- Name
- o-Xylene
- InChI
- InChI=1S/C8H10/c1-7-5-3-4-6-8(7)2/h3-6H,1-2H3
- InChI Key
- CTQNGGLPUBDAKN-UHFFFAOYSA-N
- Formula
- C8H10
- SMILES
- Cc1ccccc1C
- Mol. Weight (g/mol)
- 106.17
- CAS
- 95-47-6
- 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
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
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 | 0.0009 |
| 288.15 | 0.0764 | 0.0008 |
| 288.15 | 0.1504 | 0.0008 |
| 288.15 | 0.2243 | 0.0008 |
| 288.15 | 0.2942 | 0.0008 |
| 288.15 | 0.3660 | 0.0007 |
| 288.15 | 0.4226 | 0.0007 |
| 288.15 | 0.4801 | 0.0007 |
| 288.15 | 0.5310 | 0.0007 |
| 288.15 | 0.5850 | 0.0007 |
| 288.15 | 0.6578 | 0.0006 |
| 288.15 | 0.7322 | 0.0006 |
| 288.15 | 0.8049 | 0.0006 |
| 288.15 | 0.8708 | 0.0006 |
| 288.15 | 0.9392 | 0.0005 |
| 288.15 | 1.0000 | 0.0005 |
| 298.15 | 0.0000 | 0.0008 |
| 298.15 | 0.0764 | 0.0007 |
| 298.15 | 0.1504 | 0.0007 |
| 298.15 | 0.2243 | 0.0007 |
| 298.15 | 0.2942 | 0.0007 |
| 298.15 | 0.3660 | 0.0007 |
| 298.15 | 0.4226 | 0.0006 |
| 298.15 | 0.4801 | 0.0006 |
| 298.15 | 0.5310 | 0.0006 |
| 298.15 | 0.5850 | 0.0006 |
| 298.15 | 0.6578 | 0.0006 |
| 298.15 | 0.7322 | 0.0005 |
| 298.15 | 0.8049 | 0.0005 |
| 298.15 | 0.8708 | 0.0005 |
| 298.15 | 0.9392 | 0.0005 |
| 298.15 | 1.0000 | 0.0005 |
| 308.15 | 0.0000 | 0.0007 |
| 308.15 | 0.0764 | 0.0007 |
| 308.15 | 0.1504 | 0.0006 |
| 308.15 | 0.2243 | 0.0006 |
| 308.15 | 0.2942 | 0.0006 |
| 308.15 | 0.3660 | 0.0006 |
| 308.15 | 0.4226 | 0.0006 |
| 308.15 | 0.4801 | 0.0006 |
| 308.15 | 0.5310 | 0.0005 |
| 308.15 | 0.5850 | 0.0005 |
| 308.15 | 0.6578 | 0.0005 |
| 308.15 | 0.7322 | 0.0005 |
| 308.15 | 0.8049 | 0.0005 |
| 308.15 | 0.8708 | 0.0005 |
| 308.15 | 0.9392 | 0.0004 |
| 308.15 | 1.0000 | 0.0004 |
| 318.15 | 0.0000 | 0.0006 |
| 318.15 | 0.0764 | 0.0006 |
| 318.15 | 0.1504 | 0.0006 |
| 318.15 | 0.2243 | 0.0006 |
| 318.15 | 0.2942 | 0.0005 |
| 318.15 | 0.3660 | 0.0005 |
| 318.15 | 0.4226 | 0.0005 |
| 318.15 | 0.4801 | 0.0005 |
| 318.15 | 0.5310 | 0.0005 |
| 318.15 | 0.5850 | 0.0005 |
| 318.15 | 0.6578 | 0.0005 |
| 318.15 | 0.7322 | 0.0004 |
| 318.15 | 0.8049 | 0.0004 |
| 318.15 | 0.8708 | 0.0004 |
| 318.15 | 0.9392 | 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 | 0.0009 |
| 288.15 | 0.0764 | 0.0008 |
| 288.15 | 0.1504 | 0.0008 |
| 288.15 | 0.2243 | 0.0008 |
| 288.15 | 0.2942 | 0.0008 |
| 288.15 | 0.3660 | 0.0007 |
| 288.15 | 0.4226 | 0.0007 |
| 288.15 | 0.4801 | 0.0007 |
| 288.15 | 0.5310 | 0.0007 |
| 288.15 | 0.5850 | 0.0007 |
| 288.15 | 0.6578 | 0.0006 |
| 288.15 | 0.7322 | 0.0006 |
| 288.15 | 0.8049 | 0.0006 |
| 288.15 | 0.8708 | 0.0006 |
| 288.15 | 0.9392 | 0.0005 |
| 288.15 | 1.0000 | 0.0005 |
| 298.15 | 0.0000 | 0.0008 |
| 298.15 | 0.0764 | 0.0007 |
| 298.15 | 0.1504 | 0.0007 |
| 298.15 | 0.2243 | 0.0007 |
| 298.15 | 0.2942 | 0.0007 |
| 298.15 | 0.3660 | 0.0007 |
| 298.15 | 0.4226 | 0.0006 |
| 298.15 | 0.4801 | 0.0006 |
| 298.15 | 0.5310 | 0.0006 |
| 298.15 | 0.5850 | 0.0006 |
| 298.15 | 0.6578 | 0.0006 |
| 298.15 | 0.7322 | 0.0005 |
| 298.15 | 0.8049 | 0.0005 |
| 298.15 | 0.8708 | 0.0005 |
| 298.15 | 0.9392 | 0.0005 |
| 298.15 | 1.0000 | 0.0005 |
| 308.15 | 0.0000 | 0.0007 |
| 308.15 | 0.0764 | 0.0007 |
| 308.15 | 0.1504 | 0.0006 |
| 308.15 | 0.2243 | 0.0006 |
| 308.15 | 0.2942 | 0.0006 |
| 308.15 | 0.3660 | 0.0006 |
| 308.15 | 0.4226 | 0.0006 |
| 308.15 | 0.4801 | 0.0006 |
| 308.15 | 0.5310 | 0.0005 |
| 308.15 | 0.5850 | 0.0005 |
| 308.15 | 0.6578 | 0.0005 |
| 308.15 | 0.7322 | 0.0005 |
| 308.15 | 0.8049 | 0.0005 |
| 308.15 | 0.8708 | 0.0005 |
| 308.15 | 0.9392 | 0.0004 |
| 308.15 | 1.0000 | 0.0004 |
| 318.15 | 0.0000 | 0.0006 |
| 318.15 | 0.0764 | 0.0006 |
| 318.15 | 0.1504 | 0.0006 |
| 318.15 | 0.2243 | 0.0006 |
| 318.15 | 0.2942 | 0.0005 |
| 318.15 | 0.3660 | 0.0005 |
| 318.15 | 0.4226 | 0.0005 |
| 318.15 | 0.4801 | 0.0005 |
| 318.15 | 0.5310 | 0.0005 |
| 318.15 | 0.5850 | 0.0005 |
| 318.15 | 0.6578 | 0.0005 |
| 318.15 | 0.7322 | 0.0004 |
| 318.15 | 0.8049 | 0.0004 |
| 318.15 | 0.8708 | 0.0004 |
| 318.15 | 0.9392 | 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 | 1.5083 |
| 288.15 | 0.0764 | 1.5032 |
| 288.15 | 0.1504 | 1.498 |
| 288.15 | 0.2243 | 1.4925 |
| 288.15 | 0.2942 | 1.487 |
| 288.15 | 0.3660 | 1.481 |
| 288.15 | 0.4226 | 1.4761 |
| 288.15 | 0.4801 | 1.4708 |
| 288.15 | 0.5310 | 1.4659 |
| 288.15 | 0.5850 | 1.4605 |
| 288.15 | 0.6578 | 1.4529 |
| 288.15 | 0.7322 | 1.4445 |
| 288.15 | 0.8049 | 1.4358 |
| 288.15 | 0.8708 | 1.4275 |
| 288.15 | 0.9392 | 1.4182 |
| 288.15 | 1.0000 | 1.4094 |
| 293.15 | 0.0000 | 1.5055 |
| 293.15 | 0.0764 | 1.5004 |
| 293.15 | 0.1504 | 1.4953 |
| 293.15 | 0.2243 | 1.4898 |
| 293.15 | 0.2942 | 1.4843 |
| 293.15 | 0.3660 | 1.4783 |
| 293.15 | 0.4226 | 1.4734 |
| 293.15 | 0.4801 | 1.4681 |
| 293.15 | 0.5310 | 1.4633 |
| 293.15 | 0.5850 | 1.4579 |
| 293.15 | 0.6578 | 1.4503 |
| 293.15 | 0.7322 | 1.4419 |
| 293.15 | 0.8049 | 1.4333 |
| 293.15 | 0.8708 | 1.425 |
| 293.15 | 0.9392 | 1.4157 |
| 293.15 | 1.0000 | 1.407 |
| 298.15 | 0.0000 | 1.5029 |
| 298.15 | 0.0764 | 1.4978 |
| 298.15 | 0.1504 | 1.4926 |
| 298.15 | 0.2243 | 1.4872 |
| 298.15 | 0.2942 | 1.4817 |
| 298.15 | 0.3660 | 1.4757 |
| 298.15 | 0.4226 | 1.4708 |
| 298.15 | 0.4801 | 1.4656 |
| 298.15 | 0.5310 | 1.4607 |
| 298.15 | 0.5850 | 1.4553 |
| 298.15 | 0.6578 | 1.4477 |
| 298.15 | 0.7322 | 1.4394 |
| 298.15 | 0.8049 | 1.4308 |
| 298.15 | 0.8708 | 1.4225 |
| 298.15 | 0.9392 | 1.4133 |
| 298.15 | 1.0000 | 1.4046 |
| 303.15 | 0.0000 | 1.5002 |
| 303.15 | 0.0764 | 1.4951 |
| 303.15 | 0.1504 | 1.49 |
| 303.15 | 0.2243 | 1.4845 |
| 303.15 | 0.2942 | 1.479 |
| 303.15 | 0.3660 | 1.4731 |
| 303.15 | 0.4226 | 1.4682 |
| 303.15 | 0.4801 | 1.463 |
| 303.15 | 0.5310 | 1.4582 |
| 303.15 | 0.5850 | 1.4528 |
| 303.15 | 0.6578 | 1.4452 |
| 303.15 | 0.7322 | 1.437 |
| 303.15 | 0.8049 | 1.4284 |
| 303.15 | 0.8708 | 1.4201 |
| 303.15 | 0.9392 | 1.4109 |
| 303.15 | 1.0000 | 1.4023 |
| 308.15 | 0.0000 | 1.4975 |
| 308.15 | 0.0764 | 1.4924 |
| 308.15 | 0.1504 | 1.4873 |
| 308.15 | 0.2243 | 1.4818 |
| 308.15 | 0.2942 | 1.4764 |
| 308.15 | 0.3660 | 1.4705 |
| 308.15 | 0.4226 | 1.4656 |
| 308.15 | 0.4801 | 1.4604 |
| 308.15 | 0.5310 | 1.4556 |
| 308.15 | 0.5850 | 1.4502 |
| 308.15 | 0.6578 | 1.4427 |
| 308.15 | 0.7322 | 1.4344 |
| 308.15 | 0.8049 | 1.4259 |
| 308.15 | 0.8708 | 1.4176 |
| 308.15 | 0.9392 | 1.4085 |
| 308.15 | 1.0000 | 1.3999 |
| 313.15 | 0.0000 | 1.4948 |
| 313.15 | 0.0764 | 1.4897 |
| 313.15 | 0.1504 | 1.4846 |
| 313.15 | 0.2243 | 1.4791 |
| 313.15 | 0.2942 | 1.4737 |
| 313.15 | 0.3660 | 1.4678 |
| 313.15 | 0.4226 | 1.4629 |
| 313.15 | 0.4801 | 1.4578 |
| 313.15 | 0.5310 | 1.453 |
| 313.15 | 0.5850 | 1.4476 |
| 313.15 | 0.6578 | 1.4401 |
| 313.15 | 0.7322 | 1.4319 |
| 313.15 | 0.8049 | 1.4234 |
| 313.15 | 0.8708 | 1.4151 |
| 313.15 | 0.9392 | 1.4061 |
| 313.15 | 1.0000 | 1.3975 |
| 318.15 | 0.0000 | 1.4921 |
| 318.15 | 0.0764 | 1.487 |
| 318.15 | 0.1504 | 1.4819 |
| 318.15 | 0.2243 | 1.4765 |
| 318.15 | 0.2942 | 1.4711 |
| 318.15 | 0.3660 | 1.4652 |
| 318.15 | 0.4226 | 1.4603 |
| 318.15 | 0.4801 | 1.4551 |
| 318.15 | 0.5310 | 1.4504 |
| 318.15 | 0.5850 | 1.4451 |
| 318.15 | 0.6578 | 1.4375 |
| 318.15 | 0.7322 | 1.4294 |
| 318.15 | 0.8049 | 1.4209 |
| 318.15 | 0.8708 | 1.4127 |
| 318.15 | 0.9392 | 1.4036 |
| 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 | 1.5083 |
| 288.15 | 0.0764 | 1.5032 |
| 288.15 | 0.1504 | 1.498 |
| 288.15 | 0.2243 | 1.4925 |
| 288.15 | 0.2942 | 1.487 |
| 288.15 | 0.3660 | 1.481 |
| 288.15 | 0.4226 | 1.4761 |
| 288.15 | 0.4801 | 1.4708 |
| 288.15 | 0.5310 | 1.4659 |
| 288.15 | 0.5850 | 1.4605 |
| 288.15 | 0.6578 | 1.4529 |
| 288.15 | 0.7322 | 1.4445 |
| 288.15 | 0.8049 | 1.4358 |
| 288.15 | 0.8708 | 1.4275 |
| 288.15 | 0.9392 | 1.4182 |
| 288.15 | 1.0000 | 1.4094 |
| 293.15 | 0.0000 | 1.5055 |
| 293.15 | 0.0764 | 1.5004 |
| 293.15 | 0.1504 | 1.4953 |
| 293.15 | 0.2243 | 1.4898 |
| 293.15 | 0.2942 | 1.4843 |
| 293.15 | 0.3660 | 1.4783 |
| 293.15 | 0.4226 | 1.4734 |
| 293.15 | 0.4801 | 1.4681 |
| 293.15 | 0.5310 | 1.4633 |
| 293.15 | 0.5850 | 1.4579 |
| 293.15 | 0.6578 | 1.4503 |
| 293.15 | 0.7322 | 1.4419 |
| 293.15 | 0.8049 | 1.4333 |
| 293.15 | 0.8708 | 1.425 |
| 293.15 | 0.9392 | 1.4157 |
| 293.15 | 1.0000 | 1.407 |
| 298.15 | 0.0000 | 1.5029 |
| 298.15 | 0.0764 | 1.4978 |
| 298.15 | 0.1504 | 1.4926 |
| 298.15 | 0.2243 | 1.4872 |
| 298.15 | 0.2942 | 1.4817 |
| 298.15 | 0.3660 | 1.4757 |
| 298.15 | 0.4226 | 1.4708 |
| 298.15 | 0.4801 | 1.4656 |
| 298.15 | 0.5310 | 1.4607 |
| 298.15 | 0.5850 | 1.4553 |
| 298.15 | 0.6578 | 1.4477 |
| 298.15 | 0.7322 | 1.4394 |
| 298.15 | 0.8049 | 1.4308 |
| 298.15 | 0.8708 | 1.4225 |
| 298.15 | 0.9392 | 1.4133 |
| 298.15 | 1.0000 | 1.4046 |
| 303.15 | 0.0000 | 1.5002 |
| 303.15 | 0.0764 | 1.4951 |
| 303.15 | 0.1504 | 1.49 |
| 303.15 | 0.2243 | 1.4845 |
| 303.15 | 0.2942 | 1.479 |
| 303.15 | 0.3660 | 1.4731 |
| 303.15 | 0.4226 | 1.4682 |
| 303.15 | 0.4801 | 1.463 |
| 303.15 | 0.5310 | 1.4582 |
| 303.15 | 0.5850 | 1.4528 |
| 303.15 | 0.6578 | 1.4452 |
| 303.15 | 0.7322 | 1.437 |
| 303.15 | 0.8049 | 1.4284 |
| 303.15 | 0.8708 | 1.4201 |
| 303.15 | 0.9392 | 1.4109 |
| 303.15 | 1.0000 | 1.4023 |
| 308.15 | 0.0000 | 1.4975 |
| 308.15 | 0.0764 | 1.4924 |
| 308.15 | 0.1504 | 1.4873 |
| 308.15 | 0.2243 | 1.4818 |
| 308.15 | 0.2942 | 1.4764 |
| 308.15 | 0.3660 | 1.4705 |
| 308.15 | 0.4226 | 1.4656 |
| 308.15 | 0.4801 | 1.4604 |
| 308.15 | 0.5310 | 1.4556 |
| 308.15 | 0.5850 | 1.4502 |
| 308.15 | 0.6578 | 1.4427 |
| 308.15 | 0.7322 | 1.4344 |
| 308.15 | 0.8049 | 1.4259 |
| 308.15 | 0.8708 | 1.4176 |
| 308.15 | 0.9392 | 1.4085 |
| 308.15 | 1.0000 | 1.3999 |
| 313.15 | 0.0000 | 1.4948 |
| 313.15 | 0.0764 | 1.4897 |
| 313.15 | 0.1504 | 1.4846 |
| 313.15 | 0.2243 | 1.4791 |
| 313.15 | 0.2942 | 1.4737 |
| 313.15 | 0.3660 | 1.4678 |
| 313.15 | 0.4226 | 1.4629 |
| 313.15 | 0.4801 | 1.4578 |
| 313.15 | 0.5310 | 1.453 |
| 313.15 | 0.5850 | 1.4476 |
| 313.15 | 0.6578 | 1.4401 |
| 313.15 | 0.7322 | 1.4319 |
| 313.15 | 0.8049 | 1.4234 |
| 313.15 | 0.8708 | 1.4151 |
| 313.15 | 0.9392 | 1.4061 |
| 313.15 | 1.0000 | 1.3975 |
| 318.15 | 0.0000 | 1.4921 |
| 318.15 | 0.0764 | 1.487 |
| 318.15 | 0.1504 | 1.4819 |
| 318.15 | 0.2243 | 1.4765 |
| 318.15 | 0.2942 | 1.4711 |
| 318.15 | 0.3660 | 1.4652 |
| 318.15 | 0.4226 | 1.4603 |
| 318.15 | 0.4801 | 1.4551 |
| 318.15 | 0.5310 | 1.4504 |
| 318.15 | 0.5850 | 1.4451 |
| 318.15 | 0.6578 | 1.4375 |
| 318.15 | 0.7322 | 1.4294 |
| 318.15 | 0.8049 | 1.4209 |
| 318.15 | 0.8708 | 1.4127 |
| 318.15 | 0.9392 | 1.4036 |
| 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 | 1388.5 |
| 288.15 | 0.0764 | 1384.3 |
| 288.15 | 0.1504 | 1380.0 |
| 288.15 | 0.2243 | 1375.7 |
| 288.15 | 0.2942 | 1371.4 |
| 288.15 | 0.3660 | 1366.9 |
| 288.15 | 0.4226 | 1363.4 |
| 288.15 | 0.4801 | 1359.7 |
| 288.15 | 0.5310 | 1356.3 |
| 288.15 | 0.5850 | 1352.6 |
| 288.15 | 0.6578 | 1347.6 |
| 288.15 | 0.7322 | 1342.5 |
| 288.15 | 0.8049 | 1337.4 |
| 288.15 | 0.8708 | 1332.6 |
| 288.15 | 0.9392 | 1327.7 |
| 288.15 | 1.0000 | 1323.1 |
| 298.15 | 0.0000 | 1350.3 |
| 298.15 | 0.0764 | 1345.1 |
| 298.15 | 0.1504 | 1340.0 |
| 298.15 | 0.2243 | 1335.0 |
| 298.15 | 0.2942 | 1330.0 |
| 298.15 | 0.3660 | 1324.9 |
| 298.15 | 0.4226 | 1320.9 |
| 298.15 | 0.4801 | 1316.7 |
| 298.15 | 0.5310 | 1313.0 |
| 298.15 | 0.5850 | 1309.0 |
| 298.15 | 0.6578 | 1303.6 |
| 298.15 | 0.7322 | 1298.0 |
| 298.15 | 0.8049 | 1292.5 |
| 298.15 | 0.8708 | 1287.5 |
| 298.15 | 0.9392 | 1282.3 |
| 298.15 | 1.0000 | 1277.6 |
| 308.15 | 0.0000 | 1321.4 |
| 308.15 | 0.0764 | 1314.5 |
| 308.15 | 0.1504 | 1307.8 |
| 308.15 | 0.2243 | 1301.1 |
| 308.15 | 0.2942 | 1294.8 |
| 308.15 | 0.3660 | 1288.3 |
| 308.15 | 0.4226 | 1283.2 |
| 308.15 | 0.4801 | 1278.0 |
| 308.15 | 0.5310 | 1273.4 |
| 308.15 | 0.5850 | 1268.5 |
| 308.15 | 0.6578 | 1262.0 |
| 308.15 | 0.7322 | 1255.4 |
| 308.15 | 0.8049 | 1248.9 |
| 308.15 | 0.8708 | 1243.0 |
| 308.15 | 0.9392 | 1236.9 |
| 308.15 | 1.0000 | 1231.5 |
| 318.15 | 0.0000 | 1285.8 |
| 318.15 | 0.0764 | 1277.9 |
| 318.15 | 0.1504 | 1270.2 |
| 318.15 | 0.2243 | 1262.7 |
| 318.15 | 0.2942 | 1255.6 |
| 318.15 | 0.3660 | 1248.4 |
| 318.15 | 0.4226 | 1242.8 |
| 318.15 | 0.4801 | 1237.1 |
| 318.15 | 0.5310 | 1232.1 |
| 318.15 | 0.5850 | 1226.8 |
| 318.15 | 0.6578 | 1219.7 |
| 318.15 | 0.7322 | 1212.5 |
| 318.15 | 0.8049 | 1205.6 |
| 318.15 | 0.8708 | 1199.3 |
| 318.15 | 0.9392 | 1192.9 |
| 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 | 1388.5 |
| 288.15 | 0.0764 | 1384.3 |
| 288.15 | 0.1504 | 1380.0 |
| 288.15 | 0.2243 | 1375.7 |
| 288.15 | 0.2942 | 1371.4 |
| 288.15 | 0.3660 | 1366.9 |
| 288.15 | 0.4226 | 1363.4 |
| 288.15 | 0.4801 | 1359.7 |
| 288.15 | 0.5310 | 1356.3 |
| 288.15 | 0.5850 | 1352.6 |
| 288.15 | 0.6578 | 1347.6 |
| 288.15 | 0.7322 | 1342.5 |
| 288.15 | 0.8049 | 1337.4 |
| 288.15 | 0.8708 | 1332.6 |
| 288.15 | 0.9392 | 1327.7 |
| 288.15 | 1.0000 | 1323.1 |
| 298.15 | 0.0000 | 1350.3 |
| 298.15 | 0.0764 | 1345.1 |
| 298.15 | 0.1504 | 1340.0 |
| 298.15 | 0.2243 | 1335.0 |
| 298.15 | 0.2942 | 1330.0 |
| 298.15 | 0.3660 | 1324.9 |
| 298.15 | 0.4226 | 1320.9 |
| 298.15 | 0.4801 | 1316.7 |
| 298.15 | 0.5310 | 1313.0 |
| 298.15 | 0.5850 | 1309.0 |
| 298.15 | 0.6578 | 1303.6 |
| 298.15 | 0.7322 | 1298.0 |
| 298.15 | 0.8049 | 1292.5 |
| 298.15 | 0.8708 | 1287.5 |
| 298.15 | 0.9392 | 1282.3 |
| 298.15 | 1.0000 | 1277.6 |
| 308.15 | 0.0000 | 1321.4 |
| 308.15 | 0.0764 | 1314.5 |
| 308.15 | 0.1504 | 1307.8 |
| 308.15 | 0.2243 | 1301.1 |
| 308.15 | 0.2942 | 1294.8 |
| 308.15 | 0.3660 | 1288.3 |
| 308.15 | 0.4226 | 1283.2 |
| 308.15 | 0.4801 | 1278.0 |
| 308.15 | 0.5310 | 1273.4 |
| 308.15 | 0.5850 | 1268.5 |
| 308.15 | 0.6578 | 1262.0 |
| 308.15 | 0.7322 | 1255.4 |
| 308.15 | 0.8049 | 1248.9 |
| 308.15 | 0.8708 | 1243.0 |
| 308.15 | 0.9392 | 1236.9 |
| 308.15 | 1.0000 | 1231.5 |
| 318.15 | 0.0000 | 1285.8 |
| 318.15 | 0.0764 | 1277.9 |
| 318.15 | 0.1504 | 1270.2 |
| 318.15 | 0.2243 | 1262.7 |
| 318.15 | 0.2942 | 1255.6 |
| 318.15 | 0.3660 | 1248.4 |
| 318.15 | 0.4226 | 1242.8 |
| 318.15 | 0.4801 | 1237.1 |
| 318.15 | 0.5310 | 1232.1 |
| 318.15 | 0.5850 | 1226.8 |
| 318.15 | 0.6578 | 1219.7 |
| 318.15 | 0.7322 | 1212.5 |
| 318.15 | 0.8049 | 1205.6 |
| 318.15 | 0.8708 | 1199.3 |
| 318.15 | 0.9392 | 1192.9 |
| 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