- InChI
- InChI=1S/C5H4O2/c6-4-5-2-1-3-7-5/h1-4H
- InChI Key
- HYBBIBNJHNGZAN-UHFFFAOYSA-N
- Formula
- C5H4O2
- SMILES
- O=Cc1ccco1
- Molecular Weight1
- 96.08
- CAS
- 98-01-1
- Other Names
-
- .alpha.-furole
- 2-Furancarbonal
- 2-Furancarboxaldehyde (furfural)
- 2-Furankarbaldehyd
- 2-Furil-metanale
- 2-Furylaldehyde
- 2-Furylmethanal
- 2-formylfuran
- 2-furaldehyde
- 2-furanaldehyde
- 2-furancarbaldehyde
- 2-furancarboxaldehyde
- 2-furancarboxyaldehyde
- 2-furfural
- 2-furfuraldehyde
- 2-furylcarboxaldehyde
- Artificial ant oil
- Artificial oil of ants
- Fural
- Furale
- Furancarbonal
- Furfurale
- Furfurol
- Furfurole
- Furol
- Furole
- NCI-C56177
- NSC 8841
- Pyromucic aldehyde
- Qo furfural
- Rcra waste number U125
- furaldehyde
- furan-2-aldehyde
- furan-2-carbaldehyde
- furan-2-carboxaldehyde
- furancarboxaldehyde (furfural)
- furfural (2-furancarboxaldehyde)
- furfuraldehyde
- furfurylaldehyde
- «alpha»-Furole
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- Rg : Radius of Gyration.
- 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).
- n0 : Refractive Index.
- 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).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3830 | KDB | |
| ΔcH°liquid | [-2344.00; -2338.00] | kJ/mol |
|
| ΔcH°liquid | -2339.00 ± 0.08 | kJ/mol | NIST |
| ΔcH°liquid | -2344.00 | kJ/mol | NIST |
| ΔcH°liquid | -2338.00 | kJ/mol | NIST |
| μ | 3.60 | debye | KDB |
| Rg | 3.1700 | KDB | |
| ΔfH°gas | [-151.40; -144.30] | kJ/mol |
|
| ΔfH°gas | -149.60 | kJ/mol | NIST |
| ΔfH°gas | -151.04 | kJ/mol | NIST |
| ΔfH°gas | -144.30 | kJ/mol | NIST |
| ΔfH°gas | -151.40 | kJ/mol | NIST |
| ΔfH°liquid | [-202.00; -194.90] | kJ/mol |
|
| ΔfH°liquid | -200.20 | kJ/mol | NIST |
| ΔfH°liquid | -194.90 | kJ/mol | NIST |
| ΔfH°liquid | -202.00 | kJ/mol | NIST |
| ΔvapH° | [50.60; 50.70] | kJ/mol |
|
| ΔvapH° | 50.70 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 50.70 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 50.63 ± 0.42 | kJ/mol | NIST |
| ΔvapH° | 50.60 ± 0.40 | kJ/mol | NIST |
| IE | [9.21; 9.50] | eV |
|
| IE | 9.22 ± 0.01 | eV | NIST |
| IE | 9.22 | eV | NIST |
| IE | Outlier 9.50 ± 0.05 | eV | NIST |
| IE | 9.22 | eV | NIST |
| IE | 9.21 ± 0.01 | eV | NIST |
| IE | 9.22 | eV | NIST |
| log10WS | [-0.10; -0.10] |
|
|
| log10WS | -0.10 | Aq. Solubility Prediction | |
| log10WS | -0.10 | Estimated Solubility | |
| logPoct/wat | 1.092 | Crippen Calculated Property | |
| McVol | 69.290 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 1 | KDB | |
| NFPA Safety | 1 | KDB | |
| Pc | [5510.00; 5890.00] | kPa |
|
| Pc | 5890.00 | kPa | KDB |
| Pc | 5510.00 ± 98.06 | kPa | NIST |
| Inp | [123.78; 860.00] |
|
|
| Inp | 805.00 | NIST | |
| Inp | 825.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 825.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 812.00 | NIST | |
| Inp | 820.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 818.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 818.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 836.00 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 826.00 | NIST | |
| Inp | 831.00 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 833.00 | NIST | |
| Inp | 840.00 | NIST | |
| Inp | 833.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 841.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 817.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 831.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 794.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 847.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 807.00 | NIST | |
| Inp | 795.00 | NIST | |
| Inp | 795.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 838.00 | NIST | |
| Inp | 838.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 800.40 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 795.00 | NIST | |
| Inp | 795.00 | NIST | |
| Inp | 833.84 | NIST | |
| Inp | 835.20 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 826.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 816.00 | NIST | |
| Inp | 799.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 842.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 810.00 | NIST | |
| Inp | 808.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 799.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 840.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 840.00 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 836.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 824.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 825.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 831.00 | NIST | |
| Inp | 836.00 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 828.00 | NIST | |
| Inp | 842.00 | NIST | |
| Inp | 828.00 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 826.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 828.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 831.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 821.00 | NIST | |
| Inp | 833.00 | NIST | |
| Inp | 831.00 | NIST | |
| Inp | 808.00 | NIST | |
| Inp | 838.20 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 807.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 810.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 794.00 | NIST | |
| Inp | 797.00 | NIST | |
| Inp | 798.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 831.00 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 796.00 | NIST | |
| Inp | 836.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 831.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 833.00 | NIST | |
| Inp | 809.00 | NIST | |
| Inp | 801.05 | NIST | |
| Inp | 817.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 833.00 | NIST | |
| Inp | 820.00 | NIST | |
| Inp | 808.00 | NIST | |
| Inp | 808.00 | NIST | |
| Inp | 798.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 810.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | 836.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 841.00 | NIST | |
| Inp | 799.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 828.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 799.00 | NIST | |
| Inp | 810.00 | NIST | |
| Inp | 813.00 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 828.00 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 840.00 | NIST | |
| Inp | 820.00 | NIST | |
| Inp | 842.00 | NIST | |
| Inp | 831.00 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 831.00 | NIST | |
| Inp | 836.00 | NIST | |
| Inp | 833.00 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 826.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 828.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 831.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 828.00 | NIST | |
| Inp | 836.00 | NIST | |
| Inp | 836.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 798.00 | NIST | |
| Inp | 838.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 817.00 | NIST | |
| Inp | 817.00 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 828.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 828.00 | NIST | |
| Inp | 812.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 828.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 838.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 797.00 | NIST | |
| Inp | 797.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 825.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 820.00 | NIST | |
| Inp | Outlier 123.78 | NIST | |
| Inp | 828.00 | NIST | |
| Inp | 820.00 | NIST | |
| Inp | 831.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 817.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 841.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 795.00 | NIST | |
| Inp | 800.40 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 816.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 802.00 | NIST | |
| Inp | 799.00 | NIST | |
| I | [1410.00; 1503.00] |
|
|
| I | 1467.00 | NIST | |
| I | 1467.00 | NIST | |
| I | 1486.00 | NIST | |
| I | 1468.00 | NIST | |
| I | 1466.00 | NIST | |
| I | 1467.00 | NIST | |
| I | 1440.00 | NIST | |
| I | 1459.00 | NIST | |
| I | 1449.00 | NIST | |
| I | 1437.00 | NIST | |
| I | 1437.00 | NIST | |
| I | Outlier 1425.00 | NIST | |
| I | 1432.00 | NIST | |
| I | 1448.00 | NIST | |
| I | 1449.00 | NIST | |
| I | 1445.00 | NIST | |
| I | 1444.00 | NIST | |
| I | 1460.00 | NIST | |
| I | 1464.00 | NIST | |
| I | 1439.00 | NIST | |
| I | 1465.00 | NIST | |
| I | 1480.00 | NIST | |
| I | 1476.00 | NIST | |
| I | 1462.00 | NIST | |
| I | 1458.00 | NIST | |
| I | 1469.00 | NIST | |
| I | 1456.00 | NIST | |
| I | 1458.00 | NIST | |
| I | 1468.00 | NIST | |
| I | 1462.00 | NIST | |
| I | 1432.00 | NIST | |
| I | 1445.00 | NIST | |
| I | 1455.00 | NIST | |
| I | 1474.00 | NIST | |
| I | 1471.00 | NIST | |
| I | 1471.00 | NIST | |
| I | 1454.00 | NIST | |
| I | 1447.00 | NIST | |
| I | 1462.00 | NIST | |
| I | 1439.00 | NIST | |
| I | 1438.00 | NIST | |
| I | 1451.00 | NIST | |
| I | 1471.00 | NIST | |
| I | 1456.00 | NIST | |
| I | 1448.00 | NIST | |
| I | 1471.00 | NIST | |
| I | 1449.00 | NIST | |
| I | 1452.00 | NIST | |
| I | 1448.00 | NIST | |
| I | 1447.00 | NIST | |
| I | 1460.00 | NIST | |
| I | 1472.00 | NIST | |
| I | 1460.00 | NIST | |
| I | 1455.00 | NIST | |
| I | 1462.00 | NIST | |
| I | 1473.00 | NIST | |
| I | 1472.00 | NIST | |
| I | 1458.00 | NIST | |
| I | 1495.00 | NIST | |
| I | 1456.00 | NIST | |
| I | 1456.00 | NIST | |
| I | 1467.00 | NIST | |
| I | 1447.00 | NIST | |
| I | 1465.00 | NIST | |
| I | 1466.00 | NIST | |
| I | 1457.00 | NIST | |
| I | 1451.00 | NIST | |
| I | 1469.00 | NIST | |
| I | 1471.00 | NIST | |
| I | 1445.00 | NIST | |
| I | 1455.00 | NIST | |
| I | 1454.00 | NIST | |
| I | 1455.00 | NIST | |
| I | 1460.00 | NIST | |
| I | 1429.00 | NIST | |
| I | 1474.00 | NIST | |
| I | 1473.00 | NIST | |
| I | 1478.00 | NIST | |
| I | 1467.00 | NIST | |
| I | 1470.00 | NIST | |
| I | 1493.00 | NIST | |
| I | 1493.00 | NIST | |
| I | 1453.00 | NIST | |
| I | 1462.00 | NIST | |
| I | 1457.00 | NIST | |
| I | 1476.00 | NIST | |
| I | 1493.00 | NIST | |
| I | Outlier 1422.00 | NIST | |
| I | 1457.00 | NIST | |
| I | 1457.00 | NIST | |
| I | 1468.00 | NIST | |
| I | 1435.00 | NIST | |
| I | 1471.00 | NIST | |
| I | 1446.00 | NIST | |
| I | 1446.00 | NIST | |
| I | 1446.00 | NIST | |
| I | 1448.00 | NIST | |
| I | 1448.00 | NIST | |
| I | 1449.00 | NIST | |
| I | 1487.00 | NIST | |
| I | 1492.00 | NIST | |
| I | 1494.00 | NIST | |
| I | 1455.00 | NIST | |
| I | 1483.00 | NIST | |
| I | 1441.00 | NIST | |
| I | 1456.00 | NIST | |
| I | 1469.00 | NIST | |
| I | 1427.00 | NIST | |
| I | 1452.00 | NIST | |
| I | 1482.00 | NIST | |
| I | 1460.00 | NIST | |
| I | 1443.00 | NIST | |
| I | 1473.00 | NIST | |
| I | 1470.00 | NIST | |
| I | Outlier 1503.00 | NIST | |
| I | 1477.00 | NIST | |
| I | 1479.00 | NIST | |
| I | 1483.00 | NIST | |
| I | 1433.00 | NIST | |
| I | 1456.00 | NIST | |
| I | 1456.00 | NIST | |
| I | 1466.00 | NIST | |
| I | Outlier 1423.00 | NIST | |
| I | 1494.00 | NIST | |
| I | 1468.00 | NIST | |
| I | 1468.00 | NIST | |
| I | 1430.00 | NIST | |
| I | 1467.00 | NIST | |
| I | 1467.00 | NIST | |
| I | 1473.00 | NIST | |
| I | 1454.00 | NIST | |
| I | 1448.00 | NIST | |
| I | 1472.00 | NIST | |
| I | 1472.00 | NIST | |
| I | 1485.00 | NIST | |
| I | 1485.00 | NIST | |
| I | 1470.00 | NIST | |
| I | 1483.00 | NIST | |
| I | 1461.00 | NIST | |
| I | 1483.00 | NIST | |
| I | 1469.00 | NIST | |
| I | 1458.00 | NIST | |
| I | 1458.00 | NIST | |
| I | 1485.00 | NIST | |
| I | 1471.00 | NIST | |
| I | 1447.00 | NIST | |
| I | 1478.00 | NIST | |
| I | 1478.00 | NIST | |
| I | 1487.00 | NIST | |
| I | 1494.00 | NIST | |
| I | 1492.00 | NIST | |
| I | 1481.00 | NIST | |
| I | 1490.00 | NIST | |
| I | 1474.00 | NIST | |
| I | 1465.00 | NIST | |
| I | 1474.00 | NIST | |
| I | 1490.00 | NIST | |
| I | 1490.00 | NIST | |
| I | 1445.00 | NIST | |
| I | 1496.00 | NIST | |
| I | 1489.00 | NIST | |
| I | 1471.00 | NIST | |
| I | 1455.00 | NIST | |
| I | 1465.00 | NIST | |
| I | 1475.00 | NIST | |
| I | 1456.00 | NIST | |
| I | 1465.00 | NIST | |
| I | 1475.00 | NIST | |
| I | 1475.00 | NIST | |
| I | Outlier 1410.00 | NIST | |
| I | 1471.00 | NIST | |
| I | 1462.00 | NIST | |
| I | 1451.00 | NIST | |
| I | 1473.00 | NIST | |
| I | 1426.00 | NIST | |
| I | 1427.00 | NIST | |
| I | 1461.00 | NIST | |
| I | 1452.00 | NIST | |
| I | 1469.00 | NIST | |
| I | 1475.00 | NIST | |
| I | 1469.00 | NIST | |
| I | 1469.00 | NIST | |
| I | 1469.00 | NIST | |
| I | 1470.00 | NIST | |
| I | 1449.00 | NIST | |
| I | 1427.00 | NIST | |
| I | 1457.00 | NIST | |
| I | 1429.00 | NIST | |
| I | 1427.00 | NIST | |
| I | 1427.00 | NIST | |
| I | 1454.00 | NIST | |
| I | 1454.00 | NIST | |
| I | 1450.00 | NIST | |
| I | 1449.00 | NIST | |
| I | 1449.00 | NIST | |
| I | 1450.00 | NIST | |
| I | 1441.00 | NIST | |
| I | 1465.00 | NIST | |
| I | 1471.00 | NIST | |
| I | 1450.00 | NIST | |
| I | 1452.00 | NIST | |
| I | 1452.00 | NIST | |
| I | 1450.00 | NIST | |
| I | 1452.00 | NIST | |
| I | 1458.00 | NIST | |
| I | 1477.00 | NIST | |
| I | 1486.00 | NIST | |
| I | 1460.00 | NIST | |
| I | 1465.00 | NIST | |
| I | 1465.00 | NIST | |
| I | 1464.00 | NIST | |
| I | 1464.00 | NIST | |
| I | 1474.00 | NIST | |
| I | 1451.00 | NIST | |
| I | 1482.00 | NIST | |
| I | 1467.00 | NIST | |
| I | 1486.00 | NIST | |
| I | 1486.00 | NIST | |
| I | 1469.00 | NIST | |
| I | 1467.00 | NIST | |
| I | 1464.00 | NIST | |
| I | 1444.00 | NIST | |
| I | 1477.00 | NIST | |
| I | 1462.00 | NIST | |
| I | 1477.00 | NIST | |
| I | 1477.00 | NIST | |
| I | 1452.00 | NIST | |
| I | 1483.00 | NIST | |
| I | 1459.00 | NIST | |
| I | 1461.00 | NIST | |
| I | 1449.00 | NIST | |
| I | 1426.00 | NIST | |
| I | 1455.00 | NIST | |
| I | 1466.00 | NIST | |
| I | 1466.00 | NIST | |
| I | 1456.00 | NIST | |
| I | 1459.00 | NIST | |
| I | 1478.00 | NIST | |
| I | 1466.00 | NIST | |
| I | 1495.00 | NIST | |
| I | 1483.00 | NIST | |
| I | 1436.00 | NIST | |
| I | Outlier 1410.00 | NIST | |
| I | Outlier 1410.00 | NIST | |
| I | 1445.00 | NIST | |
| I | 1433.00 | NIST | |
| I | 1447.00 | NIST | |
| I | 1450.00 | NIST | |
| I | 1471.00 | NIST | |
| I | 1479.00 | NIST | |
| I | 1479.00 | NIST | |
| I | 1460.00 | NIST | |
| I | 1479.00 | NIST | |
| I | 1482.00 | NIST | |
| I | 1474.00 | NIST | |
| I | 1445.00 | NIST | |
| I | 1468.00 | NIST | |
| I | 1449.00 | NIST | |
| I | 1452.00 | NIST | |
| I | 1483.00 | NIST | |
| I | 1460.00 | NIST | |
| I | 1449.00 | NIST | |
| I | 1441.00 | NIST | |
| I | Outlier 1421.00 | NIST | |
| I | 1447.00 | NIST | |
| I | 1456.00 | NIST | |
| I | 1456.00 | NIST | |
| I | 1449.00 | NIST | |
| I | 1446.00 | NIST | |
| I | 1457.00 | NIST | |
| I | 1441.00 | NIST | |
| I | 1462.00 | NIST | |
| I | 1467.00 | NIST | |
| I | 1437.00 | NIST | |
| I | 1445.00 | NIST | |
| I | 1487.00 | NIST | |
| I | 1441.00 | NIST | |
| I | 1482.00 | NIST | |
| I | Outlier 1503.00 | NIST | |
| I | 1456.00 | NIST | |
| I | 1468.00 | NIST | |
| I | 1473.00 | NIST | |
| I | 1485.00 | NIST | |
| I | 1483.00 | NIST | |
| I | 1471.00 | NIST | |
| I | 1494.00 | NIST | |
| I | 1465.00 | NIST | |
| I | 1496.00 | NIST | |
| I | 1475.00 | NIST | |
| I | Outlier 1410.00 | NIST | |
| I | 1426.00 | NIST | |
| I | 1449.00 | NIST | |
| I | 1427.00 | NIST | |
| I | 1450.00 | NIST | |
| I | 1458.00 | NIST | |
| I | 1477.00 | NIST | |
| I | 1461.00 | NIST | |
| I | 1466.00 | NIST | |
| I | 1495.00 | NIST | |
| I | 1479.00 | NIST | |
| I | 1474.00 | NIST | |
| I | 1447.00 | NIST | |
| I | 1457.00 | NIST | |
| S°liquid | 218.00 | J/mol×K | NIST |
| Tboil | [434.15; 435.15] | K |
|
| Tboil | 435.00 | K | Solubility and tie-line data for ternary aqueous mixtures of cyclopentanol with organic solvents at T = 298.2 K: Experiments and NRTL model |
| Tboil | 435.15 | K | Isobaric vapour-liquid equilibrium measurements and extractive distillation process for the azeotrope of (N,N-dimethylisopropylamine + acetone) |
| Tboil | 434.90 | K | KDB |
| Tboil | 434.90 | K | NIST |
| Tboil | 434.85 ± 0.50 | K | NIST |
| Tboil | 434.65 ± 1.00 | K | NIST |
| Tboil | 434.90 ± 0.50 | K | NIST |
| Tboil | 435.00 ± 2.00 | K | NIST |
| Tboil | 434.60 ± 0.50 | K | NIST |
| Tboil | Outlier 434.15 ± 1.50 | K | NIST |
| Tboil | 434.60 ± 0.50 | K | NIST |
| Tboil | 434.60 ± 0.50 | K | NIST |
| Tboil | 434.60 ± 0.50 | K | NIST |
| Tboil | 434.60 ± 0.50 | K | NIST |
| Tc | [670.00; 670.00] | K |
|
| Tc | 670.00 | K | KDB |
| Tc | 670.00 ± 2.00 | K | NIST |
| Tfus | [234.50; 236.60] | K |
|
| Tfus | 236.60 | K | KDB |
| Tfus | 236.00 | K | Aq. Solubility Prediction |
| Tfus | 234.50 ± 0.40 | K | NIST |
| Ttriple | [235.10; 235.10] | K |
|
| Ttriple | 235.10 ± 0.40 | K | NIST |
| Ttriple | 235.10 ± 0.40 | K | NIST |
| Zra | 0.26 | KDB |
Cheméo can also estimate Critical Volume, Standard Gibbs free energy of formation 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
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 363.20 | K | 8.70 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [328.97; 460.72] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.46545e+01 | |||
| Coefficient B | -3.52022e+03 | |||
| Coefficient C | -8.39460e+01 | |||
| Temperature range, min. | 328.97 | |||
| Temperature range, max. | 460.72 | |||
| Pvap | 1.33 | kPa | 328.97 | Calculated Property |
| Pvap | 3.00 | kPa | 343.61 | Calculated Property |
| Pvap | 6.18 | kPa | 358.25 | Calculated Property |
| Pvap | 11.84 | kPa | 372.89 | Calculated Property |
| Pvap | 21.30 | kPa | 387.53 | Calculated Property |
| Pvap | 36.31 | kPa | 402.16 | Calculated Property |
| Pvap | 59.07 | kPa | 416.80 | Calculated Property |
| Pvap | 92.23 | kPa | 431.44 | Calculated Property |
| Pvap | 138.90 | kPa | 446.08 | Calculated Property |
| Pvap | 202.64 | kPa | 460.72 | Calculated Property |
| Pvap | [1.50e-03; 5477.68] | kPa | [236.65; 657.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 6.59497e+01 | |||
| Coefficient B | -7.83040e+03 | |||
| Coefficient C | -7.23773e+00 | |||
| Coefficient D | 3.55203e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 236.65 | |||
| Temperature range, max. | 657.00 | |||
| Pvap | 1.50e-03 | kPa | 236.65 | Calculated Property |
| Pvap | 0.10 | kPa | 283.36 | Calculated Property |
| Pvap | 1.89 | kPa | 330.06 | Calculated Property |
| Pvap | 15.48 | kPa | 376.77 | Calculated Property |
| Pvap | 75.07 | kPa | 423.47 | Calculated Property |
| Pvap | 256.28 | kPa | 470.18 | Calculated Property |
| Pvap | 685.02 | kPa | 516.88 | Calculated Property |
| Pvap | 1537.66 | kPa | 563.59 | Calculated Property |
| Pvap | 3040.60 | kPa | 610.29 | Calculated Property |
| Pvap | 5477.68 | kPa | 657.00 | Calculated Property |
| Pvap | [1.76; 100.24] | kPa | [329.02; 433.90] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.40309e+01 | |||
| Coefficient B | -3.29300e+03 | |||
| Coefficient C | -8.44490e+01 | |||
| Reference | Matthews, Sumner, et al., 1950, 2 | |||
| Temperature range, min. | 329.02 | |||
| Temperature range, max. | 433.90 | |||
| Pvap | 1.76 | kPa | 329.02 | Calculated Property |
| Pvap | 3.25 | kPa | 340.67 | Calculated Property |
| Pvap | 5.69 | kPa | 352.33 | Calculated Property |
| Pvap | 9.49 | kPa | 363.98 | Calculated Property |
| Pvap | 15.21 | kPa | 375.63 | Calculated Property |
| Pvap | 23.50 | kPa | 387.29 | Calculated Property |
| Pvap | 35.16 | kPa | 398.94 | Calculated Property |
| Pvap | 51.12 | kPa | 410.59 | Calculated Property |
| Pvap | 72.42 | kPa | 422.25 | Calculated Property |
| Pvap | 100.24 | kPa | 433.90 | Calculated Property |
| Pvap | [1.76; 100.24] | kPa | [329.02; 433.90] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.40309e+01 | |||
| Coefficient B | -3.29300e+03 | |||
| Coefficient C | -8.44490e+01 | |||
| Reference | Matthews, Sumner, et al., 1950 | |||
| Temperature range, min. | 329.02 | |||
| Temperature range, max. | 433.90 | |||
| Pvap | 1.76 | kPa | 329.02 | Calculated Property |
| Pvap | 3.25 | kPa | 340.67 | Calculated Property |
| Pvap | 5.69 | kPa | 352.33 | Calculated Property |
| Pvap | 9.49 | kPa | 363.98 | Calculated Property |
| Pvap | 15.21 | kPa | 375.63 | Calculated Property |
| Pvap | 23.50 | kPa | 387.29 | Calculated Property |
| Pvap | 35.16 | kPa | 398.94 | Calculated Property |
| Pvap | 51.12 | kPa | 410.59 | Calculated Property |
| Pvap | 72.42 | kPa | 422.25 | Calculated Property |
| Pvap | 100.24 | kPa | 433.90 | Calculated Property |
Similar Compounds
Find more compounds similar to Furfural.
Mixtures
- Furan + Furfural
- Furfural + Water
- Furfural + 1-Butanol + Water
- Furfural + Ethyl Acetate + Water
- Furfural + Acetic acid, propyl ester + Water
- Furfural + Acetic acid + Water
- Furfural + Ethanol
- Furfural + 1-Butanol
- p-Xylene + Furfural + Water
- Toluene + Furfural + Water
- Furfural + 2-Pentanol, 4-methyl- + Water
- Furfural + Benzyl alcohol + Water
- Furfural + Acetophenone + Water
- Furfural + Water + Furan, tetrahydro-2-methyl-
- Furfural + Cyclopentane,methoxy- + Water
- n-Hexane + Furfural
- Furan + n-Hexane + Furfural
- Furfural + Pentane
- Furfural + Heptane
- Furfural + Cyclopentane
Find more mixtures with Furfural.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Experimental and calculated liquid-liquid equilibrium data for water + furfural + solvents
- Isothermal vapor-liquid equilibrium and excess molar enthalpies of the binary mixtures furfural + methyl isobutyl ketone, + 2-butanol and + 2-methyl-2-butanol
- Solubility and tie-line data for ternary aqueous mixtures of cyclopentanol with organic solvents at T = 298.2 K: Experiments and NRTL model
- Isothermal vapor liquid equilibrium for binary mixtures containing furfural and its derivatives
- Enhancement of bio-oil derived chemicals in aqueous phase using ionic liquids: Experimental and COSMO-SAC predictions using a modified hydrogen bonding expression
- Liquid-liquid equilibria for the extraction of furfural from aqueous solution using different solvents
- Equilibrium data and GC-PC SAFT predictions for furanic extraction
- Liquid-liquid equilibria of water + solutes (acetic acid/ acetol/furfural/guaiacol/methanol/phenol/propanal) + solvents (isopropyl acetate/toluene) ternary systems for pyrolysis oil fractionation
- The determination of activity coefficients at infinite dilution using g.l.c. for hydrocarbons in furfural at T = 278:15 K and T = 298:15 K
- Determination of infinite dilution activity coefficients using HS-SPME/GC/FID for hydrocarbons in furfural at temperatures of (298.15, 308.15, and 318.15) K
- Self-aggregation of liquids from biomass in aqueous solution
- Ternary and binary LLE measurements for solvent (2-methyltetrahydrofuran and cyclopentyl methyl ether) + furfural + water between 298 and 343 K
- Hydrogen solubility in furfural and 2-propanol: Experiments and modeling
- Quaternary and ternary LLE measurements for solvent (2-methyltetrahydrofuran and cyclopentyl methyl ether) + furfural + acetic acid + water between 298 and 343 K
- Liquid-liquid equilibria for the ternary system of water + furfural + solvents at 303.15 and 323.15 K under atmospheric pressure
- Isobaric vapour-liquid equilibrium measurements and extractive distillation process for the azeotrope of (N,N-dimethylisopropylamine + acetone)
- Excess volumes and partial molar volumes of binary liquid mixtures of furfural or 2-methylfuran with alcohols at 298.15 K
- Effects of alkyl group and temperature on the interactions between furfural and alcohol: Insight from density and sound velocity studies
- Volumetric and acoustic properties of binary systems (furfural or furfuryl alcohol + toluene) and (furfuryl alcohol + ethanol) at different temperatures
- Mutual Solubilities for the Water 2-sec-Butylphenol System and Partition Coefficients for Furfural and Formic Acid in the Water 2-sec-Butylphenol System
- Ternary and Binary LLE Measurements for Solvent (4- Methyl-2-pentanone and 2-Methyl-2-butanol) + Furfural + Water between 298 and 401 K
- Quaternary, Ternary, and Binary LLE Measurements for 2-Methoxy-2-methylpropane + Furfural + Acetic Acid + Water at Temperatures between 298 and 307 K
- Quaternary, Ternary and Binary LLE Measurements for 2-Methoxy-2-methylbutane + Furfural + Acetic Acid + Water at Temperatures between 298 and 341 K
- Thermophysical Properties and Solubility of Different Sugar-Derived Molecules in Deep Eutectic Solvents
- Vapor Pressure and Isobaric Vapor-Liquid Equilibrium for Binary Systems of Furfural, 2-Acetylfuran, and 5-Methylfurfural at 3.60 and 5.18 kPa
- Mutual Influence of Furfural and Furancarboxylic Acids on Their Solubility in Aqueous Solutions: Experiments and Perturbed-Chain Statistical Associating Fluid Theory (PC-SAFT) Predictions
- Liquid-Liquid Phase Equilibria for Quinary, Quaternary, and Ternary Systems {Water + Furfural + Acetic Acid + Cyclopentyl Methyl Ether + CaCl2}: Measurement, Effect of Salt ,and Comparative Study
- Liquid-Liquid Equilibria of Formic Acid and Furfural in a Biphasic Aqueous-Organic System: Optimization of Solvent and Amine Extractant
- Isobaric Vapor-Liquid Equilibrium of Furfural + gamma-Valerolactone at 30 kPa and Isothermal Liquid-Liquid Equilibrium of Carbon Dioxide + gamma-Valerolactone + Water at 298 K
- Measurement and Modeling of Phase Equilibria in Systems Containing Water, Xylose, Furfural, and Acetic Acid
- Liquid-liquid equilibria for mixtures of (Furfural + an Aromatic hydrocarbon + an alkane) at T=298.15 K
- Phase Equilibria of Water + Furfural and Dichloromethane + n-Hexane
- Liquid-Liquid Equilibria for Mixtures of (Furfural + a Chlorinated Aromatic Compound + an Alkane) at T = 298.15 K
- Separation of Furfural from Ternary Mixtures
- Limiting Separation Factors and Limiting Activity Coefficients for 2-Furfural, gamma-Nonalactone, Benzaldehyde, and Linalool in Water at 100 deg C
- Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
- Mutual Solubilities for Water-o-Nitrotoluene System and Distribution Coefficients for Furfural and Acetic Acid in Water-o-Nitrotoluene System
- Liquid-Liquid Equilibria Measurement of Systems Involving Alkanes (Heptane and Dodecane), Aromatics (Benzene or Toluene), and Furfural
- Infinite Dilution Binary Diffusion Coefficients for Compounds Derived from Biomass in Water at 0.1 MPa and Temperatures from (298.2 to 353.2) K
- Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
- Solubility of Benzothiazolium Ionic Liquids in Water and in Furfural
- Solubilities of Hexanal, Benzaldehyde, 2-Furfural, 2-Phenylethanol, Phenylethanal, and c-Nonalactone in Water at Temperatures between (50 and 100) deg C
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- 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.
These property values are available through the Cheméo API. A free account gives you an access key.