- Name
- Benzene
- InChI
- InChI=1S/C6H6/c1-2-4-6-5-3-1/h1-6H
- InChI Key
- UHOVQNZJYSORNB-UHFFFAOYSA-N
- Formula
- C6H6
- SMILES
- c1ccccc1
- Mol. Weight (g/mol)
- 78.11
- CAS
- 71-43-2
- Name
- Tetrahydrofuran
- InChI
- InChI=1S/C4H8O/c1-2-4-5-3-1/h1-4H2
- InChI Key
- WYURNTSHIVDZCO-UHFFFAOYSA-N
- Formula
- C4H8O
- SMILES
- C1CCOC1
- Mol. Weight (g/mol)
- 72.11
- CAS
- 109-99-9
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Datasets
- η - Viscosity, Pa*s (2)
- n0 - Refractive index (Na D-line) (2)
- csound,fluid - Speed of Sound, m/s (2)
- Vapor Liquid Equilibrium at Constant Temperature (3)
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydrofuran (2) - Liquid | Viscosity, Pa*s - Liquid |
| 288.15 | 0.0000 | 0.0007 |
| 288.15 | 0.0754 | 0.0007 |
| 288.15 | 0.1518 | 0.0007 |
| 288.15 | 0.2230 | 0.0007 |
| 288.15 | 0.2962 | 0.0007 |
| 288.15 | 0.3556 | 0.0006 |
| 288.15 | 0.4128 | 0.0006 |
| 288.15 | 0.4812 | 0.0006 |
| 288.15 | 0.5506 | 0.0006 |
| 288.15 | 0.6219 | 0.0006 |
| 288.15 | 0.6884 | 0.0006 |
| 288.15 | 0.7512 | 0.0006 |
| 288.15 | 0.8119 | 0.0006 |
| 288.15 | 0.8792 | 0.0005 |
| 288.15 | 0.9388 | 0.0005 |
| 288.15 | 1.0000 | 0.0005 |
| 298.15 | 0.0000 | 0.0006 |
| 298.15 | 0.0754 | 0.0006 |
| 298.15 | 0.1518 | 0.0006 |
| 298.15 | 0.2230 | 0.0006 |
| 298.15 | 0.2962 | 0.0006 |
| 298.15 | 0.3556 | 0.0006 |
| 298.15 | 0.4128 | 0.0006 |
| 298.15 | 0.4812 | 0.0006 |
| 298.15 | 0.5506 | 0.0005 |
| 298.15 | 0.6219 | 0.0005 |
| 298.15 | 0.6884 | 0.0005 |
| 298.15 | 0.7512 | 0.0005 |
| 298.15 | 0.8119 | 0.0005 |
| 298.15 | 0.8792 | 0.0005 |
| 298.15 | 0.9388 | 0.0005 |
| 298.15 | 1.0000 | 0.0005 |
| 308.15 | 0.0000 | 0.0005 |
| 308.15 | 0.0754 | 0.0005 |
| 308.15 | 0.1518 | 0.0005 |
| 308.15 | 0.2230 | 0.0005 |
| 308.15 | 0.2962 | 0.0005 |
| 308.15 | 0.3556 | 0.0005 |
| 308.15 | 0.4128 | 0.0005 |
| 308.15 | 0.4812 | 0.0005 |
| 308.15 | 0.5506 | 0.0005 |
| 308.15 | 0.6219 | 0.0005 |
| 308.15 | 0.6884 | 0.0005 |
| 308.15 | 0.7512 | 0.0005 |
| 308.15 | 0.8119 | 0.0005 |
| 308.15 | 0.8792 | 0.0004 |
| 308.15 | 0.9388 | 0.0004 |
| 308.15 | 1.0000 | 0.0004 |
| 318.15 | 0.0000 | 0.0005 |
| 318.15 | 0.0754 | 0.0005 |
| 318.15 | 0.1518 | 0.0005 |
| 318.15 | 0.2230 | 0.0005 |
| 318.15 | 0.2962 | 0.0005 |
| 318.15 | 0.3556 | 0.0005 |
| 318.15 | 0.4128 | 0.0005 |
| 318.15 | 0.4812 | 0.0005 |
| 318.15 | 0.5506 | 0.0004 |
| 318.15 | 0.6219 | 0.0004 |
| 318.15 | 0.6884 | 0.0004 |
| 318.15 | 0.7512 | 0.0004 |
| 318.15 | 0.8119 | 0.0004 |
| 318.15 | 0.8792 | 0.0004 |
| 318.15 | 0.9388 | 0.0004 |
| 318.15 | 1.0000 | 0.0004 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydrofuran (2) - Liquid | Viscosity, Pa*s - Liquid |
| 288.15 | 0.0000 | 0.0007 |
| 288.15 | 0.0754 | 0.0007 |
| 288.15 | 0.1518 | 0.0007 |
| 288.15 | 0.2230 | 0.0007 |
| 288.15 | 0.2962 | 0.0007 |
| 288.15 | 0.3556 | 0.0006 |
| 288.15 | 0.4128 | 0.0006 |
| 288.15 | 0.4812 | 0.0006 |
| 288.15 | 0.5506 | 0.0006 |
| 288.15 | 0.6219 | 0.0006 |
| 288.15 | 0.6884 | 0.0006 |
| 288.15 | 0.7512 | 0.0006 |
| 288.15 | 0.8119 | 0.0006 |
| 288.15 | 0.8792 | 0.0005 |
| 288.15 | 0.9388 | 0.0005 |
| 288.15 | 1.0000 | 0.0005 |
| 298.15 | 0.0000 | 0.0006 |
| 298.15 | 0.0754 | 0.0006 |
| 298.15 | 0.1518 | 0.0006 |
| 298.15 | 0.2230 | 0.0006 |
| 298.15 | 0.2962 | 0.0006 |
| 298.15 | 0.3556 | 0.0006 |
| 298.15 | 0.4128 | 0.0006 |
| 298.15 | 0.4812 | 0.0006 |
| 298.15 | 0.5506 | 0.0005 |
| 298.15 | 0.6219 | 0.0005 |
| 298.15 | 0.6884 | 0.0005 |
| 298.15 | 0.7512 | 0.0005 |
| 298.15 | 0.8119 | 0.0005 |
| 298.15 | 0.8792 | 0.0005 |
| 298.15 | 0.9388 | 0.0005 |
| 298.15 | 1.0000 | 0.0005 |
| 308.15 | 0.0000 | 0.0005 |
| 308.15 | 0.0754 | 0.0005 |
| 308.15 | 0.1518 | 0.0005 |
| 308.15 | 0.2230 | 0.0005 |
| 308.15 | 0.2962 | 0.0005 |
| 308.15 | 0.3556 | 0.0005 |
| 308.15 | 0.4128 | 0.0005 |
| 308.15 | 0.4812 | 0.0005 |
| 308.15 | 0.5506 | 0.0005 |
| 308.15 | 0.6219 | 0.0005 |
| 308.15 | 0.6884 | 0.0005 |
| 308.15 | 0.7512 | 0.0005 |
| 308.15 | 0.8119 | 0.0005 |
| 308.15 | 0.8792 | 0.0004 |
| 308.15 | 0.9388 | 0.0004 |
| 308.15 | 1.0000 | 0.0004 |
| 318.15 | 0.0000 | 0.0005 |
| 318.15 | 0.0754 | 0.0005 |
| 318.15 | 0.1518 | 0.0005 |
| 318.15 | 0.2230 | 0.0005 |
| 318.15 | 0.2962 | 0.0005 |
| 318.15 | 0.3556 | 0.0005 |
| 318.15 | 0.4128 | 0.0005 |
| 318.15 | 0.4812 | 0.0005 |
| 318.15 | 0.5506 | 0.0004 |
| 318.15 | 0.6219 | 0.0004 |
| 318.15 | 0.6884 | 0.0004 |
| 318.15 | 0.7512 | 0.0004 |
| 318.15 | 0.8119 | 0.0004 |
| 318.15 | 0.8792 | 0.0004 |
| 318.15 | 0.9388 | 0.0004 |
| 318.15 | 1.0000 | 0.0004 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydrofuran (2) - Liquid | Refractive index (Na D-line) - Liquid |
| 288.15 | 0.0000 | 1.5042 |
| 288.15 | 0.0754 | 1.498 |
| 288.15 | 0.1518 | 1.4917 |
| 288.15 | 0.2230 | 1.4855 |
| 288.15 | 0.2962 | 1.4791 |
| 288.15 | 0.3556 | 1.4738 |
| 288.15 | 0.4128 | 1.4686 |
| 288.15 | 0.4812 | 1.4622 |
| 288.15 | 0.5506 | 1.4556 |
| 288.15 | 0.6219 | 1.4487 |
| 288.15 | 0.6884 | 1.4421 |
| 288.15 | 0.7512 | 1.4358 |
| 288.15 | 0.8119 | 1.4295 |
| 288.15 | 0.8792 | 1.4225 |
| 288.15 | 0.9388 | 1.4161 |
| 288.15 | 1.0000 | 1.4094 |
| 293.15 | 0.0000 | 1.5011 |
| 293.15 | 0.0754 | 1.4949 |
| 293.15 | 0.1518 | 1.4886 |
| 293.15 | 0.2230 | 1.4825 |
| 293.15 | 0.2962 | 1.4761 |
| 293.15 | 0.3556 | 1.4709 |
| 293.15 | 0.4128 | 1.4657 |
| 293.15 | 0.4812 | 1.4593 |
| 293.15 | 0.5506 | 1.4528 |
| 293.15 | 0.6219 | 1.446 |
| 293.15 | 0.6884 | 1.4394 |
| 293.15 | 0.7512 | 1.4332 |
| 293.15 | 0.8119 | 1.4269 |
| 293.15 | 0.8792 | 1.42 |
| 293.15 | 0.9388 | 1.4136 |
| 293.15 | 1.0000 | 1.407 |
| 298.15 | 0.0000 | 1.498 |
| 298.15 | 0.0754 | 1.4918 |
| 298.15 | 0.1518 | 1.4855 |
| 298.15 | 0.2230 | 1.4795 |
| 298.15 | 0.2962 | 1.4732 |
| 298.15 | 0.3556 | 1.4679 |
| 298.15 | 0.4128 | 1.4628 |
| 298.15 | 0.4812 | 1.4565 |
| 298.15 | 0.5506 | 1.45 |
| 298.15 | 0.6219 | 1.4432 |
| 298.15 | 0.6884 | 1.4367 |
| 298.15 | 0.7512 | 1.4305 |
| 298.15 | 0.8119 | 1.4243 |
| 298.15 | 0.8792 | 1.4174 |
| 298.15 | 0.9388 | 1.4111 |
| 298.15 | 1.0000 | 1.4046 |
| 303.15 | 0.0000 | 1.4949 |
| 303.15 | 0.0754 | 1.4888 |
| 303.15 | 0.1518 | 1.4825 |
| 303.15 | 0.2230 | 1.4765 |
| 303.15 | 0.2962 | 1.4702 |
| 303.15 | 0.3556 | 1.465 |
| 303.15 | 0.4128 | 1.4599 |
| 303.15 | 0.4812 | 1.4537 |
| 303.15 | 0.5506 | 1.4473 |
| 303.15 | 0.6219 | 1.4405 |
| 303.15 | 0.6884 | 1.4341 |
| 303.15 | 0.7512 | 1.4279 |
| 303.15 | 0.8119 | 1.4218 |
| 303.15 | 0.8792 | 1.4149 |
| 303.15 | 0.9388 | 1.4087 |
| 303.15 | 1.0000 | 1.4023 |
| 308.15 | 0.0000 | 1.4918 |
| 308.15 | 0.0754 | 1.4857 |
| 308.15 | 0.1518 | 1.4794 |
| 308.15 | 0.2230 | 1.4735 |
| 308.15 | 0.2962 | 1.4672 |
| 308.15 | 0.3556 | 1.4621 |
| 308.15 | 0.4128 | 1.457 |
| 308.15 | 0.4812 | 1.4509 |
| 308.15 | 0.5506 | 1.4445 |
| 308.15 | 0.6219 | 1.4378 |
| 308.15 | 0.6884 | 1.4314 |
| 308.15 | 0.7512 | 1.4253 |
| 308.15 | 0.8119 | 1.4192 |
| 308.15 | 0.8792 | 1.4124 |
| 308.15 | 0.9388 | 1.4062 |
| 308.15 | 1.0000 | 1.3999 |
| 313.15 | 0.0000 | 1.4887 |
| 313.15 | 0.0754 | 1.4826 |
| 313.15 | 0.1518 | 1.4764 |
| 313.15 | 0.2230 | 1.4705 |
| 313.15 | 0.2962 | 1.4642 |
| 313.15 | 0.3556 | 1.4592 |
| 313.15 | 0.4128 | 1.4541 |
| 313.15 | 0.4812 | 1.448 |
| 313.15 | 0.5506 | 1.4417 |
| 313.15 | 0.6219 | 1.435 |
| 313.15 | 0.6884 | 1.4287 |
| 313.15 | 0.7512 | 1.4226 |
| 313.15 | 0.8119 | 1.4166 |
| 313.15 | 0.8792 | 1.4098 |
| 313.15 | 0.9388 | 1.4037 |
| 313.15 | 1.0000 | 1.3975 |
| 318.15 | 0.0000 | 1.4856 |
| 318.15 | 0.0754 | 1.4796 |
| 318.15 | 0.1518 | 1.4734 |
| 318.15 | 0.2230 | 1.4675 |
| 318.15 | 0.2962 | 1.4614 |
| 318.15 | 0.3556 | 1.4563 |
| 318.15 | 0.4128 | 1.4513 |
| 318.15 | 0.4812 | 1.4452 |
| 318.15 | 0.5506 | 1.4389 |
| 318.15 | 0.6219 | 1.4323 |
| 318.15 | 0.6884 | 1.426 |
| 318.15 | 0.7512 | 1.42 |
| 318.15 | 0.8119 | 1.414 |
| 318.15 | 0.8792 | 1.4073 |
| 318.15 | 0.9388 | 1.4013 |
| 318.15 | 1.0000 | 1.3951 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydrofuran (2) - Liquid | Refractive index (Na D-line) - Liquid |
| 288.15 | 0.0000 | 1.5042 |
| 288.15 | 0.0754 | 1.498 |
| 288.15 | 0.1518 | 1.4917 |
| 288.15 | 0.2230 | 1.4855 |
| 288.15 | 0.2962 | 1.4791 |
| 288.15 | 0.3556 | 1.4738 |
| 288.15 | 0.4128 | 1.4686 |
| 288.15 | 0.4812 | 1.4622 |
| 288.15 | 0.5506 | 1.4556 |
| 288.15 | 0.6219 | 1.4487 |
| 288.15 | 0.6884 | 1.4421 |
| 288.15 | 0.7512 | 1.4358 |
| 288.15 | 0.8119 | 1.4295 |
| 288.15 | 0.8792 | 1.4225 |
| 288.15 | 0.9388 | 1.4161 |
| 288.15 | 1.0000 | 1.4094 |
| 293.15 | 0.0000 | 1.5011 |
| 293.15 | 0.0754 | 1.4949 |
| 293.15 | 0.1518 | 1.4886 |
| 293.15 | 0.2230 | 1.4825 |
| 293.15 | 0.2962 | 1.4761 |
| 293.15 | 0.3556 | 1.4709 |
| 293.15 | 0.4128 | 1.4657 |
| 293.15 | 0.4812 | 1.4593 |
| 293.15 | 0.5506 | 1.4528 |
| 293.15 | 0.6219 | 1.446 |
| 293.15 | 0.6884 | 1.4394 |
| 293.15 | 0.7512 | 1.4332 |
| 293.15 | 0.8119 | 1.4269 |
| 293.15 | 0.8792 | 1.42 |
| 293.15 | 0.9388 | 1.4136 |
| 293.15 | 1.0000 | 1.407 |
| 298.15 | 0.0000 | 1.498 |
| 298.15 | 0.0754 | 1.4918 |
| 298.15 | 0.1518 | 1.4855 |
| 298.15 | 0.2230 | 1.4795 |
| 298.15 | 0.2962 | 1.4732 |
| 298.15 | 0.3556 | 1.4679 |
| 298.15 | 0.4128 | 1.4628 |
| 298.15 | 0.4812 | 1.4565 |
| 298.15 | 0.5506 | 1.45 |
| 298.15 | 0.6219 | 1.4432 |
| 298.15 | 0.6884 | 1.4367 |
| 298.15 | 0.7512 | 1.4305 |
| 298.15 | 0.8119 | 1.4243 |
| 298.15 | 0.8792 | 1.4174 |
| 298.15 | 0.9388 | 1.4111 |
| 298.15 | 1.0000 | 1.4046 |
| 303.15 | 0.0000 | 1.4949 |
| 303.15 | 0.0754 | 1.4888 |
| 303.15 | 0.1518 | 1.4825 |
| 303.15 | 0.2230 | 1.4765 |
| 303.15 | 0.2962 | 1.4702 |
| 303.15 | 0.3556 | 1.465 |
| 303.15 | 0.4128 | 1.4599 |
| 303.15 | 0.4812 | 1.4537 |
| 303.15 | 0.5506 | 1.4473 |
| 303.15 | 0.6219 | 1.4405 |
| 303.15 | 0.6884 | 1.4341 |
| 303.15 | 0.7512 | 1.4279 |
| 303.15 | 0.8119 | 1.4218 |
| 303.15 | 0.8792 | 1.4149 |
| 303.15 | 0.9388 | 1.4087 |
| 303.15 | 1.0000 | 1.4023 |
| 308.15 | 0.0000 | 1.4918 |
| 308.15 | 0.0754 | 1.4857 |
| 308.15 | 0.1518 | 1.4794 |
| 308.15 | 0.2230 | 1.4735 |
| 308.15 | 0.2962 | 1.4672 |
| 308.15 | 0.3556 | 1.4621 |
| 308.15 | 0.4128 | 1.457 |
| 308.15 | 0.4812 | 1.4509 |
| 308.15 | 0.5506 | 1.4445 |
| 308.15 | 0.6219 | 1.4378 |
| 308.15 | 0.6884 | 1.4314 |
| 308.15 | 0.7512 | 1.4253 |
| 308.15 | 0.8119 | 1.4192 |
| 308.15 | 0.8792 | 1.4124 |
| 308.15 | 0.9388 | 1.4062 |
| 308.15 | 1.0000 | 1.3999 |
| 313.15 | 0.0000 | 1.4887 |
| 313.15 | 0.0754 | 1.4826 |
| 313.15 | 0.1518 | 1.4764 |
| 313.15 | 0.2230 | 1.4705 |
| 313.15 | 0.2962 | 1.4642 |
| 313.15 | 0.3556 | 1.4592 |
| 313.15 | 0.4128 | 1.4541 |
| 313.15 | 0.4812 | 1.448 |
| 313.15 | 0.5506 | 1.4417 |
| 313.15 | 0.6219 | 1.435 |
| 313.15 | 0.6884 | 1.4287 |
| 313.15 | 0.7512 | 1.4226 |
| 313.15 | 0.8119 | 1.4166 |
| 313.15 | 0.8792 | 1.4098 |
| 313.15 | 0.9388 | 1.4037 |
| 313.15 | 1.0000 | 1.3975 |
| 318.15 | 0.0000 | 1.4856 |
| 318.15 | 0.0754 | 1.4796 |
| 318.15 | 0.1518 | 1.4734 |
| 318.15 | 0.2230 | 1.4675 |
| 318.15 | 0.2962 | 1.4614 |
| 318.15 | 0.3556 | 1.4563 |
| 318.15 | 0.4128 | 1.4513 |
| 318.15 | 0.4812 | 1.4452 |
| 318.15 | 0.5506 | 1.4389 |
| 318.15 | 0.6219 | 1.4323 |
| 318.15 | 0.6884 | 1.426 |
| 318.15 | 0.7512 | 1.42 |
| 318.15 | 0.8119 | 1.414 |
| 318.15 | 0.8792 | 1.4073 |
| 318.15 | 0.9388 | 1.4013 |
| 318.15 | 1.0000 | 1.3951 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydrofuran (2) - Liquid | Speed of sound, m/s - Liquid |
| 288.15 | 0.0000 | 1352.4 |
| 288.15 | 0.0754 | 1351.7 |
| 288.15 | 0.1518 | 1350.7 |
| 288.15 | 0.2230 | 1349.8 |
| 288.15 | 0.2962 | 1348.5 |
| 288.15 | 0.3556 | 1347.4 |
| 288.15 | 0.4128 | 1346.3 |
| 288.15 | 0.4812 | 1344.6 |
| 288.15 | 0.5506 | 1342.7 |
| 288.15 | 0.6219 | 1340.5 |
| 288.15 | 0.6884 | 1338.0 |
| 288.15 | 0.7512 | 1335.3 |
| 288.15 | 0.8119 | 1332.7 |
| 288.15 | 0.8792 | 1329.3 |
| 288.15 | 0.9388 | 1326.3 |
| 288.15 | 1.0000 | 1323.1 |
| 298.15 | 0.0000 | 1303.5 |
| 298.15 | 0.0754 | 1302.5 |
| 298.15 | 0.1518 | 1301.4 |
| 298.15 | 0.2230 | 1300.6 |
| 298.15 | 0.2962 | 1299.3 |
| 298.15 | 0.3556 | 1298.4 |
| 298.15 | 0.4128 | 1297.5 |
| 298.15 | 0.4812 | 1296.0 |
| 298.15 | 0.5506 | 1294.3 |
| 298.15 | 0.6219 | 1292.4 |
| 298.15 | 0.6884 | 1290.2 |
| 298.15 | 0.7512 | 1287.9 |
| 298.15 | 0.8119 | 1285.5 |
| 298.15 | 0.8792 | 1282.7 |
| 298.15 | 0.9388 | 1280.1 |
| 298.15 | 1.0000 | 1277.6 |
| 308.15 | 0.0000 | 1257.4 |
| 308.15 | 0.0754 | 1256.0 |
| 308.15 | 0.1518 | 1254.7 |
| 308.15 | 0.2230 | 1253.6 |
| 308.15 | 0.2962 | 1252.2 |
| 308.15 | 0.3556 | 1251.3 |
| 308.15 | 0.4128 | 1250.3 |
| 308.15 | 0.4812 | 1248.8 |
| 308.15 | 0.5506 | 1247.1 |
| 308.15 | 0.6219 | 1245.1 |
| 308.15 | 0.6884 | 1243.0 |
| 308.15 | 0.7512 | 1240.8 |
| 308.15 | 0.8119 | 1238.6 |
| 308.15 | 0.8792 | 1236.1 |
| 308.15 | 0.9388 | 1233.8 |
| 308.15 | 1.0000 | 1231.5 |
| 318.15 | 0.0000 | 1207.2 |
| 318.15 | 0.0754 | 1206.1 |
| 318.15 | 0.1518 | 1205.1 |
| 318.15 | 0.2230 | 1204.3 |
| 318.15 | 0.2962 | 1203.2 |
| 318.15 | 0.3556 | 1202.5 |
| 318.15 | 0.4128 | 1201.8 |
| 318.15 | 0.4812 | 1200.7 |
| 318.15 | 0.5506 | 1199.4 |
| 318.15 | 0.6219 | 1197.8 |
| 318.15 | 0.6884 | 1196.1 |
| 318.15 | 0.7512 | 1194.4 |
| 318.15 | 0.8119 | 1192.7 |
| 318.15 | 0.8792 | 1190.7 |
| 318.15 | 0.9388 | 1188.9 |
| 318.15 | 1.0000 | 1187.2 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydrofuran (2) - Liquid | Speed of sound, m/s - Liquid |
| 288.15 | 0.0000 | 1352.4 |
| 288.15 | 0.0754 | 1351.7 |
| 288.15 | 0.1518 | 1350.7 |
| 288.15 | 0.2230 | 1349.8 |
| 288.15 | 0.2962 | 1348.5 |
| 288.15 | 0.3556 | 1347.4 |
| 288.15 | 0.4128 | 1346.3 |
| 288.15 | 0.4812 | 1344.6 |
| 288.15 | 0.5506 | 1342.7 |
| 288.15 | 0.6219 | 1340.5 |
| 288.15 | 0.6884 | 1338.0 |
| 288.15 | 0.7512 | 1335.3 |
| 288.15 | 0.8119 | 1332.7 |
| 288.15 | 0.8792 | 1329.3 |
| 288.15 | 0.9388 | 1326.3 |
| 288.15 | 1.0000 | 1323.1 |
| 298.15 | 0.0000 | 1303.5 |
| 298.15 | 0.0754 | 1302.5 |
| 298.15 | 0.1518 | 1301.4 |
| 298.15 | 0.2230 | 1300.6 |
| 298.15 | 0.2962 | 1299.3 |
| 298.15 | 0.3556 | 1298.4 |
| 298.15 | 0.4128 | 1297.5 |
| 298.15 | 0.4812 | 1296.0 |
| 298.15 | 0.5506 | 1294.3 |
| 298.15 | 0.6219 | 1292.4 |
| 298.15 | 0.6884 | 1290.2 |
| 298.15 | 0.7512 | 1287.9 |
| 298.15 | 0.8119 | 1285.5 |
| 298.15 | 0.8792 | 1282.7 |
| 298.15 | 0.9388 | 1280.1 |
| 298.15 | 1.0000 | 1277.6 |
| 308.15 | 0.0000 | 1257.4 |
| 308.15 | 0.0754 | 1256.0 |
| 308.15 | 0.1518 | 1254.7 |
| 308.15 | 0.2230 | 1253.6 |
| 308.15 | 0.2962 | 1252.2 |
| 308.15 | 0.3556 | 1251.3 |
| 308.15 | 0.4128 | 1250.3 |
| 308.15 | 0.4812 | 1248.8 |
| 308.15 | 0.5506 | 1247.1 |
| 308.15 | 0.6219 | 1245.1 |
| 308.15 | 0.6884 | 1243.0 |
| 308.15 | 0.7512 | 1240.8 |
| 308.15 | 0.8119 | 1238.6 |
| 308.15 | 0.8792 | 1236.1 |
| 308.15 | 0.9388 | 1233.8 |
| 308.15 | 1.0000 | 1231.5 |
| 318.15 | 0.0000 | 1207.2 |
| 318.15 | 0.0754 | 1206.1 |
| 318.15 | 0.1518 | 1205.1 |
| 318.15 | 0.2230 | 1204.3 |
| 318.15 | 0.2962 | 1203.2 |
| 318.15 | 0.3556 | 1202.5 |
| 318.15 | 0.4128 | 1201.8 |
| 318.15 | 0.4812 | 1200.7 |
| 318.15 | 0.5506 | 1199.4 |
| 318.15 | 0.6219 | 1197.8 |
| 318.15 | 0.6884 | 1196.1 |
| 318.15 | 0.7512 | 1194.4 |
| 318.15 | 0.8119 | 1192.7 |
| 318.15 | 0.8792 | 1190.7 |
| 318.15 | 0.9388 | 1188.9 |
| 318.15 | 1.0000 | 1187.2 |
Vapor Liquid Equilibrium at Constant Temperature [ref]
Operational condition: Temperature, K = 298.15 (VLE)
| P [kPa] - VLE | x1[mol/mol] of Tetrahydrofuran (2) - Liquid |
|---|---|
| 12.586 | 0.0000 |
| 13.039 | 0.0674 |
| 13.492 | 0.1559 |
| 14.052 | 0.2365 |
| 14.465 | 0.3053 |
| 15.079 | 0.3647 |
| 15.599 | 0.4293 |
| 16.079 | 0.4835 |
| 16.585 | 0.5512 |
| 17.105 | 0.5983 |
| 17.852 | 0.6703 |
| 18.545 | 0.7371 |
| 19.438 | 0.8125 |
| 20.172 | 0.8837 |
| 21.025 | 0.9545 |
Vapor Liquid Equilibrium at Constant Temperature [ref]
Operational condition: Temperature, K = 313.15 (VLE)
| P [kPa] - VLE | x1[mol/mol] of Tetrahydrofuran (2) - Liquid |
|---|---|
| 24.478 | 0.0000 |
| 25.025 | 0.0674 |
| 25.891 | 0.1559 |
| 26.864 | 0.2365 |
| 27.771 | 0.3053 |
| 28.731 | 0.3647 |
| 29.638 | 0.4293 |
| 30.597 | 0.4835 |
| 31.624 | 0.5512 |
| 32.411 | 0.5983 |
| 33.877 | 0.6703 |
| 34.89 | 0.7371 |
| 36.517 | 0.8125 |
| 37.85 | 0.8837 |
| 39.37 | 0.9545 |
Vapor Liquid Equilibrium at Constant Temperature [ref]
Operational condition: Temperature, K = 303.15 (VLE)
| Fixed | Measured | |
|---|---|---|
| P [kPa] - VLE | x1[mol/mol] of Tetrahydrofuran (2) - Liquid | y1[mol/mol] of Tetrahydrofuran (2) - Vapour |
| 16.025 | 0.0000 | 0.0000 |
| 16.345 | 0.0500 | 0.0680 |
| 16.839 | 0.1250 | 0.1650 |
| 17.599 | 0.2280 | 0.3030 |
| 18.398 | 0.3270 | 0.4230 |
| 19.265 | 0.4230 | 0.5380 |
| 19.998 | 0.4950 | 0.6140 |
| 20.398 | 0.5300 | 0.6570 |
| 20.625 | 0.5500 | 0.6750 |
| 21.572 | 0.6200 | 0.7420 |
| 22.038 | 0.6550 | 0.7720 |
| 23.398 | 0.7500 | 0.8480 |
| 25.318 | 0.8880 | 0.9360 |
| 26.331 | 0.9500 | 0.9740 |
| 27.011 | 1.0000 | 1.0000 |
Sources
- Dortmund Data Bank Vapor-Liquid Equilibrium Data
- Ultrasonic and viscometric study of molecular interactions in binary mixtures of aniline with 1-propanol, 2-propanol, 2-methyl-1-propanol, and 2-methyl-2-propanol at different temperatures
- Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K