- Name
- p-Xylene
- InChI
- InChI=1S/C8H10/c1-7-3-5-8(2)6-4-7/h3-6H,1-2H3
- InChI Key
- URLKBWYHVLBVBO-UHFFFAOYSA-N
- Formula
- C8H10
- SMILES
- Cc1ccc(C)cc1
- Mol. Weight (g/mol)
- 106.17
- CAS
- 106-42-3
- 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)
- Vapor Liquid Equilibrium at Constant Pressure
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 | 0.0840 | 0.0007 |
| 288.15 | 0.1716 | 0.0007 |
| 288.15 | 0.2322 | 0.0007 |
| 288.15 | 0.2934 | 0.0007 |
| 288.15 | 0.3548 | 0.0007 |
| 288.15 | 0.4284 | 0.0006 |
| 288.15 | 0.4896 | 0.0006 |
| 288.15 | 0.5518 | 0.0006 |
| 288.15 | 0.6201 | 0.0006 |
| 288.15 | 0.6825 | 0.0006 |
| 288.15 | 0.7414 | 0.0006 |
| 288.15 | 0.8102 | 0.0006 |
| 288.15 | 0.8756 | 0.0005 |
| 288.15 | 0.9409 | 0.0005 |
| 288.15 | 1.0000 | 0.0005 |
| 298.15 | 0.0000 | 0.0006 |
| 298.15 | 0.0840 | 0.0006 |
| 298.15 | 0.1716 | 0.0006 |
| 298.15 | 0.2322 | 0.0006 |
| 298.15 | 0.2934 | 0.0006 |
| 298.15 | 0.3548 | 0.0006 |
| 298.15 | 0.4284 | 0.0006 |
| 298.15 | 0.4896 | 0.0006 |
| 298.15 | 0.5518 | 0.0005 |
| 298.15 | 0.6201 | 0.0005 |
| 298.15 | 0.6825 | 0.0005 |
| 298.15 | 0.7414 | 0.0005 |
| 298.15 | 0.8102 | 0.0005 |
| 298.15 | 0.8756 | 0.0005 |
| 298.15 | 0.9409 | 0.0005 |
| 298.15 | 1.0000 | 0.0005 |
| 308.15 | 0.0000 | 0.0006 |
| 308.15 | 0.0840 | 0.0005 |
| 308.15 | 0.1716 | 0.0005 |
| 308.15 | 0.2322 | 0.0005 |
| 308.15 | 0.2934 | 0.0005 |
| 308.15 | 0.3548 | 0.0005 |
| 308.15 | 0.4284 | 0.0005 |
| 308.15 | 0.4896 | 0.0005 |
| 308.15 | 0.5518 | 0.0005 |
| 308.15 | 0.6201 | 0.0005 |
| 308.15 | 0.6825 | 0.0005 |
| 308.15 | 0.7414 | 0.0005 |
| 308.15 | 0.8102 | 0.0005 |
| 308.15 | 0.8756 | 0.0004 |
| 308.15 | 0.9409 | 0.0004 |
| 308.15 | 1.0000 | 0.0004 |
| 318.15 | 0.0000 | 0.0005 |
| 318.15 | 0.0840 | 0.0005 |
| 318.15 | 0.1716 | 0.0005 |
| 318.15 | 0.2322 | 0.0005 |
| 318.15 | 0.2934 | 0.0005 |
| 318.15 | 0.3548 | 0.0005 |
| 318.15 | 0.4284 | 0.0005 |
| 318.15 | 0.4896 | 0.0005 |
| 318.15 | 0.5518 | 0.0005 |
| 318.15 | 0.6201 | 0.0004 |
| 318.15 | 0.6825 | 0.0004 |
| 318.15 | 0.7414 | 0.0004 |
| 318.15 | 0.8102 | 0.0004 |
| 318.15 | 0.8756 | 0.0004 |
| 318.15 | 0.9409 | 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 | 0.0840 | 0.0007 |
| 288.15 | 0.1716 | 0.0007 |
| 288.15 | 0.2322 | 0.0007 |
| 288.15 | 0.2934 | 0.0007 |
| 288.15 | 0.3548 | 0.0007 |
| 288.15 | 0.4284 | 0.0006 |
| 288.15 | 0.4896 | 0.0006 |
| 288.15 | 0.5518 | 0.0006 |
| 288.15 | 0.6201 | 0.0006 |
| 288.15 | 0.6825 | 0.0006 |
| 288.15 | 0.7414 | 0.0006 |
| 288.15 | 0.8102 | 0.0006 |
| 288.15 | 0.8756 | 0.0005 |
| 288.15 | 0.9409 | 0.0005 |
| 288.15 | 1.0000 | 0.0005 |
| 298.15 | 0.0000 | 0.0006 |
| 298.15 | 0.0840 | 0.0006 |
| 298.15 | 0.1716 | 0.0006 |
| 298.15 | 0.2322 | 0.0006 |
| 298.15 | 0.2934 | 0.0006 |
| 298.15 | 0.3548 | 0.0006 |
| 298.15 | 0.4284 | 0.0006 |
| 298.15 | 0.4896 | 0.0006 |
| 298.15 | 0.5518 | 0.0005 |
| 298.15 | 0.6201 | 0.0005 |
| 298.15 | 0.6825 | 0.0005 |
| 298.15 | 0.7414 | 0.0005 |
| 298.15 | 0.8102 | 0.0005 |
| 298.15 | 0.8756 | 0.0005 |
| 298.15 | 0.9409 | 0.0005 |
| 298.15 | 1.0000 | 0.0005 |
| 308.15 | 0.0000 | 0.0006 |
| 308.15 | 0.0840 | 0.0005 |
| 308.15 | 0.1716 | 0.0005 |
| 308.15 | 0.2322 | 0.0005 |
| 308.15 | 0.2934 | 0.0005 |
| 308.15 | 0.3548 | 0.0005 |
| 308.15 | 0.4284 | 0.0005 |
| 308.15 | 0.4896 | 0.0005 |
| 308.15 | 0.5518 | 0.0005 |
| 308.15 | 0.6201 | 0.0005 |
| 308.15 | 0.6825 | 0.0005 |
| 308.15 | 0.7414 | 0.0005 |
| 308.15 | 0.8102 | 0.0005 |
| 308.15 | 0.8756 | 0.0004 |
| 308.15 | 0.9409 | 0.0004 |
| 308.15 | 1.0000 | 0.0004 |
| 318.15 | 0.0000 | 0.0005 |
| 318.15 | 0.0840 | 0.0005 |
| 318.15 | 0.1716 | 0.0005 |
| 318.15 | 0.2322 | 0.0005 |
| 318.15 | 0.2934 | 0.0005 |
| 318.15 | 0.3548 | 0.0005 |
| 318.15 | 0.4284 | 0.0005 |
| 318.15 | 0.4896 | 0.0005 |
| 318.15 | 0.5518 | 0.0005 |
| 318.15 | 0.6201 | 0.0004 |
| 318.15 | 0.6825 | 0.0004 |
| 318.15 | 0.7414 | 0.0004 |
| 318.15 | 0.8102 | 0.0004 |
| 318.15 | 0.8756 | 0.0004 |
| 318.15 | 0.9409 | 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 | 1.4985 |
| 288.15 | 0.0840 | 1.4936 |
| 288.15 | 0.1716 | 1.4881 |
| 288.15 | 0.2322 | 1.4842 |
| 288.15 | 0.2934 | 1.48 |
| 288.15 | 0.3548 | 1.4755 |
| 288.15 | 0.4284 | 1.4698 |
| 288.15 | 0.4896 | 1.4648 |
| 288.15 | 0.5518 | 1.4594 |
| 288.15 | 0.6201 | 1.4531 |
| 288.15 | 0.6825 | 1.447 |
| 288.15 | 0.7414 | 1.4409 |
| 288.15 | 0.8102 | 1.4333 |
| 288.15 | 0.8756 | 1.4256 |
| 288.15 | 0.9409 | 1.4174 |
| 288.15 | 1.0000 | 1.4094 |
| 293.15 | 0.0000 | 1.4959 |
| 293.15 | 0.0840 | 1.491 |
| 293.15 | 0.1716 | 1.4855 |
| 293.15 | 0.2322 | 1.4816 |
| 293.15 | 0.2934 | 1.4774 |
| 293.15 | 0.3548 | 1.4729 |
| 293.15 | 0.4284 | 1.4672 |
| 293.15 | 0.4896 | 1.4622 |
| 293.15 | 0.5518 | 1.4568 |
| 293.15 | 0.6201 | 1.4505 |
| 293.15 | 0.6825 | 1.4444 |
| 293.15 | 0.7414 | 1.4383 |
| 293.15 | 0.8102 | 1.4308 |
| 293.15 | 0.8756 | 1.4231 |
| 293.15 | 0.9409 | 1.4149 |
| 293.15 | 1.0000 | 1.407 |
| 298.15 | 0.0000 | 1.4933 |
| 298.15 | 0.0840 | 1.4884 |
| 298.15 | 0.1716 | 1.4829 |
| 298.15 | 0.2322 | 1.479 |
| 298.15 | 0.2934 | 1.4748 |
| 298.15 | 0.3548 | 1.4703 |
| 298.15 | 0.4284 | 1.4646 |
| 298.15 | 0.4896 | 1.4596 |
| 298.15 | 0.5518 | 1.4542 |
| 298.15 | 0.6201 | 1.448 |
| 298.15 | 0.6825 | 1.4419 |
| 298.15 | 0.7414 | 1.4358 |
| 298.15 | 0.8102 | 1.4282 |
| 298.15 | 0.8756 | 1.4206 |
| 298.15 | 0.9409 | 1.4125 |
| 298.15 | 1.0000 | 1.4046 |
| 303.15 | 0.0000 | 1.4907 |
| 303.15 | 0.0840 | 1.4858 |
| 303.15 | 0.1716 | 1.4803 |
| 303.15 | 0.2322 | 1.4764 |
| 303.15 | 0.2934 | 1.4722 |
| 303.15 | 0.3548 | 1.4677 |
| 303.15 | 0.4284 | 1.4621 |
| 303.15 | 0.4896 | 1.4571 |
| 303.15 | 0.5518 | 1.4517 |
| 303.15 | 0.6201 | 1.4454 |
| 303.15 | 0.6825 | 1.4394 |
| 303.15 | 0.7414 | 1.4333 |
| 303.15 | 0.8102 | 1.4258 |
| 303.15 | 0.8756 | 1.4182 |
| 303.15 | 0.9409 | 1.4101 |
| 303.15 | 1.0000 | 1.4023 |
| 308.15 | 0.0000 | 1.4881 |
| 308.15 | 0.0840 | 1.4832 |
| 308.15 | 0.1716 | 1.4777 |
| 308.15 | 0.2322 | 1.4738 |
| 308.15 | 0.2934 | 1.4696 |
| 308.15 | 0.3548 | 1.4651 |
| 308.15 | 0.4284 | 1.4595 |
| 308.15 | 0.4896 | 1.4545 |
| 308.15 | 0.5518 | 1.4491 |
| 308.15 | 0.6201 | 1.4429 |
| 308.15 | 0.6825 | 1.4368 |
| 308.15 | 0.7414 | 1.4308 |
| 308.15 | 0.8102 | 1.4233 |
| 308.15 | 0.8756 | 1.4157 |
| 308.15 | 0.9409 | 1.4077 |
| 308.15 | 1.0000 | 1.3999 |
| 313.15 | 0.0000 | 1.4855 |
| 313.15 | 0.0840 | 1.4806 |
| 313.15 | 0.1716 | 1.4751 |
| 313.15 | 0.2322 | 1.4712 |
| 313.15 | 0.2934 | 1.467 |
| 313.15 | 0.3548 | 1.4625 |
| 313.15 | 0.4284 | 1.4569 |
| 313.15 | 0.4896 | 1.4519 |
| 313.15 | 0.5518 | 1.4465 |
| 313.15 | 0.6201 | 1.4403 |
| 313.15 | 0.6825 | 1.4342 |
| 313.15 | 0.7414 | 1.4282 |
| 313.15 | 0.8102 | 1.4207 |
| 313.15 | 0.8756 | 1.4132 |
| 313.15 | 0.9409 | 1.4052 |
| 313.15 | 1.0000 | 1.3975 |
| 318.15 | 0.0000 | 1.483 |
| 318.15 | 0.0840 | 1.478 |
| 318.15 | 0.1716 | 1.4726 |
| 318.15 | 0.2322 | 1.4686 |
| 318.15 | 0.2934 | 1.4644 |
| 318.15 | 0.3548 | 1.46 |
| 318.15 | 0.4284 | 1.4544 |
| 318.15 | 0.4896 | 1.4494 |
| 318.15 | 0.5518 | 1.4441 |
| 318.15 | 0.6201 | 1.4378 |
| 318.15 | 0.6825 | 1.4318 |
| 318.15 | 0.7414 | 1.4258 |
| 318.15 | 0.8102 | 1.4183 |
| 318.15 | 0.8756 | 1.4108 |
| 318.15 | 0.9409 | 1.4028 |
| 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 | 1.4985 |
| 288.15 | 0.0840 | 1.4936 |
| 288.15 | 0.1716 | 1.4881 |
| 288.15 | 0.2322 | 1.4842 |
| 288.15 | 0.2934 | 1.48 |
| 288.15 | 0.3548 | 1.4755 |
| 288.15 | 0.4284 | 1.4698 |
| 288.15 | 0.4896 | 1.4648 |
| 288.15 | 0.5518 | 1.4594 |
| 288.15 | 0.6201 | 1.4531 |
| 288.15 | 0.6825 | 1.447 |
| 288.15 | 0.7414 | 1.4409 |
| 288.15 | 0.8102 | 1.4333 |
| 288.15 | 0.8756 | 1.4256 |
| 288.15 | 0.9409 | 1.4174 |
| 288.15 | 1.0000 | 1.4094 |
| 293.15 | 0.0000 | 1.4959 |
| 293.15 | 0.0840 | 1.491 |
| 293.15 | 0.1716 | 1.4855 |
| 293.15 | 0.2322 | 1.4816 |
| 293.15 | 0.2934 | 1.4774 |
| 293.15 | 0.3548 | 1.4729 |
| 293.15 | 0.4284 | 1.4672 |
| 293.15 | 0.4896 | 1.4622 |
| 293.15 | 0.5518 | 1.4568 |
| 293.15 | 0.6201 | 1.4505 |
| 293.15 | 0.6825 | 1.4444 |
| 293.15 | 0.7414 | 1.4383 |
| 293.15 | 0.8102 | 1.4308 |
| 293.15 | 0.8756 | 1.4231 |
| 293.15 | 0.9409 | 1.4149 |
| 293.15 | 1.0000 | 1.407 |
| 298.15 | 0.0000 | 1.4933 |
| 298.15 | 0.0840 | 1.4884 |
| 298.15 | 0.1716 | 1.4829 |
| 298.15 | 0.2322 | 1.479 |
| 298.15 | 0.2934 | 1.4748 |
| 298.15 | 0.3548 | 1.4703 |
| 298.15 | 0.4284 | 1.4646 |
| 298.15 | 0.4896 | 1.4596 |
| 298.15 | 0.5518 | 1.4542 |
| 298.15 | 0.6201 | 1.448 |
| 298.15 | 0.6825 | 1.4419 |
| 298.15 | 0.7414 | 1.4358 |
| 298.15 | 0.8102 | 1.4282 |
| 298.15 | 0.8756 | 1.4206 |
| 298.15 | 0.9409 | 1.4125 |
| 298.15 | 1.0000 | 1.4046 |
| 303.15 | 0.0000 | 1.4907 |
| 303.15 | 0.0840 | 1.4858 |
| 303.15 | 0.1716 | 1.4803 |
| 303.15 | 0.2322 | 1.4764 |
| 303.15 | 0.2934 | 1.4722 |
| 303.15 | 0.3548 | 1.4677 |
| 303.15 | 0.4284 | 1.4621 |
| 303.15 | 0.4896 | 1.4571 |
| 303.15 | 0.5518 | 1.4517 |
| 303.15 | 0.6201 | 1.4454 |
| 303.15 | 0.6825 | 1.4394 |
| 303.15 | 0.7414 | 1.4333 |
| 303.15 | 0.8102 | 1.4258 |
| 303.15 | 0.8756 | 1.4182 |
| 303.15 | 0.9409 | 1.4101 |
| 303.15 | 1.0000 | 1.4023 |
| 308.15 | 0.0000 | 1.4881 |
| 308.15 | 0.0840 | 1.4832 |
| 308.15 | 0.1716 | 1.4777 |
| 308.15 | 0.2322 | 1.4738 |
| 308.15 | 0.2934 | 1.4696 |
| 308.15 | 0.3548 | 1.4651 |
| 308.15 | 0.4284 | 1.4595 |
| 308.15 | 0.4896 | 1.4545 |
| 308.15 | 0.5518 | 1.4491 |
| 308.15 | 0.6201 | 1.4429 |
| 308.15 | 0.6825 | 1.4368 |
| 308.15 | 0.7414 | 1.4308 |
| 308.15 | 0.8102 | 1.4233 |
| 308.15 | 0.8756 | 1.4157 |
| 308.15 | 0.9409 | 1.4077 |
| 308.15 | 1.0000 | 1.3999 |
| 313.15 | 0.0000 | 1.4855 |
| 313.15 | 0.0840 | 1.4806 |
| 313.15 | 0.1716 | 1.4751 |
| 313.15 | 0.2322 | 1.4712 |
| 313.15 | 0.2934 | 1.467 |
| 313.15 | 0.3548 | 1.4625 |
| 313.15 | 0.4284 | 1.4569 |
| 313.15 | 0.4896 | 1.4519 |
| 313.15 | 0.5518 | 1.4465 |
| 313.15 | 0.6201 | 1.4403 |
| 313.15 | 0.6825 | 1.4342 |
| 313.15 | 0.7414 | 1.4282 |
| 313.15 | 0.8102 | 1.4207 |
| 313.15 | 0.8756 | 1.4132 |
| 313.15 | 0.9409 | 1.4052 |
| 313.15 | 1.0000 | 1.3975 |
| 318.15 | 0.0000 | 1.483 |
| 318.15 | 0.0840 | 1.478 |
| 318.15 | 0.1716 | 1.4726 |
| 318.15 | 0.2322 | 1.4686 |
| 318.15 | 0.2934 | 1.4644 |
| 318.15 | 0.3548 | 1.46 |
| 318.15 | 0.4284 | 1.4544 |
| 318.15 | 0.4896 | 1.4494 |
| 318.15 | 0.5518 | 1.4441 |
| 318.15 | 0.6201 | 1.4378 |
| 318.15 | 0.6825 | 1.4318 |
| 318.15 | 0.7414 | 1.4258 |
| 318.15 | 0.8102 | 1.4183 |
| 318.15 | 0.8756 | 1.4108 |
| 318.15 | 0.9409 | 1.4028 |
| 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 | 1357.5 |
| 288.15 | 0.0840 | 1356.0 |
| 288.15 | 0.1716 | 1354.2 |
| 288.15 | 0.2322 | 1353.1 |
| 288.15 | 0.2934 | 1351.7 |
| 288.15 | 0.3548 | 1350.2 |
| 288.15 | 0.4284 | 1348.1 |
| 288.15 | 0.4896 | 1346.2 |
| 288.15 | 0.5518 | 1344.1 |
| 288.15 | 0.6201 | 1341.5 |
| 288.15 | 0.6825 | 1338.9 |
| 288.15 | 0.7414 | 1336.3 |
| 288.15 | 0.8102 | 1333.1 |
| 288.15 | 0.8756 | 1329.8 |
| 288.15 | 0.9409 | 1326.4 |
| 288.15 | 1.0000 | 1323.1 |
| 298.15 | 0.0000 | 1316.4 |
| 298.15 | 0.0840 | 1314.1 |
| 298.15 | 0.1716 | 1311.7 |
| 298.15 | 0.2322 | 1310.1 |
| 298.15 | 0.2934 | 1308.3 |
| 298.15 | 0.3548 | 1306.5 |
| 298.15 | 0.4284 | 1304.0 |
| 298.15 | 0.4896 | 1301.8 |
| 298.15 | 0.5518 | 1299.4 |
| 298.15 | 0.6201 | 1296.6 |
| 298.15 | 0.6825 | 1293.7 |
| 298.15 | 0.7414 | 1290.9 |
| 298.15 | 0.8102 | 1287.6 |
| 298.15 | 0.8756 | 1284.3 |
| 298.15 | 0.9409 | 1280.8 |
| 298.15 | 1.0000 | 1277.6 |
| 308.15 | 0.0000 | 1268.0 |
| 308.15 | 0.0840 | 1265.7 |
| 308.15 | 0.1716 | 1263.2 |
| 308.15 | 0.2322 | 1261.6 |
| 308.15 | 0.2934 | 1259.9 |
| 308.15 | 0.3548 | 1258.1 |
| 308.15 | 0.4284 | 1255.7 |
| 308.15 | 0.4896 | 1253.7 |
| 308.15 | 0.5518 | 1251.5 |
| 308.15 | 0.6201 | 1248.8 |
| 308.15 | 0.6825 | 1246.2 |
| 308.15 | 0.7414 | 1243.6 |
| 308.15 | 0.8102 | 1240.6 |
| 308.15 | 0.8756 | 1237.5 |
| 308.15 | 0.9409 | 1234.4 |
| 308.15 | 1.0000 | 1231.5 |
| 318.15 | 0.0000 | 1230.3 |
| 318.15 | 0.0840 | 1227.2 |
| 318.15 | 0.1716 | 1224.0 |
| 318.15 | 0.2322 | 1221.9 |
| 318.15 | 0.2934 | 1219.6 |
| 318.15 | 0.3548 | 1217.3 |
| 318.15 | 0.4284 | 1214.5 |
| 318.15 | 0.4896 | 1212.0 |
| 318.15 | 0.5518 | 1209.3 |
| 318.15 | 0.6201 | 1206.2 |
| 318.15 | 0.6825 | 1203.3 |
| 318.15 | 0.7414 | 1200.4 |
| 318.15 | 0.8102 | 1197.0 |
| 318.15 | 0.8756 | 1193.7 |
| 318.15 | 0.9409 | 1190.4 |
| 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 | 1357.5 |
| 288.15 | 0.0840 | 1356.0 |
| 288.15 | 0.1716 | 1354.2 |
| 288.15 | 0.2322 | 1353.1 |
| 288.15 | 0.2934 | 1351.7 |
| 288.15 | 0.3548 | 1350.2 |
| 288.15 | 0.4284 | 1348.1 |
| 288.15 | 0.4896 | 1346.2 |
| 288.15 | 0.5518 | 1344.1 |
| 288.15 | 0.6201 | 1341.5 |
| 288.15 | 0.6825 | 1338.9 |
| 288.15 | 0.7414 | 1336.3 |
| 288.15 | 0.8102 | 1333.1 |
| 288.15 | 0.8756 | 1329.8 |
| 288.15 | 0.9409 | 1326.4 |
| 288.15 | 1.0000 | 1323.1 |
| 298.15 | 0.0000 | 1316.4 |
| 298.15 | 0.0840 | 1314.1 |
| 298.15 | 0.1716 | 1311.7 |
| 298.15 | 0.2322 | 1310.1 |
| 298.15 | 0.2934 | 1308.3 |
| 298.15 | 0.3548 | 1306.5 |
| 298.15 | 0.4284 | 1304.0 |
| 298.15 | 0.4896 | 1301.8 |
| 298.15 | 0.5518 | 1299.4 |
| 298.15 | 0.6201 | 1296.6 |
| 298.15 | 0.6825 | 1293.7 |
| 298.15 | 0.7414 | 1290.9 |
| 298.15 | 0.8102 | 1287.6 |
| 298.15 | 0.8756 | 1284.3 |
| 298.15 | 0.9409 | 1280.8 |
| 298.15 | 1.0000 | 1277.6 |
| 308.15 | 0.0000 | 1268.0 |
| 308.15 | 0.0840 | 1265.7 |
| 308.15 | 0.1716 | 1263.2 |
| 308.15 | 0.2322 | 1261.6 |
| 308.15 | 0.2934 | 1259.9 |
| 308.15 | 0.3548 | 1258.1 |
| 308.15 | 0.4284 | 1255.7 |
| 308.15 | 0.4896 | 1253.7 |
| 308.15 | 0.5518 | 1251.5 |
| 308.15 | 0.6201 | 1248.8 |
| 308.15 | 0.6825 | 1246.2 |
| 308.15 | 0.7414 | 1243.6 |
| 308.15 | 0.8102 | 1240.6 |
| 308.15 | 0.8756 | 1237.5 |
| 308.15 | 0.9409 | 1234.4 |
| 308.15 | 1.0000 | 1231.5 |
| 318.15 | 0.0000 | 1230.3 |
| 318.15 | 0.0840 | 1227.2 |
| 318.15 | 0.1716 | 1224.0 |
| 318.15 | 0.2322 | 1221.9 |
| 318.15 | 0.2934 | 1219.6 |
| 318.15 | 0.3548 | 1217.3 |
| 318.15 | 0.4284 | 1214.5 |
| 318.15 | 0.4896 | 1212.0 |
| 318.15 | 0.5518 | 1209.3 |
| 318.15 | 0.6201 | 1206.2 |
| 318.15 | 0.6825 | 1203.3 |
| 318.15 | 0.7414 | 1200.4 |
| 318.15 | 0.8102 | 1197.0 |
| 318.15 | 0.8756 | 1193.7 |
| 318.15 | 0.9409 | 1190.4 |
| 318.15 | 1.0000 | 1187.2 |
Vapor Liquid Equilibrium at Constant Pressure [ref]
Operational condition: Pressure, kPa = 95.8 (VLE)
| T [K] - VLE | x1[mol/mol] of Tetrahydrofuran (2) - Liquid |
|---|---|
| 409.35 | 0.0000 |
| 385.15 | 0.1855 |
| 373.05 | 0.3130 |
| 362.65 | 0.4511 |
| 351.75 | 0.6279 |
| 345.35 | 0.7523 |
| 338.55 | 0.9101 |
| 335.55 | 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