- InChI
- InChI=1S/C5H10O2/c6-4-5-2-1-3-7-5/h5-6H,1-4H2
- InChI Key
- BSYVTEYKTMYBMK-UHFFFAOYSA-N
- Formula
- C5H10O2
- SMILES
- OCC1CCCO1
- Molecular Weight1
- 102.13
- CAS
- 97-99-4
- Other Names
-
- 2-(hydroxymethyl)tetrahydrofuran
- 2-Hydroxymethyl-tetrahydrofuran
- 2-oxolanemethanol
- 2-tetrahydrofurylmethanol
- NSC 15434
- Oxolan-2-methanol
- QO THFA
- THFA
- Tetrahydro-2-furanmethanol
- Tetrahydro-2-furfuryl alcohol
- Tetrahydrofurfurylalkohol
- Tetrahydrofuryl carbinol
- Tetrahydrofurylalkohol
- Tetrahydrofurylmethanol
- furfuryl alcohol, tetrahydro-
- tetrahydro-2-furancarbinol
- tetrahydro-2-furanylmethanol
- tetrahydro-2-furylmethanol
- tetrahydrofurfuryl alcohol
- «alpha»-Tetrahydrofurfuryl alcohol
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfH°gas | -369.00 ± 6.30 | kJ/mol | NIST |
| ΔfH°liquid | -435.60 ± 5.90 | kJ/mol | NIST |
| ΔfusH° | 14.71 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [66.60; 67.00] | kJ/mol |
|
| ΔvapH° | 67.00 ± 2.00 | kJ/mol | NIST |
| ΔvapH° | 66.60 | kJ/mol | NIST |
| IE | 9.72 | eV | Relay (1.0) Calculated Property |
| logPoct/wat | 0.158 | Crippen Calculated Property | |
| McVol | 82.190 | ml/mol | McGowan Calculated Property |
| Inp | [853.00; 916.00] |
|
|
| Inp | 874.00 | NIST | |
| Inp | 916.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 878.00 | NIST | |
| I | [1494.00; 1501.00] |
|
|
| I | 1501.00 | NIST | |
| I | 1494.00 | NIST | |
| I | 1496.00 | NIST | |
| S°liquid | 219.20 | J/mol×K | NIST |
| Tboil | [451.00; 451.20] | K |
|
| Tboil | 451.20 | K | NIST |
| Tboil | 451.00 ± 3.00 | K | NIST |
| Tfus | 330.00 ± 3.00 | K | NIST |
Cheméo can also estimate Critical Temperature, Critical Pressure, Critical Volume, Standard Gibbs free energy of formation, Acentric Factor, Log10 of Water solubility in mol/l for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [177.30; 233.22] | J/mol×K | [448.41; 637.94] |
|
| Cp,gas | 177.30 | J/mol×K | 448.41 | Joback Calculated Property |
| Cp,gas | 187.88 | J/mol×K | 480.00 | Joback Calculated Property |
| Cp,gas | 197.94 | J/mol×K | 511.59 | Joback Calculated Property |
| Cp,gas | 207.48 | J/mol×K | 543.18 | Joback Calculated Property |
| Cp,gas | 216.53 | J/mol×K | 574.77 | Joback Calculated Property |
| Cp,gas | 225.10 | J/mol×K | 606.35 | Joback Calculated Property |
| Cp,gas | 233.22 | J/mol×K | 637.94 | Joback Calculated Property |
| Cp,liquid | 190.00 | J/mol×K | 298.15 | NIST |
| η | [0.0003212; 0.0436528] | Pa×s | [244.40; 448.41] |
|
| η | 0.0436528 | Pa×s | 244.40 | Joback Calculated Property |
| η | 0.0116780 | Pa×s | 278.40 | Joback Calculated Property |
| η | 0.0041627 | Pa×s | 312.40 | Joback Calculated Property |
| η | 0.0018169 | Pa×s | 346.40 | Joback Calculated Property |
| η | 0.0009197 | Pa×s | 380.41 | Joback Calculated Property |
| η | 0.0005206 | Pa×s | 414.41 | Joback Calculated Property |
| η | 0.0003212 | Pa×s | 448.41 | Joback Calculated Property |
| ΔvapH | [46.20; 46.50] | kJ/mol | [388.00; 423.00] |
|
| ΔvapH | 46.50 | kJ/mol | 388.00 | NIST |
| ΔvapH | 46.20 | kJ/mol | 423.00 | NIST |
| n0 | 1.45250 | 293.20 | Phase Equilibria for the Ternary Liquid Systems of (Water + Tetrahydrofurfuryl Alcohol + Cyclic Solvent) at 298.2 K | |
| ρl | 1050.75 | kg/m3 | 298.15 | Self-aggregation of liquids from biomass in aqueous solution |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 100.00 | 1062.84 |
| 288.15 | 100.00 | 1058.59 |
| 293.15 | 100.00 | 1054.34 |
| 298.15 | 100.00 | 1050.06 |
| 303.15 | 100.00 | 1045.78 |
| 308.15 | 100.00 | 1041.48 |
| 313.15 | 100.00 | 1037.17 |
| 318.15 | 100.00 | 1032.83 |
| 323.15 | 100.00 | 1028.47 |
| 328.15 | 100.00 | 1024.08 |
| 333.15 | 100.00 | 1019.68 |
| 338.15 | 100.00 | 1015.24 |
| 283.15 | 2500.00 | 1064.37 |
| 288.15 | 2500.00 | 1060.15 |
| 293.15 | 2500.00 | 1055.94 |
| 298.15 | 2500.00 | 1051.72 |
| 303.15 | 2500.00 | 1047.47 |
| 308.15 | 2500.00 | 1043.19 |
| 313.15 | 2500.00 | 1038.92 |
| 318.15 | 2500.00 | 1034.57 |
| 323.15 | 2500.00 | 1030.3 |
| 328.15 | 2500.00 | 1025.88 |
| 333.15 | 2500.00 | 1021.52 |
| 338.15 | 2500.00 | 1017.04 |
| 283.15 | 5000.00 | 1065.68 |
| 288.15 | 5000.00 | 1061.47 |
| 293.15 | 5000.00 | 1057.3 |
| 298.15 | 5000.00 | 1053.11 |
| 303.15 | 5000.00 | 1048.9 |
| 308.15 | 5000.00 | 1044.66 |
| 313.15 | 5000.00 | 1040.41 |
| 318.15 | 5000.00 | 1036.11 |
| 323.15 | 5000.00 | 1031.87 |
| 328.15 | 5000.00 | 1027.49 |
| 333.15 | 5000.00 | 1023.18 |
| 338.15 | 5000.00 | 1018.75 |
| 283.15 | 7500.00 | 1066.97 |
| 288.15 | 7500.00 | 1062.8 |
| 293.15 | 7500.00 | 1058.64 |
| 298.15 | 7500.00 | 1054.48 |
| 303.15 | 7500.00 | 1050.31 |
| 308.15 | 7500.00 | 1046.09 |
| 313.15 | 7500.00 | 1041.89 |
| 318.15 | 7500.00 | 1037.62 |
| 323.15 | 7500.00 | 1033.41 |
| 328.15 | 7500.00 | 1029.13 |
| 333.15 | 7500.00 | 1024.84 |
| 338.15 | 7500.00 | 1020.45 |
| 283.15 | 10000.00 | 1068.24 |
| 288.15 | 10000.00 | 1064.09 |
| 293.15 | 10000.00 | 1060.0 |
| 298.15 | 10000.00 | 1055.84 |
| 303.15 | 10000.00 | 1051.69 |
| 308.15 | 10000.00 | 1047.48 |
| 313.15 | 10000.00 | 1043.41 |
| 318.15 | 10000.00 | 1039.11 |
| 323.15 | 10000.00 | 1034.93 |
| 328.15 | 10000.00 | 1030.63 |
| 333.15 | 10000.00 | 1026.39 |
| 338.15 | 10000.00 | 1022.06 |
| 283.15 | 20000.00 | 1073.16 |
| 288.15 | 20000.00 | 1069.11 |
| 293.15 | 20000.00 | 1065.1 |
| 298.15 | 20000.00 | 1061.08 |
| 303.15 | 20000.00 | 1057.06 |
| 308.15 | 20000.00 | 1052.96 |
| 313.15 | 20000.00 | 1048.93 |
| 318.15 | 20000.00 | 1044.81 |
| 323.15 | 20000.00 | 1040.79 |
| 328.15 | 20000.00 | 1036.6 |
| 333.15 | 20000.00 | 1032.49 |
| 338.15 | 20000.00 | 1028.31 |
| 283.15 | 30000.00 | 1077.84 |
| 288.15 | 30000.00 | 1073.88 |
| 293.15 | 30000.00 | 1069.97 |
| 298.15 | 30000.00 | 1066.04 |
| 303.15 | 30000.00 | 1062.11 |
| 308.15 | 30000.00 | 1058.12 |
| 313.15 | 30000.00 | 1054.21 |
| 318.15 | 30000.00 | 1050.15 |
| 323.15 | 30000.00 | 1046.28 |
| 328.15 | 30000.00 | 1042.2 |
| 333.15 | 30000.00 | 1038.22 |
| 338.15 | 30000.00 | 1034.16 |
| 283.15 | 40000.00 | 1082.28 |
| 288.15 | 40000.00 | 1078.41 |
| 293.15 | 40000.00 | 1074.62 |
| 298.15 | 40000.00 | 1070.75 |
| 303.15 | 40000.00 | 1066.94 |
| 308.15 | 40000.00 | 1063.05 |
| 313.15 | 40000.00 | 1059.19 |
| 318.15 | 40000.00 | 1055.24 |
| 323.15 | 40000.00 | 1051.44 |
| 328.15 | 40000.00 | 1047.5 |
| 333.15 | 40000.00 | 1043.64 |
| 338.15 | 40000.00 | 1039.68 |
| 283.15 | 50000.00 | 1086.55 |
| 288.15 | 50000.00 | 1082.72 |
| 293.15 | 50000.00 | 1078.97 |
| 298.15 | 50000.00 | 1075.22 |
| 303.15 | 50000.00 | 1071.49 |
| 308.15 | 50000.00 | 1067.61 |
| 313.15 | 50000.00 | 1063.91 |
| 318.15 | 50000.00 | 1060.12 |
| 323.15 | 50000.00 | 1056.41 |
| 328.15 | 50000.00 | 1052.52 |
| 333.15 | 50000.00 | 1048.73 |
| 338.15 | 50000.00 | 1044.89 |
| 283.15 | 60000.00 | 1090.57 |
| 288.15 | 60000.00 | 1086.83 |
| 293.15 | 60000.00 | 1083.18 |
| 298.15 | 60000.00 | 1079.49 |
| 303.15 | 60000.00 | 1075.79 |
| 308.15 | 60000.00 | 1072.09 |
| 313.15 | 60000.00 | 1068.44 |
| 318.15 | 60000.00 | 1064.68 |
| 323.15 | 60000.00 | 1061.07 |
| 328.15 | 60000.00 | 1057.3 |
| 333.15 | 60000.00 | 1053.6 |
| 338.15 | 60000.00 | 1049.83 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [335.84; 477.57] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.79248e+01 | |||
| Coefficient B | -6.27566e+03 | |||
| Coefficient C | 1.99750e+01 | |||
| Temperature range, min. | 335.84 | |||
| Temperature range, max. | 477.57 | |||
| Pvap | 1.33 | kPa | 335.84 | Calculated Property |
| Pvap | 2.81 | kPa | 351.59 | Calculated Property |
| Pvap | 5.59 | kPa | 367.34 | Calculated Property |
| Pvap | 10.53 | kPa | 383.08 | Calculated Property |
| Pvap | 18.92 | kPa | 398.83 | Calculated Property |
| Pvap | 32.56 | kPa | 414.58 | Calculated Property |
| Pvap | 53.96 | kPa | 430.33 | Calculated Property |
| Pvap | 86.41 | kPa | 446.07 | Calculated Property |
| Pvap | 134.19 | kPa | 461.82 | Calculated Property |
| Pvap | 202.66 | kPa | 477.57 | Calculated Property |
| Pvap | [3.63e-07; 4314.07] | kPa | [193.00; 639.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.92241e+01 | |||
| Coefficient B | -9.24652e+03 | |||
| Coefficient C | -1.07177e+01 | |||
| Coefficient D | 6.98190e-06 | |||
| Temperature range, min. | 193.00 | |||
| Temperature range, max. | 639.00 | |||
| Pvap | 3.63e-07 | kPa | 193.00 | Calculated Property |
| Pvap | 6.49e-04 | kPa | 242.56 | Calculated Property |
| Pvap | 0.07 | kPa | 292.11 | Calculated Property |
| Pvap | 1.57 | kPa | 341.67 | Calculated Property |
| Pvap | 14.60 | kPa | 391.22 | Calculated Property |
| Pvap | 77.32 | kPa | 440.78 | Calculated Property |
| Pvap | 283.82 | kPa | 490.33 | Calculated Property |
| Pvap | 815.52 | kPa | 539.89 | Calculated Property |
| Pvap | 1984.73 | kPa | 589.44 | Calculated Property |
| Pvap | 4314.07 | kPa | 639.00 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Furanmethanol, tetrahydro-.
Mixtures
- 2-Furanmethanol, tetrahydro- + 1-Hexanol + Water
- 2-Furanmethanol, tetrahydro- + Water
- 2-Furanmethanol, tetrahydro- + Cyclohexane + Water
- Cyclohexanol + 2-Furanmethanol, tetrahydro- + Water
- 2-Furanmethanol, tetrahydro- + Acetic acid, cyclohexyl ester + Water
- 2-Furanmethanol, tetrahydro- + Benzene, chloro- + Water
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Cheméo Relay (1.0, beta) Beta: served but experimental, data-limited and below our cross-validation release bar; the Joback value is recommended where available.
- Crippen Method
- Crippen Method
- Phase equilibria for ternary liquid systems of (water + carboxylic acid or alcohol + 1-hexanol) at T = 293.15 K: modelling considerations
- Self-aggregation of liquids from biomass in aqueous solution
- Phase Equilibria for the Ternary Liquid Systems of (Water + Tetrahydrofurfuryl Alcohol + Cyclic Solvent) at 298.2 K
- Thermophysical Properties of Furfural Compounds
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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