |
| 0.2001 | 308.15 | 1.4638 |
| 0.2001 | 313.15 | 1.461 |
| 0.2502 | 293.15 | 1.4664 |
| 0.2502 | 298.15 | 1.4636 |
| 0.2502 | 303.15 | 1.4608 |
| 0.2502 | 308.15 | 1.4581 |
| 0.2502 | 313.15 | 1.4553 |
| 0.2985 | 293.15 | 1.461 |
| 0.2985 | 298.15 | 1.4583 |
| 0.2985 | 303.15 | 1.4555 |
| 0.2985 | 308.15 | 1.4528 |
| 0.2985 | 313.15 | 1.4501 |
| 0.3447 | 293.15 | 1.4559 |
| 0.3447 | 298.15 | 1.4532 |
| 0.3447 | 303.15 | 1.4504 |
| 0.3447 | 308.15 | 1.4477 |
| 0.3447 | 313.15 | 1.4449 |
| 0.4011 | 293.15 | 1.4498 |
| 0.4011 | 298.15 | 1.447 |
| 0.4011 | 303.15 | 1.4443 |
| 0.4011 | 308.15 | 1.4416 |
| 0.4011 | 313.15 | 1.4389 |
| 0.4468 | 293.15 | 1.445 |
| 0.4468 | 298.15 | 1.4424 |
| 0.4468 | 303.15 | 1.4397 |
| 0.4468 | 308.15 | 1.4369 |
| 0.4468 | 313.15 | 1.4342 |
| 0.4994 | 293.15 | 1.4396 |
| 0.4994 | 298.15 | 1.437 |
| 0.4994 | 303.15 | 1.4343 |
| 0.4994 | 308.15 | 1.4316 |
| 0.4994 | 313.15 | 1.4289 |
| 0.5524 | 293.15 | 1.4343 |
| 0.5524 | 298.15 | 1.4317 |
| 0.5524 | 303.15 | 1.429 |
| 0.5524 | 308.15 | 1.4263 |
| 0.5524 | 313.15 | 1.4237 |
| 0.5999 | 293.15 | 1.4296 |
| 0.5999 | 298.15 | 1.4269 |
| 0.5999 | 303.15 | 1.4243 |
| 0.5999 | 308.15 | 1.4216 |
| 0.5999 | 313.15 | 1.419 |
| 0.6517 | 293.15 | 1.4247 |
| 0.6517 | 298.15 | 1.4221 |
| 0.6517 | 303.15 | 1.4194 |
| 0.6517 | 308.15 | 1.4168 |
| 0.6517 | 313.15 | 1.4142 |
| 0.7000 | 293.15 | 1.4202 |
| 0.7000 | 298.15 | 1.4176 |
| 0.7000 | 303.15 | 1.415 |
| 0.7000 | 308.15 | 1.4123 |
| 0.7000 | 313.15 | 1.4097 |
| 0.7516 | 293.15 | 1.4155 |
| 0.7516 | 298.15 | 1.4129 |
| 0.7516 | 303.15 | 1.4103 |
| 0.7516 | 308.15 | 1.4077 |
| 0.7516 | 313.15 | 1.4051 |
| 0.7972 | 293.15 | 1.4114 |
| 0.7972 | 298.15 | 1.4089 |
| 0.7972 | 303.15 | 1.4063 |
| 0.7972 | 308.15 | 1.4037 |
| 0.7972 | 313.15 | 1.4012 |
| 0.8404 | 293.15 | 1.4076 |
| 0.8404 | 298.15 | 1.4051 |
| 0.8404 | 303.15 | 1.4025 |
| 0.8404 | 308.15 | 1.3999 |
| 0.8404 | 313.15 | 1.3974 |
| 0.8971 | 293.15 | 1.4027 |
| 0.8971 | 298.15 | 1.4002 |
| 0.8971 | 303.15 | 1.3978 |
| 0.8971 | 308.15 | 1.3952 |
| 0.8971 | 313.15 | 1.3926 |
| 0.9449 | 293.15 | 1.3988 |
| 0.9449 | 298.15 | 1.3963 |
| 0.9449 | 303.15 | 1.3938 |
| 0.9449 | 308.15 | 1.3913 |
| 0.9449 | 313.15 | 1.3888 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Acetic acid, butyl ester (2) - Liquid | Temperature, K - Liquid | Refractive index (Na D-line) - Liquid |
| 0.0499 | 293.15 | 1.4904 |
| 0.0499 | 298.15 | 1.4876 |
| 0.0499 | 303.15 | 1.4847 |
| 0.0499 | 308.15 | 1.4818 |
| 0.0499 | 313.15 | 1.4789 |
| 0.0998 | 293.15 | 1.4843 |
| 0.0998 | 298.15 | 1.4815 |
| 0.0998 | 303.15 | 1.4786 |
| 0.0998 | 308.15 | 1.4757 |
| 0.0998 | 313.15 | 1.4728 |
| 0.1500 | 293.15 | 1.4782 |
| 0.1500 | 298.15 | 1.4754 |
| 0.1500 | 303.15 | 1.4725 |
| 0.1500 | 308.15 | 1.4697 |
| 0.1500 | 313.15 | 1.4668 |
| 0.2001 | 293.15 | 1.4722 |
| 0.2001 | 298.15 | 1.4695 |
| 0.2001 | 303.15 | 1.4667 |
| 0.2001 | 308.15 | 1.4638 |
| 0.2001 | 313.15 | 1.461 |
| 0.2502 | 293.15 | 1.4664 |
| 0.2502 | 298.15 | 1.4636 |
| 0.2502 | 303.15 | 1.4608 |
| 0.2502 | 308.15 | 1.4581 |
| 0.2502 | 313.15 | 1.4553 |
| 0.2985 | 293.15 | 1.461 |
| 0.2985 | 298.15 | 1.4583 |
| 0.2985 | 303.15 | 1.4555 |
| 0.2985 | 308.15 | 1.4528 |
| 0.2985 | 313.15 | 1.4501 |
| 0.3447 | 293.15 | 1.4559 |
| 0.3447 | 298.15 | 1.4532 |
| 0.3447 | 303.15 | 1.4504 |
| 0.3447 | 308.15 | 1.4477 |
| 0.3447 | 313.15 | 1.4449 |
| 0.4011 | 293.15 | 1.4498 |
| 0.4011 | 298.15 | 1.447 |
| 0.4011 | 303.15 | 1.4443 |
| 0.4011 | 308.15 | 1.4416 |
| 0.4011 | 313.15 | 1.4389 |
| 0.4468 | 293.15 | 1.445 |
| 0.4468 | 298.15 | 1.4424 |
| 0.4468 | 303.15 | 1.4397 |
| 0.4468 | 308.15 | 1.4369 |
| 0.4468 | 313.15 | 1.4342 |
| 0.4994 | 293.15 | 1.4396 |
| 0.4994 | 298.15 | 1.437 |
| 0.4994 | 303.15 | 1.4343 |
| 0.4994 | 308.15 | 1.4316 |
| 0.4994 | 313.15 | 1.4289 |
| 0.5524 | 293.15 | 1.4343 |
| 0.5524 | 298.15 | 1.4317 |
| 0.5524 | 303.15 | 1.429 |
| 0.5524 | 308.15 | 1.4263 |
| 0.5524 | 313.15 | 1.4237 |
| 0.5999 | 293.15 | 1.4296 |
| 0.5999 | 298.15 | 1.4269 |
| 0.5999 | 303.15 | 1.4243 |
| 0.5999 | 308.15 | 1.4216 |
| 0.5999 | 313.15 | 1.419 |
| 0.6517 | 293.15 | 1.4247 |
| 0.6517 | 298.15 | 1.4221 |
| 0.6517 | 303.15 | 1.4194 |
| 0.6517 | 308.15 | 1.4168 |
| 0.6517 | 313.15 | 1.4142 |
| 0.7000 | 293.15 | 1.4202 |
| 0.7000 | 298.15 | 1.4176 |
| 0.7000 | 303.15 | 1.415 |
| 0.7000 | 308.15 | 1.4123 |
| 0.7000 | 313.15 | 1.4097 |
| 0.7516 | 293.15 | 1.4155 |
| 0.7516 | 298.15 | 1.4129 |
| 0.7516 | 303.15 | 1.4103 |
| 0.7516 | 308.15 | 1.4077 |
| 0.7516 | 313.15 | 1.4051 |
| 0.7972 | 293.15 | 1.4114 |
| 0.7972 | 298.15 | 1.4089 |
| 0.7972 | 303.15 | 1.4063 |
| 0.7972 | 308.15 | 1.4037 |
| 0.7972 | 313.15 | 1.4012 |
| 0.8404 | 293.15 | 1.4076 |
| 0.8404 | 298.15 | 1.4051 |
| 0.8404 | 303.15 | 1.4025 |
| 0.8404 | 308.15 | 1.3999 |
| 0.8404 | 313.15 | 1.3974 |
| 0.8971 | 293.15 | 1.4027 |
| 0.8971 | 298.15 | 1.4002 |
| 0.8971 | 303.15 | 1.3978 |
| 0.8971 | 308.15 | 1.3952 |
| 0.8971 | 313.15 | 1.3926 |
| 0.9449 | 293.15 | 1.3988 |
| 0.9449 | 298.15 | 1.3963 |
| 0.9449 | 303.15 | 1.3938 |
| 0.9449 | 308.15 | 1.3913 |
| 0.9449 | 313.15 | 1.3888 |
Operational condition: Temperature, K = 298.15 (Liquid)
| Mole fraction of Toluene (1) - Liquid | Surface tension liquid-gas, N/m - Liquid |
|---|---|
| 0.0544 | 0.0250 |
| 0.1097 | 0.0250 |
| 0.1530 | 0.0252 |
| 0.2081 | 0.0254 |
| 0.2565 | 0.0255 |
| 0.3033 | 0.0256 |
| 0.3549 | 0.0258 |
| 0.4024 | 0.0259 |
| 0.4509 | 0.0261 |
| 0.5066 | 0.0263 |
| 0.5520 | 0.0264 |
| 0.6094 | 0.0266 |
| 0.6577 | 0.0268 |
| 0.7071 | 0.0270 |
| 0.7549 | 0.0272 |
| 0.8073 | 0.0274 |
| 0.8500 | 0.0276 |
| 0.9035 | 0.0279 |
| 0.9500 | 0.0282 |
Operational condition: Temperature, K = 298.15 (Liquid)
| Mole fraction of Toluene (1) - Liquid | Surface tension liquid-gas, N/m - Liquid |
|---|---|
| 0.0544 | 0.0250 |
| 0.1097 | 0.0250 |
| 0.1530 | 0.0252 |
| 0.2081 | 0.0254 |
| 0.2565 | 0.0255 |
| 0.3033 | 0.0256 |
| 0.3549 | 0.0258 |
| 0.4024 | 0.0259 |
| 0.4509 | 0.0261 |
| 0.5066 | 0.0263 |
| 0.5520 | 0.0264 |
| 0.6094 | 0.0266 |
| 0.6577 | 0.0268 |
| 0.7071 | 0.0270 |
| 0.7549 | 0.0272 |
| 0.8073 | 0.0274 |
| 0.8500 | 0.0276 |
| 0.9035 | 0.0279 |
| 0.9500 | 0.0282 |
Operational conditions:
| Mole fraction of Acetic acid, butyl ester (2) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.0550 | -1.9000e-08 |
| 0.1581 | -6.0000e-08 |
| 0.2744 | -8.2000e-08 |
| 0.4420 | -1.0000e-07 |
| 0.5243 | -1.0300e-07 |
| 0.6231 | -1.0200e-07 |
| 0.7619 | -8.9000e-08 |
| 0.8490 | -6.9000e-08 |
| 0.9052 | -5.1000e-08 |
Operational conditions:
| Mole fraction of Acetic acid, butyl ester (2) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.0550 | -1.9000e-08 |
| 0.1581 | -6.0000e-08 |
| 0.2744 | -8.2000e-08 |
| 0.4420 | -1.0000e-07 |
| 0.5243 | -1.0300e-07 |
| 0.6231 | -1.0200e-07 |
| 0.7619 | -8.9000e-08 |
| 0.8490 | -6.9000e-08 |
| 0.9052 | -5.1000e-08 |