- Name
- Toluene
- InChI
- InChI=1S/C7H8/c1-7-5-3-2-4-6-7/h2-6H,1H3
- InChI Key
- YXFVVABEGXRONW-UHFFFAOYSA-N
- Formula
- C7H8
- SMILES
- Cc1ccccc1
- Mol. Weight (g/mol)
- 92.14
- CAS
- 108-88-3
- 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)
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 | 0.0006 |
| 288.15 | 0.0718 | 0.0006 |
| 288.15 | 0.1498 | 0.0006 |
| 288.15 | 0.2283 | 0.0006 |
| 288.15 | 0.2902 | 0.0006 |
| 288.15 | 0.3452 | 0.0006 |
| 288.15 | 0.4005 | 0.0006 |
| 288.15 | 0.4694 | 0.0006 |
| 288.15 | 0.5368 | 0.0006 |
| 288.15 | 0.6067 | 0.0006 |
| 288.15 | 0.6704 | 0.0006 |
| 288.15 | 0.7378 | 0.0006 |
| 288.15 | 0.8018 | 0.0006 |
| 288.15 | 0.8714 | 0.0005 |
| 288.15 | 0.9368 | 0.0005 |
| 288.15 | 1.0000 | 0.0005 |
| 298.15 | 0.0000 | 0.0006 |
| 298.15 | 0.0718 | 0.0006 |
| 298.15 | 0.1498 | 0.0005 |
| 298.15 | 0.2283 | 0.0005 |
| 298.15 | 0.2902 | 0.0005 |
| 298.15 | 0.3452 | 0.0005 |
| 298.15 | 0.4005 | 0.0005 |
| 298.15 | 0.4694 | 0.0005 |
| 298.15 | 0.5368 | 0.0005 |
| 298.15 | 0.6067 | 0.0005 |
| 298.15 | 0.6704 | 0.0005 |
| 298.15 | 0.7378 | 0.0005 |
| 298.15 | 0.8018 | 0.0005 |
| 298.15 | 0.8714 | 0.0005 |
| 298.15 | 0.9368 | 0.0005 |
| 298.15 | 1.0000 | 0.0005 |
| 308.15 | 0.0000 | 0.0005 |
| 308.15 | 0.0718 | 0.0005 |
| 308.15 | 0.1498 | 0.0005 |
| 308.15 | 0.2283 | 0.0005 |
| 308.15 | 0.2902 | 0.0005 |
| 308.15 | 0.3452 | 0.0005 |
| 308.15 | 0.4005 | 0.0005 |
| 308.15 | 0.4694 | 0.0005 |
| 308.15 | 0.5368 | 0.0005 |
| 308.15 | 0.6067 | 0.0005 |
| 308.15 | 0.6704 | 0.0005 |
| 308.15 | 0.7378 | 0.0005 |
| 308.15 | 0.8018 | 0.0004 |
| 308.15 | 0.8714 | 0.0004 |
| 308.15 | 0.9368 | 0.0004 |
| 308.15 | 1.0000 | 0.0004 |
| 318.15 | 0.0000 | 0.0004 |
| 318.15 | 0.0718 | 0.0004 |
| 318.15 | 0.1498 | 0.0004 |
| 318.15 | 0.2283 | 0.0004 |
| 318.15 | 0.2902 | 0.0004 |
| 318.15 | 0.3452 | 0.0004 |
| 318.15 | 0.4005 | 0.0004 |
| 318.15 | 0.4694 | 0.0004 |
| 318.15 | 0.5368 | 0.0004 |
| 318.15 | 0.6067 | 0.0004 |
| 318.15 | 0.6704 | 0.0004 |
| 318.15 | 0.7378 | 0.0004 |
| 318.15 | 0.8018 | 0.0004 |
| 318.15 | 0.8714 | 0.0004 |
| 318.15 | 0.9368 | 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 | 0.0006 |
| 288.15 | 0.0718 | 0.0006 |
| 288.15 | 0.1498 | 0.0006 |
| 288.15 | 0.2283 | 0.0006 |
| 288.15 | 0.2902 | 0.0006 |
| 288.15 | 0.3452 | 0.0006 |
| 288.15 | 0.4005 | 0.0006 |
| 288.15 | 0.4694 | 0.0006 |
| 288.15 | 0.5368 | 0.0006 |
| 288.15 | 0.6067 | 0.0006 |
| 288.15 | 0.6704 | 0.0006 |
| 288.15 | 0.7378 | 0.0006 |
| 288.15 | 0.8018 | 0.0006 |
| 288.15 | 0.8714 | 0.0005 |
| 288.15 | 0.9368 | 0.0005 |
| 288.15 | 1.0000 | 0.0005 |
| 298.15 | 0.0000 | 0.0006 |
| 298.15 | 0.0718 | 0.0006 |
| 298.15 | 0.1498 | 0.0005 |
| 298.15 | 0.2283 | 0.0005 |
| 298.15 | 0.2902 | 0.0005 |
| 298.15 | 0.3452 | 0.0005 |
| 298.15 | 0.4005 | 0.0005 |
| 298.15 | 0.4694 | 0.0005 |
| 298.15 | 0.5368 | 0.0005 |
| 298.15 | 0.6067 | 0.0005 |
| 298.15 | 0.6704 | 0.0005 |
| 298.15 | 0.7378 | 0.0005 |
| 298.15 | 0.8018 | 0.0005 |
| 298.15 | 0.8714 | 0.0005 |
| 298.15 | 0.9368 | 0.0005 |
| 298.15 | 1.0000 | 0.0005 |
| 308.15 | 0.0000 | 0.0005 |
| 308.15 | 0.0718 | 0.0005 |
| 308.15 | 0.1498 | 0.0005 |
| 308.15 | 0.2283 | 0.0005 |
| 308.15 | 0.2902 | 0.0005 |
| 308.15 | 0.3452 | 0.0005 |
| 308.15 | 0.4005 | 0.0005 |
| 308.15 | 0.4694 | 0.0005 |
| 308.15 | 0.5368 | 0.0005 |
| 308.15 | 0.6067 | 0.0005 |
| 308.15 | 0.6704 | 0.0005 |
| 308.15 | 0.7378 | 0.0005 |
| 308.15 | 0.8018 | 0.0004 |
| 308.15 | 0.8714 | 0.0004 |
| 308.15 | 0.9368 | 0.0004 |
| 308.15 | 1.0000 | 0.0004 |
| 318.15 | 0.0000 | 0.0004 |
| 318.15 | 0.0718 | 0.0004 |
| 318.15 | 0.1498 | 0.0004 |
| 318.15 | 0.2283 | 0.0004 |
| 318.15 | 0.2902 | 0.0004 |
| 318.15 | 0.3452 | 0.0004 |
| 318.15 | 0.4005 | 0.0004 |
| 318.15 | 0.4694 | 0.0004 |
| 318.15 | 0.5368 | 0.0004 |
| 318.15 | 0.6067 | 0.0004 |
| 318.15 | 0.6704 | 0.0004 |
| 318.15 | 0.7378 | 0.0004 |
| 318.15 | 0.8018 | 0.0004 |
| 318.15 | 0.8714 | 0.0004 |
| 318.15 | 0.9368 | 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 | 1.4998 |
| 288.15 | 0.0718 | 1.4952 |
| 288.15 | 0.1498 | 1.4898 |
| 288.15 | 0.2283 | 1.4841 |
| 288.15 | 0.2902 | 1.4795 |
| 288.15 | 0.3452 | 1.4751 |
| 288.15 | 0.4005 | 1.4706 |
| 288.15 | 0.4694 | 1.4647 |
| 288.15 | 0.5368 | 1.4587 |
| 288.15 | 0.6067 | 1.4522 |
| 288.15 | 0.6704 | 1.4461 |
| 288.15 | 0.7378 | 1.4392 |
| 288.15 | 0.8018 | 1.4325 |
| 288.15 | 0.8714 | 1.4248 |
| 288.15 | 0.9368 | 1.4171 |
| 288.15 | 1.0000 | 1.4094 |
| 293.15 | 0.0000 | 1.497 |
| 293.15 | 0.0718 | 1.4923 |
| 293.15 | 0.1498 | 1.487 |
| 293.15 | 0.2283 | 1.4813 |
| 293.15 | 0.2902 | 1.4766 |
| 293.15 | 0.3452 | 1.4723 |
| 293.15 | 0.4005 | 1.4678 |
| 293.15 | 0.4694 | 1.4619 |
| 293.15 | 0.5368 | 1.456 |
| 293.15 | 0.6067 | 1.4495 |
| 293.15 | 0.6704 | 1.4434 |
| 293.15 | 0.7378 | 1.4366 |
| 293.15 | 0.8018 | 1.4298 |
| 293.15 | 0.8714 | 1.4222 |
| 293.15 | 0.9368 | 1.4146 |
| 293.15 | 1.0000 | 1.407 |
| 298.15 | 0.0000 | 1.4942 |
| 298.15 | 0.0718 | 1.4895 |
| 298.15 | 0.1498 | 1.4841 |
| 298.15 | 0.2283 | 1.4784 |
| 298.15 | 0.2902 | 1.4738 |
| 298.15 | 0.3452 | 1.4695 |
| 298.15 | 0.4005 | 1.465 |
| 298.15 | 0.4694 | 1.4592 |
| 298.15 | 0.5368 | 1.4533 |
| 298.15 | 0.6067 | 1.4468 |
| 298.15 | 0.6704 | 1.4407 |
| 298.15 | 0.7378 | 1.4339 |
| 298.15 | 0.8018 | 1.4272 |
| 298.15 | 0.8714 | 1.4196 |
| 298.15 | 0.9368 | 1.4121 |
| 298.15 | 1.0000 | 1.4046 |
| 303.15 | 0.0000 | 1.4913 |
| 303.15 | 0.0718 | 1.4866 |
| 303.15 | 0.1498 | 1.4812 |
| 303.15 | 0.2283 | 1.4755 |
| 303.15 | 0.2902 | 1.4709 |
| 303.15 | 0.3452 | 1.4667 |
| 303.15 | 0.4005 | 1.4623 |
| 303.15 | 0.4694 | 1.4565 |
| 303.15 | 0.5368 | 1.4505 |
| 303.15 | 0.6067 | 1.4441 |
| 303.15 | 0.6704 | 1.438 |
| 303.15 | 0.7378 | 1.4313 |
| 303.15 | 0.8018 | 1.4246 |
| 303.15 | 0.8714 | 1.4171 |
| 303.15 | 0.9368 | 1.4097 |
| 303.15 | 1.0000 | 1.4023 |
| 308.15 | 0.0000 | 1.4884 |
| 308.15 | 0.0718 | 1.4837 |
| 308.15 | 0.1498 | 1.4783 |
| 308.15 | 0.2283 | 1.4727 |
| 308.15 | 0.2902 | 1.4681 |
| 308.15 | 0.3452 | 1.4639 |
| 308.15 | 0.4005 | 1.4595 |
| 308.15 | 0.4694 | 1.4537 |
| 308.15 | 0.5368 | 1.4478 |
| 308.15 | 0.6067 | 1.4414 |
| 308.15 | 0.6704 | 1.4353 |
| 308.15 | 0.7378 | 1.4286 |
| 308.15 | 0.8018 | 1.422 |
| 308.15 | 0.8714 | 1.4145 |
| 308.15 | 0.9368 | 1.4072 |
| 308.15 | 1.0000 | 1.3999 |
| 313.15 | 0.0000 | 1.4855 |
| 313.15 | 0.0718 | 1.4808 |
| 313.15 | 0.1498 | 1.4755 |
| 313.15 | 0.2283 | 1.4698 |
| 313.15 | 0.2902 | 1.4652 |
| 313.15 | 0.3452 | 1.4611 |
| 313.15 | 0.4005 | 1.4568 |
| 313.15 | 0.4694 | 1.451 |
| 313.15 | 0.5368 | 1.4451 |
| 313.15 | 0.6067 | 1.4387 |
| 313.15 | 0.6704 | 1.4326 |
| 313.15 | 0.7378 | 1.426 |
| 313.15 | 0.8018 | 1.4194 |
| 313.15 | 0.8714 | 1.4119 |
| 313.15 | 0.9368 | 1.4047 |
| 313.15 | 1.0000 | 1.3975 |
| 318.15 | 0.0000 | 1.4826 |
| 318.15 | 0.0718 | 1.4779 |
| 318.15 | 0.1498 | 1.4726 |
| 318.15 | 0.2283 | 1.467 |
| 318.15 | 0.2902 | 1.4625 |
| 318.15 | 0.3452 | 1.4583 |
| 318.15 | 0.4005 | 1.4539 |
| 318.15 | 0.4694 | 1.4482 |
| 318.15 | 0.5368 | 1.4424 |
| 318.15 | 0.6067 | 1.4361 |
| 318.15 | 0.6704 | 1.43 |
| 318.15 | 0.7378 | 1.4234 |
| 318.15 | 0.8018 | 1.4169 |
| 318.15 | 0.8714 | 1.4095 |
| 318.15 | 0.9368 | 1.4023 |
| 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 | 1.4998 |
| 288.15 | 0.0718 | 1.4952 |
| 288.15 | 0.1498 | 1.4898 |
| 288.15 | 0.2283 | 1.4841 |
| 288.15 | 0.2902 | 1.4795 |
| 288.15 | 0.3452 | 1.4751 |
| 288.15 | 0.4005 | 1.4706 |
| 288.15 | 0.4694 | 1.4647 |
| 288.15 | 0.5368 | 1.4587 |
| 288.15 | 0.6067 | 1.4522 |
| 288.15 | 0.6704 | 1.4461 |
| 288.15 | 0.7378 | 1.4392 |
| 288.15 | 0.8018 | 1.4325 |
| 288.15 | 0.8714 | 1.4248 |
| 288.15 | 0.9368 | 1.4171 |
| 288.15 | 1.0000 | 1.4094 |
| 293.15 | 0.0000 | 1.497 |
| 293.15 | 0.0718 | 1.4923 |
| 293.15 | 0.1498 | 1.487 |
| 293.15 | 0.2283 | 1.4813 |
| 293.15 | 0.2902 | 1.4766 |
| 293.15 | 0.3452 | 1.4723 |
| 293.15 | 0.4005 | 1.4678 |
| 293.15 | 0.4694 | 1.4619 |
| 293.15 | 0.5368 | 1.456 |
| 293.15 | 0.6067 | 1.4495 |
| 293.15 | 0.6704 | 1.4434 |
| 293.15 | 0.7378 | 1.4366 |
| 293.15 | 0.8018 | 1.4298 |
| 293.15 | 0.8714 | 1.4222 |
| 293.15 | 0.9368 | 1.4146 |
| 293.15 | 1.0000 | 1.407 |
| 298.15 | 0.0000 | 1.4942 |
| 298.15 | 0.0718 | 1.4895 |
| 298.15 | 0.1498 | 1.4841 |
| 298.15 | 0.2283 | 1.4784 |
| 298.15 | 0.2902 | 1.4738 |
| 298.15 | 0.3452 | 1.4695 |
| 298.15 | 0.4005 | 1.465 |
| 298.15 | 0.4694 | 1.4592 |
| 298.15 | 0.5368 | 1.4533 |
| 298.15 | 0.6067 | 1.4468 |
| 298.15 | 0.6704 | 1.4407 |
| 298.15 | 0.7378 | 1.4339 |
| 298.15 | 0.8018 | 1.4272 |
| 298.15 | 0.8714 | 1.4196 |
| 298.15 | 0.9368 | 1.4121 |
| 298.15 | 1.0000 | 1.4046 |
| 303.15 | 0.0000 | 1.4913 |
| 303.15 | 0.0718 | 1.4866 |
| 303.15 | 0.1498 | 1.4812 |
| 303.15 | 0.2283 | 1.4755 |
| 303.15 | 0.2902 | 1.4709 |
| 303.15 | 0.3452 | 1.4667 |
| 303.15 | 0.4005 | 1.4623 |
| 303.15 | 0.4694 | 1.4565 |
| 303.15 | 0.5368 | 1.4505 |
| 303.15 | 0.6067 | 1.4441 |
| 303.15 | 0.6704 | 1.438 |
| 303.15 | 0.7378 | 1.4313 |
| 303.15 | 0.8018 | 1.4246 |
| 303.15 | 0.8714 | 1.4171 |
| 303.15 | 0.9368 | 1.4097 |
| 303.15 | 1.0000 | 1.4023 |
| 308.15 | 0.0000 | 1.4884 |
| 308.15 | 0.0718 | 1.4837 |
| 308.15 | 0.1498 | 1.4783 |
| 308.15 | 0.2283 | 1.4727 |
| 308.15 | 0.2902 | 1.4681 |
| 308.15 | 0.3452 | 1.4639 |
| 308.15 | 0.4005 | 1.4595 |
| 308.15 | 0.4694 | 1.4537 |
| 308.15 | 0.5368 | 1.4478 |
| 308.15 | 0.6067 | 1.4414 |
| 308.15 | 0.6704 | 1.4353 |
| 308.15 | 0.7378 | 1.4286 |
| 308.15 | 0.8018 | 1.422 |
| 308.15 | 0.8714 | 1.4145 |
| 308.15 | 0.9368 | 1.4072 |
| 308.15 | 1.0000 | 1.3999 |
| 313.15 | 0.0000 | 1.4855 |
| 313.15 | 0.0718 | 1.4808 |
| 313.15 | 0.1498 | 1.4755 |
| 313.15 | 0.2283 | 1.4698 |
| 313.15 | 0.2902 | 1.4652 |
| 313.15 | 0.3452 | 1.4611 |
| 313.15 | 0.4005 | 1.4568 |
| 313.15 | 0.4694 | 1.451 |
| 313.15 | 0.5368 | 1.4451 |
| 313.15 | 0.6067 | 1.4387 |
| 313.15 | 0.6704 | 1.4326 |
| 313.15 | 0.7378 | 1.426 |
| 313.15 | 0.8018 | 1.4194 |
| 313.15 | 0.8714 | 1.4119 |
| 313.15 | 0.9368 | 1.4047 |
| 313.15 | 1.0000 | 1.3975 |
| 318.15 | 0.0000 | 1.4826 |
| 318.15 | 0.0718 | 1.4779 |
| 318.15 | 0.1498 | 1.4726 |
| 318.15 | 0.2283 | 1.467 |
| 318.15 | 0.2902 | 1.4625 |
| 318.15 | 0.3452 | 1.4583 |
| 318.15 | 0.4005 | 1.4539 |
| 318.15 | 0.4694 | 1.4482 |
| 318.15 | 0.5368 | 1.4424 |
| 318.15 | 0.6067 | 1.4361 |
| 318.15 | 0.6704 | 1.43 |
| 318.15 | 0.7378 | 1.4234 |
| 318.15 | 0.8018 | 1.4169 |
| 318.15 | 0.8714 | 1.4095 |
| 318.15 | 0.9368 | 1.4023 |
| 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 | 1358.5 |
| 288.15 | 0.0718 | 1357.7 |
| 288.15 | 0.1498 | 1356.3 |
| 288.15 | 0.2283 | 1354.6 |
| 288.15 | 0.2902 | 1353.1 |
| 288.15 | 0.3452 | 1351.7 |
| 288.15 | 0.4005 | 1350.1 |
| 288.15 | 0.4694 | 1347.8 |
| 288.15 | 0.5368 | 1345.4 |
| 288.15 | 0.6067 | 1342.8 |
| 288.15 | 0.6704 | 1340.1 |
| 288.15 | 0.7378 | 1337.0 |
| 288.15 | 0.8018 | 1333.8 |
| 288.15 | 0.8714 | 1330.2 |
| 288.15 | 0.9368 | 1326.6 |
| 288.15 | 1.0000 | 1323.1 |
| 298.15 | 0.0000 | 1310.5 |
| 298.15 | 0.0718 | 1309.4 |
| 298.15 | 0.1498 | 1307.9 |
| 298.15 | 0.2283 | 1306.2 |
| 298.15 | 0.2902 | 1304.8 |
| 298.15 | 0.3452 | 1303.4 |
| 298.15 | 0.4005 | 1302.0 |
| 298.15 | 0.4694 | 1299.9 |
| 298.15 | 0.5368 | 1297.7 |
| 298.15 | 0.6067 | 1295.2 |
| 298.15 | 0.6704 | 1292.8 |
| 298.15 | 0.7378 | 1289.9 |
| 298.15 | 0.8018 | 1287.0 |
| 298.15 | 0.8714 | 1284.0 |
| 298.15 | 0.9368 | 1280.7 |
| 298.15 | 1.0000 | 1277.6 |
| 308.15 | 0.0000 | 1266.2 |
| 308.15 | 0.0718 | 1264.6 |
| 308.15 | 0.1498 | 1262.7 |
| 308.15 | 0.2283 | 1260.7 |
| 308.15 | 0.2902 | 1259.1 |
| 308.15 | 0.3452 | 1257.6 |
| 308.15 | 0.4005 | 1255.9 |
| 308.15 | 0.4694 | 1253.7 |
| 308.15 | 0.5368 | 1251.4 |
| 308.15 | 0.6067 | 1248.8 |
| 308.15 | 0.6704 | 1246.3 |
| 308.15 | 0.7378 | 1243.5 |
| 308.15 | 0.8018 | 1240.7 |
| 308.15 | 0.8714 | 1237.6 |
| 308.15 | 0.9368 | 1234.5 |
| 308.15 | 1.0000 | 1231.5 |
| 318.15 | 0.0000 | 1221.0 |
| 318.15 | 0.0718 | 1219.3 |
| 318.15 | 0.1498 | 1217.3 |
| 318.15 | 0.2283 | 1215.2 |
| 318.15 | 0.2902 | 1213.5 |
| 318.15 | 0.3452 | 1212.0 |
| 318.15 | 0.4005 | 1210.4 |
| 318.15 | 0.4694 | 1208.2 |
| 318.15 | 0.5368 | 1205.9 |
| 318.15 | 0.6067 | 1203.4 |
| 318.15 | 0.6704 | 1200.9 |
| 318.15 | 0.7378 | 1198.3 |
| 318.15 | 0.8018 | 1195.7 |
| 318.15 | 0.8714 | 1192.8 |
| 318.15 | 0.9368 | 1190.0 |
| 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 | 1358.5 |
| 288.15 | 0.0718 | 1357.7 |
| 288.15 | 0.1498 | 1356.3 |
| 288.15 | 0.2283 | 1354.6 |
| 288.15 | 0.2902 | 1353.1 |
| 288.15 | 0.3452 | 1351.7 |
| 288.15 | 0.4005 | 1350.1 |
| 288.15 | 0.4694 | 1347.8 |
| 288.15 | 0.5368 | 1345.4 |
| 288.15 | 0.6067 | 1342.8 |
| 288.15 | 0.6704 | 1340.1 |
| 288.15 | 0.7378 | 1337.0 |
| 288.15 | 0.8018 | 1333.8 |
| 288.15 | 0.8714 | 1330.2 |
| 288.15 | 0.9368 | 1326.6 |
| 288.15 | 1.0000 | 1323.1 |
| 298.15 | 0.0000 | 1310.5 |
| 298.15 | 0.0718 | 1309.4 |
| 298.15 | 0.1498 | 1307.9 |
| 298.15 | 0.2283 | 1306.2 |
| 298.15 | 0.2902 | 1304.8 |
| 298.15 | 0.3452 | 1303.4 |
| 298.15 | 0.4005 | 1302.0 |
| 298.15 | 0.4694 | 1299.9 |
| 298.15 | 0.5368 | 1297.7 |
| 298.15 | 0.6067 | 1295.2 |
| 298.15 | 0.6704 | 1292.8 |
| 298.15 | 0.7378 | 1289.9 |
| 298.15 | 0.8018 | 1287.0 |
| 298.15 | 0.8714 | 1284.0 |
| 298.15 | 0.9368 | 1280.7 |
| 298.15 | 1.0000 | 1277.6 |
| 308.15 | 0.0000 | 1266.2 |
| 308.15 | 0.0718 | 1264.6 |
| 308.15 | 0.1498 | 1262.7 |
| 308.15 | 0.2283 | 1260.7 |
| 308.15 | 0.2902 | 1259.1 |
| 308.15 | 0.3452 | 1257.6 |
| 308.15 | 0.4005 | 1255.9 |
| 308.15 | 0.4694 | 1253.7 |
| 308.15 | 0.5368 | 1251.4 |
| 308.15 | 0.6067 | 1248.8 |
| 308.15 | 0.6704 | 1246.3 |
| 308.15 | 0.7378 | 1243.5 |
| 308.15 | 0.8018 | 1240.7 |
| 308.15 | 0.8714 | 1237.6 |
| 308.15 | 0.9368 | 1234.5 |
| 308.15 | 1.0000 | 1231.5 |
| 318.15 | 0.0000 | 1221.0 |
| 318.15 | 0.0718 | 1219.3 |
| 318.15 | 0.1498 | 1217.3 |
| 318.15 | 0.2283 | 1215.2 |
| 318.15 | 0.2902 | 1213.5 |
| 318.15 | 0.3452 | 1212.0 |
| 318.15 | 0.4005 | 1210.4 |
| 318.15 | 0.4694 | 1208.2 |
| 318.15 | 0.5368 | 1205.9 |
| 318.15 | 0.6067 | 1203.4 |
| 318.15 | 0.6704 | 1200.9 |
| 318.15 | 0.7378 | 1198.3 |
| 318.15 | 0.8018 | 1195.7 |
| 318.15 | 0.8714 | 1192.8 |
| 318.15 | 0.9368 | 1190.0 |
| 318.15 | 1.0000 | 1187.2 |
Sources
- 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