- InChI
- InChI=1S/C5H6O2/c6-4-5-2-1-3-7-5/h1-3,6H,4H2
- InChI Key
- XPFVYQJUAUNWIW-UHFFFAOYSA-N
- Formula
- C5H6O2
- SMILES
- OCc1ccco1
- Molecular Weight1
- 98.10
- CAS
- 98-00-0
- Other Names
-
- 2-(Hydroxymethyl)furan
- 2-FURYLMETHANOL
- 2-Furancarbinol
- 2-Furane-methanol (furfurol)
- 2-Furanemethanol
- 2-Furanmethanol (furfuryl alcohol)
- 2-Furanylmethanol
- 2-Furfuryl alcohol
- 2-Furfurylalkohol
- 2-Furylcarbinol
- 2-Hydroxymethylfurane
- 2-hydroxymethylfuran
- 5-Hydroxymethylfuran
- ALPHA-FURFURYL ALCOHOL
- FURYL ALCOHOL
- Furan-2-methanol
- Furfural alcohol
- Furfuralcohol
- Furfuranol
- Furfurol
- Furfuryl alcohol
- Furylcarbinol
- Methanol, (2-furyl)-
- NCI-C56224
- NSC 8843
- Qo furfuryl alcohol
- UN 2874
- furanmethanol
- furfuryl alcohol (furfurol)
- «alpha»-Furfuryl alcohol
- «alpha»-Furylcarbinol
- «alpha»-Furfuryl alcohol
- «alpha»-Furylcarbinol
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- 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 a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- NFPA Safety : NFPA Safety Rating.
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- Ttriple : Triple Point Temperature (K).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | [-2548.70; -2540.00] | kJ/mol |
|
| ΔcH°liquid | -2548.70 | kJ/mol | NIST |
| ΔcH°liquid | -2548.00 | kJ/mol | NIST |
| ΔcH°liquid | -2540.00 | kJ/mol | NIST |
| ΔfH°gas | [-212.60; -211.80] | kJ/mol |
|
| ΔfH°gas | -212.00 | kJ/mol | NIST |
| ΔfH°gas | -212.60 | kJ/mol | NIST |
| ΔfH°gas | -211.80 ± 2.10 | kJ/mol | NIST |
| ΔfH°liquid | [-277.00; -276.20] | kJ/mol |
|
| ΔfH°liquid | -276.40 | kJ/mol | NIST |
| ΔfH°liquid | -277.00 | kJ/mol | NIST |
| ΔfH°liquid | -276.20 ± 1.30 | kJ/mol | NIST |
| ΔvapH° | [64.40; 64.40] | kJ/mol |
|
| ΔvapH° | 64.40 ± 1.70 | kJ/mol | NIST |
| ΔvapH° | 64.40 | kJ/mol | NIST |
| log10WS | -5.35 | Crippen Calculated Property | |
| logPoct/wat | 0.772 | Crippen Calculated Property | |
| McVol | 73.590 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 1 | KDB | |
| NFPA Safety | 1 | KDB | |
| Inp | [127.02; 891.00] |
|
|
| Inp | 840.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 819.00 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 826.10 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 813.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 819.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 833.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | 891.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 823.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 861.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 865.90 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 842.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 823.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 825.00 | NIST | |
| Inp | 825.00 | NIST | |
| Inp | 826.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 826.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 826.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 862.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 824.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 825.00 | NIST | |
| Inp | 823.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 812.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | Outlier 127.02 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 819.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | 833.00 | NIST | |
| Inp | 846.00 | NIST | |
| I | [1613.00; 1698.00] |
|
|
| I | 1666.00 | NIST | |
| I | 1623.00 | NIST | |
| I | Outlier 1614.00 | NIST | |
| I | Outlier 1617.00 | NIST | |
| I | 1640.00 | NIST | |
| I | 1669.00 | NIST | |
| I | 1665.00 | NIST | |
| I | 1660.00 | NIST | |
| I | 1667.00 | NIST | |
| I | 1658.00 | NIST | |
| I | 1631.00 | NIST | |
| I | 1669.00 | NIST | |
| I | 1649.00 | NIST | |
| I | 1656.00 | NIST | |
| I | 1662.00 | NIST | |
| I | Outlier 1613.00 | NIST | |
| I | 1643.00 | NIST | |
| I | 1665.00 | NIST | |
| I | 1635.00 | NIST | |
| I | 1652.00 | NIST | |
| I | 1665.00 | NIST | |
| I | 1693.00 | NIST | |
| I | 1650.00 | NIST | |
| I | 1655.00 | NIST | |
| I | 1656.00 | NIST | |
| I | 1666.00 | NIST | |
| I | 1666.00 | NIST | |
| I | 1656.00 | NIST | |
| I | 1659.00 | NIST | |
| I | 1664.00 | NIST | |
| I | 1664.00 | NIST | |
| I | 1662.00 | NIST | |
| I | 1667.00 | NIST | |
| I | 1659.00 | NIST | |
| I | 1659.00 | NIST | |
| I | 1651.00 | NIST | |
| I | 1665.00 | NIST | |
| I | 1678.00 | NIST | |
| I | 1661.00 | NIST | |
| I | 1690.00 | NIST | |
| I | 1690.00 | NIST | |
| I | 1665.00 | NIST | |
| I | 1620.00 | NIST | |
| I | Outlier 1698.00 | NIST | |
| I | 1692.00 | NIST | |
| I | 1655.00 | NIST | |
| I | 1651.00 | NIST | |
| I | 1651.00 | NIST | |
| I | 1651.00 | NIST | |
| I | 1651.00 | NIST | |
| I | 1651.00 | NIST | |
| I | 1652.00 | NIST | |
| I | 1685.00 | NIST | |
| I | 1687.00 | NIST | |
| I | 1671.00 | NIST | |
| I | 1694.00 | NIST | |
| I | 1626.00 | NIST | |
| I | 1667.00 | NIST | |
| I | 1670.00 | NIST | |
| I | 1647.00 | NIST | |
| I | 1678.00 | NIST | |
| I | 1664.00 | NIST | |
| I | 1671.00 | NIST | |
| I | 1689.00 | NIST | |
| I | 1670.00 | NIST | |
| I | 1694.00 | NIST | |
| I | 1646.00 | NIST | |
| I | 1647.00 | NIST | |
| I | 1647.00 | NIST | |
| I | Outlier 1619.00 | NIST | |
| I | 1666.00 | NIST | |
| I | 1659.00 | NIST | |
| I | 1657.00 | NIST | |
| I | 1659.00 | NIST | |
| I | 1675.00 | NIST | |
| I | 1669.00 | NIST | |
| I | 1660.00 | NIST | |
| I | 1661.00 | NIST | |
| I | 1673.00 | NIST | |
| I | 1673.00 | NIST | |
| I | 1664.00 | NIST | |
| I | 1665.00 | NIST | |
| I | 1687.00 | NIST | |
| I | 1687.00 | NIST | |
| I | 1685.00 | NIST | |
| I | 1640.00 | NIST | |
| I | 1648.00 | NIST | |
| I | Outlier 1616.00 | NIST | |
| I | Outlier 1616.00 | NIST | |
| I | Outlier 1616.00 | NIST | |
| I | 1686.00 | NIST | |
| I | 1686.00 | NIST | |
| I | 1686.00 | NIST | |
| I | 1650.00 | NIST | |
| I | 1656.00 | NIST | |
| I | 1659.00 | NIST | |
| I | 1656.00 | NIST | |
| I | 1686.00 | NIST | |
| I | 1666.00 | NIST | |
| I | 1660.00 | NIST | |
| I | 1623.00 | NIST | |
| I | 1647.00 | NIST | |
| I | 1663.00 | NIST | |
| I | 1663.00 | NIST | |
| I | 1659.00 | NIST | |
| I | 1659.00 | NIST | |
| I | 1638.00 | NIST | |
| I | 1660.00 | NIST | |
| I | 1626.00 | NIST | |
| I | 1622.00 | NIST | |
| I | 1653.00 | NIST | |
| I | 1650.00 | NIST | |
| I | 1650.00 | NIST | |
| I | 1661.00 | NIST | |
| I | 1650.00 | NIST | |
| I | 1625.00 | NIST | |
| I | 1630.00 | NIST | |
| I | 1658.00 | NIST | |
| I | 1661.00 | NIST | |
| I | 1680.00 | NIST | |
| I | 1678.00 | NIST | |
| I | 1661.00 | NIST | |
| I | 1632.00 | NIST | |
| I | 1661.00 | NIST | |
| I | 1647.00 | NIST | |
| I | 1662.00 | NIST | |
| I | 1647.00 | NIST | |
| I | 1668.00 | NIST | |
| I | 1686.00 | NIST | |
| I | 1660.00 | NIST | |
| I | 1663.00 | NIST | |
| I | 1669.00 | NIST | |
| I | 1667.00 | NIST | |
| I | 1657.00 | NIST | |
| I | 1656.00 | NIST | |
| I | 1662.00 | NIST | |
| I | 1656.00 | NIST | |
| I | 1668.00 | NIST | |
| I | 1620.00 | NIST | |
| I | 1662.00 | NIST | |
| I | 1670.00 | NIST | |
| I | 1640.00 | NIST | |
| I | Outlier 1617.00 | NIST | |
| I | 1685.00 | NIST | |
| I | 1667.00 | NIST | |
| I | 1671.00 | NIST | |
| I | 1647.00 | NIST | |
| I | 1657.00 | NIST | |
| I | 1661.00 | NIST | |
| I | 1687.00 | NIST | |
| I | Outlier 1616.00 | NIST | |
| I | 1686.00 | NIST | |
| I | 1663.00 | NIST | |
| I | 1660.00 | NIST | |
| I | 1650.00 | NIST | |
| S°liquid | [215.50; 215.90] | J/mol×K |
|
| S°liquid | 215.90 | J/mol×K | NIST |
| S°liquid | 215.50 | J/mol×K | NIST |
| Ttriple | [253.50; 258.60] | K |
|
| Ttriple | 258.60 ± 0.20 | K | NIST |
| Ttriple | 253.50 ± 0.30 | K | NIST |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [193.30; 204.01] | J/mol×K | [298.15; 303.00] |
|
| Cp,liquid | 204.01 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 193.30 | J/mol×K | 303.00 | NIST |
| ΔfusH | [13.10; 14.81] | kJ/mol | [253.50; 258.60] |
|
| ΔfusH | 14.81 | kJ/mol | 253.50 | NIST |
| ΔfusH | 13.10 | kJ/mol | 258.60 | NIST |
| ΔfusH | 13.13 | kJ/mol | 258.60 | NIST |
| ΔvapH | 53.60 | kJ/mol | 373.50 | NIST |
| Pvap | [9.00e-03; 36.53] | kPa | [273.11; 412.11] |
|
| Pvap | 9.00e-03 | kPa | 273.11 | Phase e... |
| Pvap | 0.02 | kPa | 283.08 | Phase e... |
| Pvap | 0.05 | kPa | 293.16 | Phase e... |
| Pvap | 0.12 | kPa | 303.09 | Phase e... |
| Pvap | 0.24 | kPa | 313.15 | Phase e... |
| Pvap | 0.47 | kPa | 323.15 | Phase e... |
| Pvap | 0.47 | kPa | 323.16 | Phase e... |
| Pvap | 0.81 | kPa | 331.87 | Phase e... |
| Pvap | 0.89 | kPa | 333.15 | Phase e... |
| Pvap | 0.88 | kPa | 333.17 | Phase e... |
| Pvap | 1.48 | kPa | 341.85 | Phase e... |
| Pvap | 1.60 | kPa | 343.15 | Phase e... |
| Pvap | 1.61 | kPa | 343.19 | Phase e... |
| Pvap | 2.58 | kPa | 351.81 | Phase e... |
| Pvap | 2.75 | kPa | 353.15 | Phase e... |
| Pvap | 2.79 | kPa | 353.20 | Phase e... |
| Pvap | 2.60 | kPa | 353.30 | Isother... |
| Pvap | 4.37 | kPa | 362.09 | Phase e... |
| Pvap | 4.59 | kPa | 363.15 | Phase e... |
| Pvap | 4.65 | kPa | 363.20 | Phase e... |
| Pvap | 7.07 | kPa | 372.04 | Phase e... |
| Pvap | 7.00 | kPa | 373.00 | Isother... |
| Pvap | 7.40 | kPa | 373.15 | Phase e... |
| Pvap | 11.09 | kPa | 382.09 | Phase e... |
| Pvap | 11.59 | kPa | 383.15 | Phase e... |
| Pvap | 17.10 | kPa | 392.15 | Phase e... |
| Pvap | 17.68 | kPa | 393.15 | Phase e... |
| Pvap | 25.11 | kPa | 402.18 | Phase e... |
| Pvap | 30.10 | kPa | 407.90 | Isother... |
| Pvap | 36.53 | kPa | 412.11 | Phase e... |
| ρl | [1113.63; 1141.46] | kg/m3 | [283.15; 313.15] |
|
| ρl | 1141.46 | kg/m3 | 283.15 | Volumet... |
| ρl | 1132.26 | kg/m3 | 293.15 | Volumet... |
| ρl | 1130.27 | kg/m3 | 298.15 | Self-ag... |
| ρl | 1122.99 | kg/m3 | 303.15 | Volumet... |
| ρl | 1113.63 | kg/m3 | 313.15 | Volumet... |
| ΔfusS | [50.77; 58.40] | J/mol×K | [253.50; 258.60] |
|
| ΔfusS | 58.40 | J/mol×K | 253.50 | NIST |
| ΔfusS | 50.77 | J/mol×K | 258.60 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [339.70; 467.51] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.68800e+01 | |||
| Coefficient B | -4.88331e+03 | |||
| Coefficient C | -4.53900e+01 | |||
| Temperature range, min. | 339.70 | |||
| Temperature range, max. | 467.51 | |||
| Pvap | 1.33 | kPa | 339.70 | Calculated Property |
| Pvap | 2.86 | kPa | 353.90 | Calculated Property |
| Pvap | 5.74 | kPa | 368.10 | Calculated Property |
| Pvap | 10.87 | kPa | 382.30 | Calculated Property |
| Pvap | 19.53 | kPa | 396.50 | Calculated Property |
| Pvap | 33.53 | kPa | 410.71 | Calculated Property |
| Pvap | 55.30 | kPa | 424.91 | Calculated Property |
| Pvap | 87.96 | kPa | 439.11 | Calculated Property |
| Pvap | 135.46 | kPa | 453.31 | Calculated Property |
| Pvap | 202.64 | kPa | 467.51 | Calculated Property |
Similar Compounds
![Furan, 2,2'-[oxybis(methylene)]bis-.](data:image/png;base64,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)
Find more compounds similar to 2-Furanmethanol.
Mixtures
- Furan, 2-methyl- + 2-Furanmethanol
- 2-Furanmethanol + Isopropyl Alcohol
- 2-Furanmethanol + Water
- 2-Furanmethanol + Furan, 2,5-dimethyl-
- Toluene + 2-Furanmethanol
- 2-Furanmethanol + Ethanol
- 2-Furanmethanol + Pentane
- n-Hexane + 2-Furanmethanol
- 2-Furanmethanol + Heptane
- 2-Furanmethanol + Cyclopentane
- 2-Furanmethanol + Cyclohexane
- 2-Furanmethanol + Cycloheptane
- 2-Furanmethanol + 1-Hexene
- 2-Furanmethanol + 1-Heptene
- 2-Furanmethanol + 1-Hexyne
- 1-Heptyne + 2-Furanmethanol
- Benzene + 2-Furanmethanol
- 2-Furanmethanol + Carbon dioxide
Sources
- Crippen Method
- Crippen Method
- Isothermal vapor liquid equilibrium for binary mixtures containing furfural and its derivatives
- Activity coefficients at infinite dilution for hydrocarbons in furfuryl alcohol at T=(278.15 and 298.15) K, determined by g.l.c.
- Self-aggregation of liquids from biomass in aqueous solution
- Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
- Volumetric and acoustic properties of binary systems (furfural or furfuryl alcohol + toluene) and (furfuryl alcohol + ethanol) at different temperatures
- Solubilities of Carbon Dioxide in Five Bio-based Solvents
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.