- InChI
- InChI=1S/C6H8O/c1-5-3-4-6(2)7-5/h3-4H,1-2H3
- InChI Key
- GSNUFIFRDBKVIE-UHFFFAOYSA-N
- Formula
- C6H8O
- SMILES
- Cc1ccc(C)o1
- Molecular Weight1
- 96.13
- CAS
- 625-86-5
- Other Names
-
- 2,5-Dimethylfuran
- 2,5-Dimethylfurane
- 2,5-dimethyloxole
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (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).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | 865.90 | kJ/mol | NIST |
| BasG | 835.20 | kJ/mol | NIST |
| ΔvapH° | 31.80 ± 0.30 | kJ/mol | NIST |
| IE | [7.80; 8.25] | eV |
|
| IE | 7.80 | eV | NIST |
| IE | 8.25 ± 0.10 | eV | NIST |
| IE | 8.03 | eV | NIST |
| log10WS | -6.16 | Crippen Calculated Property | |
| logPoct/wat | 1.896 | Crippen Calculated Property | |
| McVol | 81.810 | ml/mol | McGowan Calculated Property |
| Inp | [667.00; 728.00] |
|
|
| Inp | 696.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 697.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 697.00 | NIST | |
| Inp | Outlier 667.00 | NIST | |
| Inp | 701.00 | NIST | |
| Inp | 701.00 | NIST | |
| Inp | 718.00 | NIST | |
| Inp | 696.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 697.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 708.00 | NIST | |
| Inp | Outlier 728.00 | NIST | |
| Inp | 706.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 706.00 | NIST | |
| Inp | 704.00 | NIST | |
| Inp | 711.00 | NIST | |
| Inp | 723.00 | NIST | |
| Inp | 707.00 | NIST | |
| Inp | 700.00 | NIST | |
| Inp | 715.00 | NIST | |
| Inp | 700.00 | NIST | |
| Inp | 712.00 | NIST | |
| Inp | Outlier 727.00 | NIST | |
| Inp | Outlier 728.00 | NIST | |
| Inp | 718.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 703.00 | NIST | |
| Inp | 708.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 697.00 | NIST | |
| Inp | 700.00 | NIST | |
| Inp | 707.00 | NIST | |
| Inp | 697.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 697.00 | NIST | |
| Inp | 697.00 | NIST | |
| Inp | 697.00 | NIST | |
| Inp | 712.00 | NIST | |
| Inp | 703.00 | NIST | |
| Inp | 707.00 | NIST | |
| Inp | 697.00 | NIST | |
| Inp | 706.00 | NIST | |
| Inp | 723.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 696.00 | NIST | |
| I | [890.00; 972.00] |
|
|
| I | 939.00 | NIST | |
| I | Outlier 892.00 | NIST | |
| I | 925.00 | NIST | |
| I | 938.00 | NIST | |
| I | Outlier 890.00 | NIST | |
| I | 950.00 | NIST | |
| I | 943.00 | NIST | |
| I | 930.00 | NIST | |
| I | 958.00 | NIST | |
| I | 958.00 | NIST | |
| I | 952.00 | NIST | |
| I | 958.00 | NIST | |
| I | 946.00 | NIST | |
| I | 925.00 | NIST | |
| I | 934.00 | NIST | |
| I | 945.00 | NIST | |
| I | 931.00 | NIST | |
| I | 933.00 | NIST | |
| I | 933.00 | NIST | |
| I | 933.00 | NIST | |
| I | 934.00 | NIST | |
| I | 938.00 | NIST | |
| I | 909.00 | NIST | |
| I | 943.00 | NIST | |
| I | Outlier 972.00 | NIST | |
| I | 957.00 | NIST | |
| I | 952.00 | NIST | |
| I | 930.00 | NIST | |
| I | 930.00 | NIST | |
| I | 930.00 | NIST | |
| I | 949.00 | NIST | |
| I | 951.00 | NIST | |
| I | 951.00 | NIST | |
| I | 953.00 | NIST | |
| I | 951.00 | NIST | |
| I | 938.00 | NIST | |
| I | 939.00 | NIST | |
| I | 939.00 | NIST | |
| I | 951.00 | NIST | |
| I | 931.00 | NIST | |
| I | 943.00 | NIST | |
| I | 945.00 | NIST | |
| I | 934.00 | NIST | |
| Tboil | 366.83 | K | Vapor L... |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 32.30 ± 0.30 | kJ/mol | 289.50 | NIST |
| Pvap | [13.94; 212.88] | kPa | [313.15; 393.15] |
|
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 320 340 360 380 | ||||
| Pvap | 13.94 | kPa | 313.15 | Phase e... |
| Pvap | 21.54 | kPa | 323.15 | Phase e... |
| Pvap | 32.20 | kPa | 333.15 | Phase e... |
| Pvap | 46.74 | kPa | 343.15 | Phase e... |
| Pvap | 66.08 | kPa | 353.15 | Phase e... |
| Pvap | 91.23 | kPa | 363.15 | Phase e... |
| Pvap | 123.28 | kPa | 373.15 | Phase e... |
| Pvap | 163.43 | kPa | 383.15 | Phase e... |
| Pvap | 212.88 | kPa | 393.15 | Phase e... |
| n0 | [1.44012; 1.44012] | [298.15; 298.15] |
|
|
| n0 | 1.44012 | 298.15 | Isobari... | |
| n0 | 1.44012 | 298.15 | Isobari... | |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 283.15 | 912.25 |
| 100.00 | 288.15 | 906.99 |
| 100.00 | 293.15 | 901.64 |
| 100.00 | 298.15 | 896.29 |
| 100.00 | 303.15 | 890.9 |
| 100.00 | 308.15 | 885.45 |
| 100.00 | 313.15 | 879.93 |
| 100.00 | 318.15 | 874.44 |
| 100.00 | 323.15 | 868.85 |
| 100.00 | 328.15 | 863.25 |
| 100.00 | 333.15 | 857.58 |
| 100.00 | 338.15 | 851.85 |
| 2500.00 | 283.15 | 914.37 |
| 2500.00 | 288.15 | 909.13 |
| 2500.00 | 293.15 | 903.82 |
| 2500.00 | 298.15 | 898.6 |
| 2500.00 | 303.15 | 893.25 |
| 2500.00 | 308.15 | 887.9 |
| 2500.00 | 313.15 | 882.45 |
| 2500.00 | 318.15 | 877.03 |
| 2500.00 | 323.15 | 871.55 |
| 2500.00 | 328.15 | 866.05 |
| 2500.00 | 333.15 | 860.47 |
| 2500.00 | 338.15 | 854.88 |
| 5000.00 | 283.15 | 916.47 |
| 5000.00 | 288.15 | 911.29 |
| 5000.00 | 293.15 | 906.07 |
| 5000.00 | 298.15 | 900.94 |
| 5000.00 | 303.15 | 895.65 |
| 5000.00 | 308.15 | 890.36 |
| 5000.00 | 313.15 | 885.02 |
| 5000.00 | 318.15 | 879.68 |
| 5000.00 | 323.15 | 874.3 |
| 5000.00 | 328.15 | 868.91 |
| 5000.00 | 333.15 | 863.42 |
| 5000.00 | 338.15 | 857.96 |
| 7500.00 | 283.15 | 918.52 |
| 7500.00 | 288.15 | 913.42 |
| 7500.00 | 293.15 | 908.26 |
| 7500.00 | 298.15 | 903.16 |
| 7500.00 | 303.15 | 897.97 |
| 7500.00 | 308.15 | 892.78 |
| 7500.00 | 313.15 | 887.51 |
| 7500.00 | 318.15 | 882.27 |
| 7500.00 | 323.15 | 876.94 |
| 7500.00 | 328.15 | 871.68 |
| 7500.00 | 333.15 | 866.28 |
| 7500.00 | 338.15 | 860.93 |
| 10000.00 | 283.15 | 920.53 |
| 10000.00 | 288.15 | 915.49 |
| 10000.00 | 293.15 | 910.4 |
| 10000.00 | 298.15 | 905.39 |
| 10000.00 | 303.15 | 900.25 |
| 10000.00 | 308.15 | 895.14 |
| 10000.00 | 313.15 | 889.95 |
| 10000.00 | 318.15 | 884.79 |
| 10000.00 | 323.15 | 879.54 |
| 10000.00 | 328.15 | 874.38 |
| 10000.00 | 333.15 | 869.07 |
| 10000.00 | 338.15 | 863.81 |
| 20000.00 | 283.15 | 928.2 |
| 20000.00 | 288.15 | 923.34 |
| 20000.00 | 293.15 | 918.5 |
| 20000.00 | 298.15 | 913.73 |
| 20000.00 | 303.15 | 908.83 |
| 20000.00 | 308.15 | 903.98 |
| 20000.00 | 313.15 | 899.05 |
| 20000.00 | 318.15 | 894.18 |
| 20000.00 | 323.15 | 889.25 |
| 20000.00 | 328.15 | 884.36 |
| 20000.00 | 333.15 | 879.4 |
| 20000.00 | 338.15 | 874.45 |
| 30000.00 | 283.15 | 935.24 |
| 30000.00 | 288.15 | 930.62 |
| 30000.00 | 293.15 | 925.97 |
| 30000.00 | 298.15 | 921.4 |
| 30000.00 | 303.15 | 916.74 |
| 30000.00 | 308.15 | 912.1 |
| 30000.00 | 313.15 | 907.41 |
| 30000.00 | 318.15 | 902.74 |
| 30000.00 | 323.15 | 898.07 |
| 30000.00 | 328.15 | 893.38 |
| 30000.00 | 333.15 | 888.7 |
| 30000.00 | 338.15 | 884.02 |
| 40000.00 | 283.15 | 941.89 |
| 40000.00 | 288.15 | 937.41 |
| 40000.00 | 293.15 | 932.94 |
| 40000.00 | 298.15 | 928.44 |
| 40000.00 | 303.15 | 924.06 |
| 40000.00 | 308.15 | 919.56 |
| 40000.00 | 313.15 | 915.12 |
| 40000.00 | 318.15 | 910.6 |
| 40000.00 | 323.15 | 906.13 |
| 40000.00 | 328.15 | 901.61 |
| 40000.00 | 333.15 | 897.22 |
| 40000.00 | 338.15 | 892.61 |
| 50000.00 | 283.15 | 948.12 |
| 50000.00 | 288.15 | 943.72 |
| 50000.00 | 293.15 | 939.57 |
| 50000.00 | 298.15 | 935.19 |
| 50000.00 | 303.15 | 930.89 |
| 50000.00 | 308.15 | 926.54 |
| 50000.00 | 313.15 | 922.3 |
| 50000.00 | 318.15 | 917.91 |
| 50000.00 | 323.15 | 913.67 |
| 50000.00 | 328.15 | 909.29 |
| 50000.00 | 333.15 | 905.17 |
| 50000.00 | 338.15 | 900.74 |
| 60000.00 | 283.15 | 953.98 |
| 60000.00 | 288.15 | 949.78 |
| 60000.00 | 293.15 | 945.6 |
| 60000.00 | 298.15 | 941.44 |
| 60000.00 | 303.15 | 937.27 |
| 60000.00 | 308.15 | 933.08 |
| 60000.00 | 313.15 | 928.9 |
| 60000.00 | 318.15 | 924.74 |
| 60000.00 | 323.15 | 920.58 |
| 60000.00 | 328.15 | 916.43 |
| 60000.00 | 333.15 | 912.4 |
| 60000.00 | 338.15 | 908.17 |
| 99.00 | 278.15 | 917.53 |
| 99.00 | 280.65 | 914.899 |
| 99.00 | 283.15 | 912.247 |
| 99.00 | 285.65 | 909.614 |
| 99.00 | 288.15 | 906.988 |
| 99.00 | 290.65 | 904.299 |
| 99.00 | 293.15 | 901.636 |
| 99.00 | 295.65 | 898.951 |
| 99.00 | 298.15 | 896.285 |
| 99.00 | 300.65 | 893.569 |
| 99.00 | 303.15 | 890.898 |
| 99.00 | 305.65 | 888.151 |
| 99.00 | 308.15 | 885.447 |
| 99.00 | 310.65 | 882.693 |
| 99.00 | 313.15 | 879.927 |
| 99.00 | 315.65 | 877.195 |
| 99.00 | 318.15 | 874.437 |
| 99.00 | 320.65 | 871.651 |
| 99.00 | 323.15 | 868.85 |
| 99.00 | 325.65 | 866.06 |
| 99.00 | 328.15 | 863.248 |
| 99.00 | 330.65 | 860.418 |
| 99.00 | 333.15 | 857.577 |
| 99.00 | 335.65 | 854.721 |
| 99.00 | 338.15 | 851.85 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [270.42; 390.63] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.48188e+01 | |||
| Coefficient B | -3.30555e+03 | |||
| Coefficient C | -4.29400e+01 | |||
| Temperature range, min. | 270.42 | |||
| Temperature range, max. | 390.63 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
| Pvap | 1.33 | kPa | 270.42 | Calculated Property |
| Pvap | 2.98 | kPa | 283.78 | Calculated Property |
| Pvap | 6.14 | kPa | 297.13 | Calculated Property |
| Pvap | 11.75 | kPa | 310.49 | Calculated Property |
| Pvap | 21.14 | kPa | 323.85 | Calculated Property |
| Pvap | 36.07 | kPa | 337.20 | Calculated Property |
| Pvap | 58.74 | kPa | 350.56 | Calculated Property |
| Pvap | 91.87 | kPa | 363.92 | Calculated Property |
| Pvap | 138.62 | kPa | 377.27 | Calculated Property |
| Pvap | 202.67 | kPa | 390.63 | Calculated Property |
Similar Compounds
![2-methyl-5-[(methylthio)methyl]furan.](data:image/png;base64,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)
Find more compounds similar to Furan, 2,5-dimethyl-.
Mixtures
- Diisopropyl ether + Furan, 2,5-dimethyl-
- 2-Furanmethanol + Furan, 2,5-dimethyl-
- Methyl Isobutyl Ketone + Furan, 2,5-dimethyl-
- n-Hexane + Furan, 2,5-dimethyl-
- Ethanol + Furan, 2,5-dimethyl-
Sources
- Crippen Method
- Crippen Method
- Isobaric vapor liquid equilibrium and isothermal surface tensions of 2,2 -oxybis[propane] + 2,5-Dimethylfuran
- Measurement and modeling of infinite dilution activity coefficients of organic compounds in an equimolar ionic liquid mixture of [Bmim]Cl and [Bmim][Tf2N]
- Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
- Thermophysical study of the furan family
- Vapor Liquid Equilibrium, Densities, and Interfacial Tensions of the System Hexane + 2,5-Dimethylfuran
- Isobaric Vapor Liquid Equilibrium and Isothermal Interfacial Tensions for the System Ethanol + 2,5-Dimethylfuran
- 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.