- 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
- Name
- Mesitylene
- InChI
- InChI=1S/C9H12/c1-7-4-8(2)6-9(3)5-7/h4-6H,1-3H3
- InChI Key
- AUHZEENZYGFFBQ-UHFFFAOYSA-N
- Formula
- C9H12
- SMILES
- Cc1cc(C)cc(C)c1
- Mol. Weight (g/mol)
- 120.19
- CAS
- 108-67-8
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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)
- γ - Surface tension liquid-gas, N/m (2)
- Excess molar volume, m3/mol (2)
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Tetrahydrofuran (1) - Liquid | Viscosity, Pa*s - Liquid |
| 288.15 | 0.0000 | 0.0008 |
| 288.15 | 0.0735 | 0.0007 |
| 288.15 | 0.1513 | 0.0007 |
| 288.15 | 0.2274 | 0.0007 |
| 288.15 | 0.2986 | 0.0007 |
| 288.15 | 0.3672 | 0.0007 |
| 288.15 | 0.4305 | 0.0007 |
| 288.15 | 0.4912 | 0.0006 |
| 288.15 | 0.5496 | 0.0006 |
| 288.15 | 0.6055 | 0.0006 |
| 288.15 | 0.6784 | 0.0006 |
| 288.15 | 0.7516 | 0.0006 |
| 288.15 | 0.8280 | 0.0006 |
| 288.15 | 0.8790 | 0.0005 |
| 288.15 | 0.9412 | 0.0005 |
| 288.15 | 1.0000 | 0.0005 |
| 298.15 | 0.0000 | 0.0007 |
| 298.15 | 0.0735 | 0.0006 |
| 298.15 | 0.1513 | 0.0006 |
| 298.15 | 0.2274 | 0.0006 |
| 298.15 | 0.2986 | 0.0006 |
| 298.15 | 0.3672 | 0.0006 |
| 298.15 | 0.4305 | 0.0006 |
| 298.15 | 0.4912 | 0.0006 |
| 298.15 | 0.5496 | 0.0006 |
| 298.15 | 0.6055 | 0.0005 |
| 298.15 | 0.6784 | 0.0005 |
| 298.15 | 0.7516 | 0.0005 |
| 298.15 | 0.8280 | 0.0005 |
| 298.15 | 0.8790 | 0.0005 |
| 298.15 | 0.9412 | 0.0005 |
| 298.15 | 1.0000 | 0.0005 |
| 308.15 | 0.0000 | 0.0006 |
| 308.15 | 0.0735 | 0.0006 |
| 308.15 | 0.1513 | 0.0006 |
| 308.15 | 0.2274 | 0.0006 |
| 308.15 | 0.2986 | 0.0005 |
| 308.15 | 0.3672 | 0.0005 |
| 308.15 | 0.4305 | 0.0005 |
| 308.15 | 0.4912 | 0.0005 |
| 308.15 | 0.5496 | 0.0005 |
| 308.15 | 0.6055 | 0.0005 |
| 308.15 | 0.6784 | 0.0005 |
| 308.15 | 0.7516 | 0.0005 |
| 308.15 | 0.8280 | 0.0004 |
| 308.15 | 0.8790 | 0.0004 |
| 308.15 | 0.9412 | 0.0004 |
| 308.15 | 1.0000 | 0.0004 |
| 318.15 | 0.0000 | 0.0005 |
| 318.15 | 0.0735 | 0.0005 |
| 318.15 | 0.1513 | 0.0005 |
| 318.15 | 0.2274 | 0.0005 |
| 318.15 | 0.2986 | 0.0005 |
| 318.15 | 0.3672 | 0.0005 |
| 318.15 | 0.4305 | 0.0005 |
| 318.15 | 0.4912 | 0.0005 |
| 318.15 | 0.5496 | 0.0005 |
| 318.15 | 0.6055 | 0.0004 |
| 318.15 | 0.6784 | 0.0004 |
| 318.15 | 0.7516 | 0.0004 |
| 318.15 | 0.8280 | 0.0004 |
| 318.15 | 0.8790 | 0.0004 |
| 318.15 | 0.9412 | 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 (1) - Liquid | Viscosity, Pa*s - Liquid |
| 288.15 | 0.0000 | 0.0008 |
| 288.15 | 0.0735 | 0.0007 |
| 288.15 | 0.1513 | 0.0007 |
| 288.15 | 0.2274 | 0.0007 |
| 288.15 | 0.2986 | 0.0007 |
| 288.15 | 0.3672 | 0.0007 |
| 288.15 | 0.4305 | 0.0007 |
| 288.15 | 0.4912 | 0.0006 |
| 288.15 | 0.5496 | 0.0006 |
| 288.15 | 0.6055 | 0.0006 |
| 288.15 | 0.6784 | 0.0006 |
| 288.15 | 0.7516 | 0.0006 |
| 288.15 | 0.8280 | 0.0006 |
| 288.15 | 0.8790 | 0.0005 |
| 288.15 | 0.9412 | 0.0005 |
| 288.15 | 1.0000 | 0.0005 |
| 298.15 | 0.0000 | 0.0007 |
| 298.15 | 0.0735 | 0.0006 |
| 298.15 | 0.1513 | 0.0006 |
| 298.15 | 0.2274 | 0.0006 |
| 298.15 | 0.2986 | 0.0006 |
| 298.15 | 0.3672 | 0.0006 |
| 298.15 | 0.4305 | 0.0006 |
| 298.15 | 0.4912 | 0.0006 |
| 298.15 | 0.5496 | 0.0006 |
| 298.15 | 0.6055 | 0.0005 |
| 298.15 | 0.6784 | 0.0005 |
| 298.15 | 0.7516 | 0.0005 |
| 298.15 | 0.8280 | 0.0005 |
| 298.15 | 0.8790 | 0.0005 |
| 298.15 | 0.9412 | 0.0005 |
| 298.15 | 1.0000 | 0.0005 |
| 308.15 | 0.0000 | 0.0006 |
| 308.15 | 0.0735 | 0.0006 |
| 308.15 | 0.1513 | 0.0006 |
| 308.15 | 0.2274 | 0.0006 |
| 308.15 | 0.2986 | 0.0005 |
| 308.15 | 0.3672 | 0.0005 |
| 308.15 | 0.4305 | 0.0005 |
| 308.15 | 0.4912 | 0.0005 |
| 308.15 | 0.5496 | 0.0005 |
| 308.15 | 0.6055 | 0.0005 |
| 308.15 | 0.6784 | 0.0005 |
| 308.15 | 0.7516 | 0.0005 |
| 308.15 | 0.8280 | 0.0004 |
| 308.15 | 0.8790 | 0.0004 |
| 308.15 | 0.9412 | 0.0004 |
| 308.15 | 1.0000 | 0.0004 |
| 318.15 | 0.0000 | 0.0005 |
| 318.15 | 0.0735 | 0.0005 |
| 318.15 | 0.1513 | 0.0005 |
| 318.15 | 0.2274 | 0.0005 |
| 318.15 | 0.2986 | 0.0005 |
| 318.15 | 0.3672 | 0.0005 |
| 318.15 | 0.4305 | 0.0005 |
| 318.15 | 0.4912 | 0.0005 |
| 318.15 | 0.5496 | 0.0005 |
| 318.15 | 0.6055 | 0.0004 |
| 318.15 | 0.6784 | 0.0004 |
| 318.15 | 0.7516 | 0.0004 |
| 318.15 | 0.8280 | 0.0004 |
| 318.15 | 0.8790 | 0.0004 |
| 318.15 | 0.9412 | 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 (1) - Liquid | Refractive index (Na D-line) - Liquid |
| 288.15 | 0.0000 | 1.502 |
| 288.15 | 0.0735 | 1.4977 |
| 288.15 | 0.1513 | 1.4928 |
| 288.15 | 0.2274 | 1.4878 |
| 288.15 | 0.2986 | 1.4827 |
| 288.15 | 0.3672 | 1.4776 |
| 288.15 | 0.4305 | 1.4726 |
| 288.15 | 0.4912 | 1.4675 |
| 288.15 | 0.5496 | 1.4624 |
| 288.15 | 0.6055 | 1.4572 |
| 288.15 | 0.6784 | 1.4499 |
| 288.15 | 0.7516 | 1.4419 |
| 288.15 | 0.8280 | 1.433 |
| 288.15 | 0.8790 | 1.4265 |
| 288.15 | 0.9412 | 1.4181 |
| 288.15 | 1.0000 | 1.4094 |
| 293.15 | 0.0000 | 1.4995 |
| 293.15 | 0.0735 | 1.4952 |
| 293.15 | 0.1513 | 1.4903 |
| 293.15 | 0.2274 | 1.4852 |
| 293.15 | 0.2986 | 1.4802 |
| 293.15 | 0.3672 | 1.4751 |
| 293.15 | 0.4305 | 1.4701 |
| 293.15 | 0.4912 | 1.465 |
| 293.15 | 0.5496 | 1.4599 |
| 293.15 | 0.6055 | 1.4547 |
| 293.15 | 0.6784 | 1.4474 |
| 293.15 | 0.7516 | 1.4395 |
| 293.15 | 0.8280 | 1.4305 |
| 293.15 | 0.8790 | 1.4241 |
| 293.15 | 0.9412 | 1.4157 |
| 293.15 | 1.0000 | 1.407 |
| 298.15 | 0.0000 | 1.4969 |
| 298.15 | 0.0735 | 1.4925 |
| 298.15 | 0.1513 | 1.4877 |
| 298.15 | 0.2274 | 1.4826 |
| 298.15 | 0.2986 | 1.4776 |
| 298.15 | 0.3672 | 1.4725 |
| 298.15 | 0.4305 | 1.4675 |
| 298.15 | 0.4912 | 1.4625 |
| 298.15 | 0.5496 | 1.4573 |
| 298.15 | 0.6055 | 1.4521 |
| 298.15 | 0.6784 | 1.4448 |
| 298.15 | 0.7516 | 1.437 |
| 298.15 | 0.8280 | 1.428 |
| 298.15 | 0.8790 | 1.4216 |
| 298.15 | 0.9412 | 1.4132 |
| 298.15 | 1.0000 | 1.4046 |
| 303.15 | 0.0000 | 1.4944 |
| 303.15 | 0.0735 | 1.49 |
| 303.15 | 0.1513 | 1.4851 |
| 303.15 | 0.2274 | 1.4801 |
| 303.15 | 0.2986 | 1.4751 |
| 303.15 | 0.3672 | 1.47 |
| 303.15 | 0.4305 | 1.465 |
| 303.15 | 0.4912 | 1.46 |
| 303.15 | 0.5496 | 1.4549 |
| 303.15 | 0.6055 | 1.4497 |
| 303.15 | 0.6784 | 1.4424 |
| 303.15 | 0.7516 | 1.4346 |
| 303.15 | 0.8280 | 1.4256 |
| 303.15 | 0.8790 | 1.4192 |
| 303.15 | 0.9412 | 1.4109 |
| 303.15 | 1.0000 | 1.4023 |
| 308.15 | 0.0000 | 1.4918 |
| 308.15 | 0.0735 | 1.4874 |
| 308.15 | 0.1513 | 1.4825 |
| 308.15 | 0.2274 | 1.4775 |
| 308.15 | 0.2986 | 1.4725 |
| 308.15 | 0.3672 | 1.4674 |
| 308.15 | 0.4305 | 1.4625 |
| 308.15 | 0.4912 | 1.4574 |
| 308.15 | 0.5496 | 1.4523 |
| 308.15 | 0.6055 | 1.4471 |
| 308.15 | 0.6784 | 1.4399 |
| 308.15 | 0.7516 | 1.432 |
| 308.15 | 0.8280 | 1.4231 |
| 308.15 | 0.8790 | 1.4167 |
| 308.15 | 0.9412 | 1.4084 |
| 308.15 | 1.0000 | 1.3999 |
| 313.15 | 0.0000 | 1.4893 |
| 313.15 | 0.0735 | 1.4849 |
| 313.15 | 0.1513 | 1.48 |
| 313.15 | 0.2274 | 1.4749 |
| 313.15 | 0.2986 | 1.47 |
| 313.15 | 0.3672 | 1.4649 |
| 313.15 | 0.4305 | 1.4599 |
| 313.15 | 0.4912 | 1.4549 |
| 313.15 | 0.5496 | 1.4498 |
| 313.15 | 0.6055 | 1.4446 |
| 313.15 | 0.6784 | 1.4374 |
| 313.15 | 0.7516 | 1.4295 |
| 313.15 | 0.8280 | 1.4206 |
| 313.15 | 0.8790 | 1.4142 |
| 313.15 | 0.9412 | 1.4059 |
| 313.15 | 1.0000 | 1.3975 |
| 318.15 | 0.0000 | 1.4868 |
| 318.15 | 0.0735 | 1.4823 |
| 318.15 | 0.1513 | 1.4774 |
| 318.15 | 0.2274 | 1.4724 |
| 318.15 | 0.2986 | 1.4675 |
| 318.15 | 0.3672 | 1.4624 |
| 318.15 | 0.4305 | 1.4574 |
| 318.15 | 0.4912 | 1.4524 |
| 318.15 | 0.5496 | 1.4473 |
| 318.15 | 0.6055 | 1.4421 |
| 318.15 | 0.6784 | 1.4349 |
| 318.15 | 0.7516 | 1.427 |
| 318.15 | 0.8280 | 1.4181 |
| 318.15 | 0.8790 | 1.4118 |
| 318.15 | 0.9412 | 1.4035 |
| 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 (1) - Liquid | Refractive index (Na D-line) - Liquid |
| 288.15 | 0.0000 | 1.502 |
| 288.15 | 0.0735 | 1.4977 |
| 288.15 | 0.1513 | 1.4928 |
| 288.15 | 0.2274 | 1.4878 |
| 288.15 | 0.2986 | 1.4827 |
| 288.15 | 0.3672 | 1.4776 |
| 288.15 | 0.4305 | 1.4726 |
| 288.15 | 0.4912 | 1.4675 |
| 288.15 | 0.5496 | 1.4624 |
| 288.15 | 0.6055 | 1.4572 |
| 288.15 | 0.6784 | 1.4499 |
| 288.15 | 0.7516 | 1.4419 |
| 288.15 | 0.8280 | 1.433 |
| 288.15 | 0.8790 | 1.4265 |
| 288.15 | 0.9412 | 1.4181 |
| 288.15 | 1.0000 | 1.4094 |
| 293.15 | 0.0000 | 1.4995 |
| 293.15 | 0.0735 | 1.4952 |
| 293.15 | 0.1513 | 1.4903 |
| 293.15 | 0.2274 | 1.4852 |
| 293.15 | 0.2986 | 1.4802 |
| 293.15 | 0.3672 | 1.4751 |
| 293.15 | 0.4305 | 1.4701 |
| 293.15 | 0.4912 | 1.465 |
| 293.15 | 0.5496 | 1.4599 |
| 293.15 | 0.6055 | 1.4547 |
| 293.15 | 0.6784 | 1.4474 |
| 293.15 | 0.7516 | 1.4395 |
| 293.15 | 0.8280 | 1.4305 |
| 293.15 | 0.8790 | 1.4241 |
| 293.15 | 0.9412 | 1.4157 |
| 293.15 | 1.0000 | 1.407 |
| 298.15 | 0.0000 | 1.4969 |
| 298.15 | 0.0735 | 1.4925 |
| 298.15 | 0.1513 | 1.4877 |
| 298.15 | 0.2274 | 1.4826 |
| 298.15 | 0.2986 | 1.4776 |
| 298.15 | 0.3672 | 1.4725 |
| 298.15 | 0.4305 | 1.4675 |
| 298.15 | 0.4912 | 1.4625 |
| 298.15 | 0.5496 | 1.4573 |
| 298.15 | 0.6055 | 1.4521 |
| 298.15 | 0.6784 | 1.4448 |
| 298.15 | 0.7516 | 1.437 |
| 298.15 | 0.8280 | 1.428 |
| 298.15 | 0.8790 | 1.4216 |
| 298.15 | 0.9412 | 1.4132 |
| 298.15 | 1.0000 | 1.4046 |
| 303.15 | 0.0000 | 1.4944 |
| 303.15 | 0.0735 | 1.49 |
| 303.15 | 0.1513 | 1.4851 |
| 303.15 | 0.2274 | 1.4801 |
| 303.15 | 0.2986 | 1.4751 |
| 303.15 | 0.3672 | 1.47 |
| 303.15 | 0.4305 | 1.465 |
| 303.15 | 0.4912 | 1.46 |
| 303.15 | 0.5496 | 1.4549 |
| 303.15 | 0.6055 | 1.4497 |
| 303.15 | 0.6784 | 1.4424 |
| 303.15 | 0.7516 | 1.4346 |
| 303.15 | 0.8280 | 1.4256 |
| 303.15 | 0.8790 | 1.4192 |
| 303.15 | 0.9412 | 1.4109 |
| 303.15 | 1.0000 | 1.4023 |
| 308.15 | 0.0000 | 1.4918 |
| 308.15 | 0.0735 | 1.4874 |
| 308.15 | 0.1513 | 1.4825 |
| 308.15 | 0.2274 | 1.4775 |
| 308.15 | 0.2986 | 1.4725 |
| 308.15 | 0.3672 | 1.4674 |
| 308.15 | 0.4305 | 1.4625 |
| 308.15 | 0.4912 | 1.4574 |
| 308.15 | 0.5496 | 1.4523 |
| 308.15 | 0.6055 | 1.4471 |
| 308.15 | 0.6784 | 1.4399 |
| 308.15 | 0.7516 | 1.432 |
| 308.15 | 0.8280 | 1.4231 |
| 308.15 | 0.8790 | 1.4167 |
| 308.15 | 0.9412 | 1.4084 |
| 308.15 | 1.0000 | 1.3999 |
| 313.15 | 0.0000 | 1.4893 |
| 313.15 | 0.0735 | 1.4849 |
| 313.15 | 0.1513 | 1.48 |
| 313.15 | 0.2274 | 1.4749 |
| 313.15 | 0.2986 | 1.47 |
| 313.15 | 0.3672 | 1.4649 |
| 313.15 | 0.4305 | 1.4599 |
| 313.15 | 0.4912 | 1.4549 |
| 313.15 | 0.5496 | 1.4498 |
| 313.15 | 0.6055 | 1.4446 |
| 313.15 | 0.6784 | 1.4374 |
| 313.15 | 0.7516 | 1.4295 |
| 313.15 | 0.8280 | 1.4206 |
| 313.15 | 0.8790 | 1.4142 |
| 313.15 | 0.9412 | 1.4059 |
| 313.15 | 1.0000 | 1.3975 |
| 318.15 | 0.0000 | 1.4868 |
| 318.15 | 0.0735 | 1.4823 |
| 318.15 | 0.1513 | 1.4774 |
| 318.15 | 0.2274 | 1.4724 |
| 318.15 | 0.2986 | 1.4675 |
| 318.15 | 0.3672 | 1.4624 |
| 318.15 | 0.4305 | 1.4574 |
| 318.15 | 0.4912 | 1.4524 |
| 318.15 | 0.5496 | 1.4473 |
| 318.15 | 0.6055 | 1.4421 |
| 318.15 | 0.6784 | 1.4349 |
| 318.15 | 0.7516 | 1.427 |
| 318.15 | 0.8280 | 1.4181 |
| 318.15 | 0.8790 | 1.4118 |
| 318.15 | 0.9412 | 1.4035 |
| 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 (1) - Liquid | Speed of sound, m/s - Liquid |
| 288.15 | 0.0000 | 1412.3 |
| 288.15 | 0.0735 | 1406.8 |
| 288.15 | 0.1513 | 1400.3 |
| 288.15 | 0.2274 | 1393.5 |
| 288.15 | 0.2986 | 1386.7 |
| 288.15 | 0.3672 | 1379.7 |
| 288.15 | 0.4305 | 1373.5 |
| 288.15 | 0.4912 | 1367.5 |
| 288.15 | 0.5496 | 1361.9 |
| 288.15 | 0.6055 | 1356.8 |
| 288.15 | 0.6784 | 1350.4 |
| 288.15 | 0.7516 | 1344.0 |
| 288.15 | 0.8280 | 1337.4 |
| 288.15 | 0.8790 | 1333.2 |
| 288.15 | 0.9412 | 1328.2 |
| 288.15 | 1.0000 | 1323.1 |
| 298.15 | 0.0000 | 1369.8 |
| 298.15 | 0.0735 | 1363.6 |
| 298.15 | 0.1513 | 1356.6 |
| 298.15 | 0.2274 | 1349.5 |
| 298.15 | 0.2986 | 1342.4 |
| 298.15 | 0.3672 | 1335.3 |
| 298.15 | 0.4305 | 1328.9 |
| 298.15 | 0.4912 | 1322.9 |
| 298.15 | 0.5496 | 1317.3 |
| 298.15 | 0.6055 | 1312.0 |
| 298.15 | 0.6784 | 1305.4 |
| 298.15 | 0.7516 | 1298.8 |
| 298.15 | 0.8280 | 1292.1 |
| 298.15 | 0.8790 | 1287.7 |
| 298.15 | 0.9412 | 1282.6 |
| 298.15 | 1.0000 | 1277.6 |
| 308.15 | 0.0000 | 1325.2 |
| 308.15 | 0.0735 | 1318.5 |
| 308.15 | 0.1513 | 1311.2 |
| 308.15 | 0.2274 | 1303.9 |
| 308.15 | 0.2986 | 1296.7 |
| 308.15 | 0.3672 | 1289.6 |
| 308.15 | 0.4305 | 1283.1 |
| 308.15 | 0.4912 | 1277.0 |
| 308.15 | 0.5496 | 1271.4 |
| 308.15 | 0.6055 | 1266.1 |
| 308.15 | 0.6784 | 1259.4 |
| 308.15 | 0.7516 | 1252.8 |
| 308.15 | 0.8280 | 1246.0 |
| 308.15 | 0.8790 | 1241.6 |
| 308.15 | 0.9412 | 1236.4 |
| 308.15 | 1.0000 | 1231.5 |
| 318.15 | 0.0000 | 1279.0 |
| 318.15 | 0.0735 | 1272.2 |
| 318.15 | 0.1513 | 1264.9 |
| 318.15 | 0.2274 | 1257.7 |
| 318.15 | 0.2986 | 1250.6 |
| 318.15 | 0.3672 | 1243.6 |
| 318.15 | 0.4305 | 1237.3 |
| 318.15 | 0.4912 | 1231.5 |
| 318.15 | 0.5496 | 1226.0 |
| 318.15 | 0.6055 | 1220.8 |
| 318.15 | 0.6784 | 1214.4 |
| 318.15 | 0.7516 | 1207.9 |
| 318.15 | 0.8280 | 1201.2 |
| 318.15 | 0.8790 | 1196.9 |
| 318.15 | 0.9412 | 1191.8 |
| 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 (1) - Liquid | Speed of sound, m/s - Liquid |
| 288.15 | 0.0000 | 1412.3 |
| 288.15 | 0.0735 | 1406.8 |
| 288.15 | 0.1513 | 1400.3 |
| 288.15 | 0.2274 | 1393.5 |
| 288.15 | 0.2986 | 1386.7 |
| 288.15 | 0.3672 | 1379.7 |
| 288.15 | 0.4305 | 1373.5 |
| 288.15 | 0.4912 | 1367.5 |
| 288.15 | 0.5496 | 1361.9 |
| 288.15 | 0.6055 | 1356.8 |
| 288.15 | 0.6784 | 1350.4 |
| 288.15 | 0.7516 | 1344.0 |
| 288.15 | 0.8280 | 1337.4 |
| 288.15 | 0.8790 | 1333.2 |
| 288.15 | 0.9412 | 1328.2 |
| 288.15 | 1.0000 | 1323.1 |
| 298.15 | 0.0000 | 1369.8 |
| 298.15 | 0.0735 | 1363.6 |
| 298.15 | 0.1513 | 1356.6 |
| 298.15 | 0.2274 | 1349.5 |
| 298.15 | 0.2986 | 1342.4 |
| 298.15 | 0.3672 | 1335.3 |
| 298.15 | 0.4305 | 1328.9 |
| 298.15 | 0.4912 | 1322.9 |
| 298.15 | 0.5496 | 1317.3 |
| 298.15 | 0.6055 | 1312.0 |
| 298.15 | 0.6784 | 1305.4 |
| 298.15 | 0.7516 | 1298.8 |
| 298.15 | 0.8280 | 1292.1 |
| 298.15 | 0.8790 | 1287.7 |
| 298.15 | 0.9412 | 1282.6 |
| 298.15 | 1.0000 | 1277.6 |
| 308.15 | 0.0000 | 1325.2 |
| 308.15 | 0.0735 | 1318.5 |
| 308.15 | 0.1513 | 1311.2 |
| 308.15 | 0.2274 | 1303.9 |
| 308.15 | 0.2986 | 1296.7 |
| 308.15 | 0.3672 | 1289.6 |
| 308.15 | 0.4305 | 1283.1 |
| 308.15 | 0.4912 | 1277.0 |
| 308.15 | 0.5496 | 1271.4 |
| 308.15 | 0.6055 | 1266.1 |
| 308.15 | 0.6784 | 1259.4 |
| 308.15 | 0.7516 | 1252.8 |
| 308.15 | 0.8280 | 1246.0 |
| 308.15 | 0.8790 | 1241.6 |
| 308.15 | 0.9412 | 1236.4 |
| 308.15 | 1.0000 | 1231.5 |
| 318.15 | 0.0000 | 1279.0 |
| 318.15 | 0.0735 | 1272.2 |
| 318.15 | 0.1513 | 1264.9 |
| 318.15 | 0.2274 | 1257.7 |
| 318.15 | 0.2986 | 1250.6 |
| 318.15 | 0.3672 | 1243.6 |
| 318.15 | 0.4305 | 1237.3 |
| 318.15 | 0.4912 | 1231.5 |
| 318.15 | 0.5496 | 1226.0 |
| 318.15 | 0.6055 | 1220.8 |
| 318.15 | 0.6784 | 1214.4 |
| 318.15 | 0.7516 | 1207.9 |
| 318.15 | 0.8280 | 1201.2 |
| 318.15 | 0.8790 | 1196.9 |
| 318.15 | 0.9412 | 1191.8 |
| 318.15 | 1.0000 | 1187.2 |
Surface tension liquid-gas, N/m [ref]
Operational condition: Temperature, K = 298.15 (Liquid)
| Mole fraction of Tetrahydrofuran (1) - Liquid | Surface tension liquid-gas, N/m - Liquid |
|---|---|
| 0.0000 | 0.0281 |
| 0.0481 | 0.0279 |
| 0.2021 | 0.0277 |
| 0.3002 | 0.0276 |
| 0.4000 | 0.0274 |
| 0.5004 | 0.0273 |
| 0.6010 | 0.0272 |
| 0.7003 | 0.0272 |
| 0.7989 | 0.0271 |
| 0.9000 | 0.0271 |
| 1.0000 | 0.0270 |
Surface tension liquid-gas, N/m [ref]
Operational condition: Temperature, K = 298.15 (Liquid)
| Mole fraction of Tetrahydrofuran (1) - Liquid | Surface tension liquid-gas, N/m - Liquid |
|---|---|
| 0.0000 | 0.0281 |
| 0.0481 | 0.0279 |
| 0.2021 | 0.0277 |
| 0.3002 | 0.0276 |
| 0.4000 | 0.0274 |
| 0.5004 | 0.0273 |
| 0.6010 | 0.0272 |
| 0.7003 | 0.0272 |
| 0.7989 | 0.0271 |
| 0.9000 | 0.0271 |
| 1.0000 | 0.0270 |
Excess molar volume, m3/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Tetrahydrofuran (1) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.0481 | 0.0000 |
| 0.1006 | 0.0000 |
| 0.1509 | 0.0000 |
| 0.2021 | 0.0000 |
| 0.2495 | 0.0000 |
| 0.3002 | 1.1000e-08 |
| 0.3501 | 1.3000e-08 |
| 0.4000 | 1.5000e-08 |
| 0.4489 | 1.7000e-08 |
| 0.5004 | 1.8000e-08 |
| 0.5501 | 1.9000e-08 |
| 0.6010 | 2.0000e-08 |
| 0.6506 | 2.0000e-08 |
| 0.7003 | 1.9000e-08 |
| 0.7498 | 1.7000e-08 |
| 0.7989 | 1.5000e-08 |
| 0.8496 | 1.2000e-08 |
| 0.9000 | 0.0000 |
| 0.9491 | 0.0000 |
Excess molar volume, m3/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Tetrahydrofuran (1) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.0481 | 0.0000 |
| 0.1006 | 0.0000 |
| 0.1509 | 0.0000 |
| 0.2021 | 0.0000 |
| 0.2495 | 0.0000 |
| 0.3002 | 1.1000e-08 |
| 0.3501 | 1.3000e-08 |
| 0.4000 | 1.5000e-08 |
| 0.4489 | 1.7000e-08 |
| 0.5004 | 1.8000e-08 |
| 0.5501 | 1.9000e-08 |
| 0.6010 | 2.0000e-08 |
| 0.6506 | 2.0000e-08 |
| 0.7003 | 1.9000e-08 |
| 0.7498 | 1.7000e-08 |
| 0.7989 | 1.5000e-08 |
| 0.8496 | 1.2000e-08 |
| 0.9000 | 0.0000 |
| 0.9491 | 0.0000 |
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
- Excess Molar volumes and Surface Tensions of Trimethylbenzene with Tetrahydrofuran Tetrachloromethane and Dimethylsulfoxide at 298.15 K
- Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K