- 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
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- 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).
- IE : Ionization energy (eV).
- 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.
- Pc : Critical Pressure (kPa).
- 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).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.5660 | Relay (1.0) Calculated Property | |
| 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 |
| ΔfG° | -140.55 | kJ/mol | Relay (1.0-beta) Calculated Property |
| 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 |
| IE | 8.81 | eV | Relay (1.0) Calculated Property |
| log10WS | 0.21 | Relay (1.0) 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 | |
| Pc | 4909.54 | kPa | Relay (1.0-beta) Calculated Property |
| 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 |
| Tboil | 450.51 | K | Relay (1.0) Calculated Property |
| Tc | 667.74 | K | Relay (1.0) Calculated Property |
| Tfus | 275.23 | K | Relay (1.0) Calculated Property |
| Ttriple | [253.50; 258.60] | K |
|
| Ttriple | 258.60 ± 0.20 | K | NIST |
| Ttriple | 253.50 ± 0.30 | K | NIST |
| Vc | 0.274 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [339.70; 467.51] |
The Yaws Handbook of Vapor Pressure
|
| 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
- 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
- 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
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.