- InChI
- InChI=1S/C5H10O/c1-5-3-2-4-6-5/h5H,2-4H2,1H3
- InChI Key
- JWUJQDFVADABEY-UHFFFAOYSA-N
- Formula
- C5H10O
- SMILES
- CC1CCCO1
- Molecular Weight1
- 86.13
- CAS
- 96-47-9
- Other Names
-
- .alpha.-methyltetramethylene oxide
- 2-Methylfuranidine
- 2-Methyloxolane
- 2-Methyltetrahydrofuran
- 2-Methyltetrahydrofurane
- Furan, 2-methyl-tetrahydro-
- Methyltetrahydrofuran
- Tetrahydro-2-methylfuran
- Tetrahydrofuran, 2-methyl-
- Tetrahydrosylvan
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : 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).
- IE : Ionization energy (eV).
- ν : Kinematic viscosity (m2/s).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- 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.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | 840.80 | kJ/mol | NIST |
| BasG | 811.60 | kJ/mol | NIST |
| ΔfG° | -58.35 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -218.05 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 10.62 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [33.70; 34.00] | kJ/mol |
|
| ΔvapH° | 34.00 | kJ/mol | NIST |
| ΔvapH° | 33.70 | kJ/mol | NIST |
| IE | 9.22 ± 0.05 | eV | NIST |
| log10WS | [0.11; 0.11] |
|
|
| log10WS | 0.11 | Aq. Sol... | |
| log10WS | 0.11 | Estimat... | |
| logPoct/wat | 1.185 | Crippen Calculated Property | |
| McVol | 76.320 | ml/mol | McGowan Calculated Property |
| Pc | 3757.63 ± 68.94 | kPa | NIST |
| Inp | [661.00; 682.00] |
|
|
| Inp | 661.00 | NIST | |
| Inp | 669.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 678.00 | NIST | |
| Inp | 663.00 | NIST | |
| Inp | 674.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 663.00 | NIST | |
| I | [876.00; 951.00] |
|
|
| I | 925.00 | NIST | |
| I | 935.00 | NIST | |
| I | 876.00 | NIST | |
| I | 876.00 | NIST | |
| I | 951.00 | NIST | |
| I | 925.00 | NIST | |
| Tboil | [338.15; 359.65] | K |
|
| Tboil | 353.20 | K | NIST |
| Tboil | 352.65 ± 2.00 | K | NIST |
| Tboil | 353.10 ± 0.30 | K | NIST |
| Tboil | 353.15 ± 1.00 | K | NIST |
| Tboil | 359.65 ± 1.00 | K | NIST |
| Tboil | Outlier 338.15 ± 2.00 | K | NIST |
| Tc | 537.00 ± 2.00 | K | NIST |
| Tfus | 137.05 ± 0.40 | K | NIST |
| Vc | 0.267 ± 0.005 | m3/kmol | NIST |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [129.20; 194.00] | J/mol×K | [356.03; 553.34] |
|
| Cp,gas | 129.20 | J/mol×K | 356.03 | Joback Calculated Property |
| Cp,gas | 141.40 | J/mol×K | 388.92 | Joback Calculated Property |
| Cp,gas | 153.02 | J/mol×K | 421.80 | Joback Calculated Property |
| Cp,gas | 164.07 | J/mol×K | 454.69 | Joback Calculated Property |
| Cp,gas | 174.57 | J/mol×K | 487.57 | Joback Calculated Property |
| Cp,gas | 184.54 | J/mol×K | 520.46 | Joback Calculated Property |
| Cp,gas | 194.00 | J/mol×K | 553.34 | Joback Calculated Property |
| Cp,liquid | [153.50; 166.20] | J/mol×K | [288.15; 323.15] |
|
| Cp,liquid | 153.50 | J/mol×K | 288.15 | Molar H... |
| Cp,liquid | 155.30 | J/mol×K | 293.15 | Molar H... |
| Cp,liquid | 155.30 | J/mol×K | 293.15 | Molar H... |
| Cp,liquid | 156.90 | J/mol×K | 298.15 | Molar H... |
| Cp,liquid | 158.70 | J/mol×K | 303.15 | Molar H... |
| Cp,liquid | 158.60 | J/mol×K | 303.15 | Molar H... |
| Cp,liquid | 160.20 | J/mol×K | 308.15 | Molar H... |
| Cp,liquid | 162.10 | J/mol×K | 313.15 | Molar H... |
| Cp,liquid | 162.10 | J/mol×K | 313.15 | Molar H... |
| Cp,liquid | 164.20 | J/mol×K | 318.15 | Molar H... |
| Cp,liquid | 166.20 | J/mol×K | 323.15 | Molar H... |
| η | [0.0004088; 0.0005618] | Pa×s | [283.15; 313.15] |
|
| η | 0.0005618 | Pa×s | 283.15 | Excess ... |
| η | 0.0004776 | Pa×s | 298.15 | Excess ... |
| η | 0.0004088 | Pa×s | 313.15 | Excess ... |
| ν | [0.0000005; 0.0000006] | m2/s | [298.15; 313.15] |
|
| ν | 0.0000006 | m2/s | 298.15 | Viscosi... |
| ν | 0.0000005 | m2/s | 313.15 | Viscosi... |
| Pvap | [4.93; 21.69] | kPa | [279.00; 310.11] |
|
| Pvap | 4.93 | kPa | 279.00 | Vapor P... |
| Pvap | 4.93 | kPa | 279.01 | Vapor P... |
| Pvap | 5.60 | kPa | 281.41 | Vapor P... |
| Pvap | 5.63 | kPa | 281.44 | Vapor P... |
| Pvap | 6.57 | kPa | 284.34 | Vapor P... |
| Pvap | 7.83 | kPa | 287.83 | Vapor P... |
| Pvap | 7.85 | kPa | 287.84 | Vapor P... |
| Pvap | 9.26 | kPa | 291.17 | Vapor P... |
| Pvap | 11.65 | kPa | 295.94 | Vapor P... |
| Pvap | 13.37 | kPa | 298.94 | Vapor P... |
| Pvap | 15.76 | kPa | 302.62 | Vapor P... |
| Pvap | 18.28 | kPa | 306.05 | Vapor P... |
| Pvap | 21.69 | kPa | 310.11 | Vapor P... |
| n0 | [1.40280; 1.40299] | [298.00; 298.15] |
|
|
| n0 | 1.40299 | 298.00 | Quatern... | |
| n0 | 1.40280 | 298.15 | Ternary... | |
| n0 | 1.40287 | 298.15 | Thermop... | |
| ρl | [848.10; 855.00] | kg/m3 | [293.15; 298.15] |
|
| ρl | 855.00 | kg/m3 | 293.15 | Isother... |
| ρl | 851.60 | kg/m3 | 295.00 | High-pr... |
| ρl | 848.10 | kg/m3 | 298.15 | Excess ... |
| ρl | 848.10 | kg/m3 | 298.15 | Excess ... |
| ρl | 848.10 | kg/m3 | 298.15 | Excess ... |
| ρl | 849.20 | kg/m3 | 298.15 | Thermod... |
| ρl | 849.40 | kg/m3 | 298.15 | Study o... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [258.70; 374.84] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.47976e+01 | |||
| Coefficient B | -3.18218e+03 | |||
| Coefficient C | -3.93870e+01 | |||
| Temperature range, min. | 258.70 | |||
| Temperature range, max. | 374.84 | |||
| Pvap | 1.33 | kPa | 258.70 | Calculated Property |
| Pvap | 2.99 | kPa | 271.60 | Calculated Property |
| Pvap | 6.14 | kPa | 284.51 | Calculated Property |
| Pvap | 11.76 | kPa | 297.41 | Calculated Property |
| Pvap | 21.16 | kPa | 310.32 | Calculated Property |
| Pvap | 36.10 | kPa | 323.22 | Calculated Property |
| Pvap | 58.78 | kPa | 336.13 | Calculated Property |
| Pvap | 91.90 | kPa | 349.03 | Calculated Property |
| Pvap | 138.64 | kPa | 361.94 | Calculated Property |
| Pvap | 202.64 | kPa | 374.84 | Calculated Property |
Similar Compounds
![7-Oxabicyclo[2.2.1]heptane.](data:image/png;base64,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)
Find more compounds similar to Furan, tetrahydro-2-methyl-.
Mixtures
- n-Butyl ether + Furan, tetrahydro-2-methyl-
- Propane, 2-methoxy-2-methyl- + Furan, tetrahydro-2-methyl-
- Dodecane + Propane, 2-methoxy-2-methyl- + Furan, tetrahydro-2-methyl-
- Octane + Propane, 2-methoxy-2-methyl- + Furan, tetrahydro-2-methyl-
- 1-Hexene + Propane, 2-methoxy-2-methyl- + Furan, tetrahydro-2-methyl-
- Water + Furan, tetrahydro-2-methyl-
- Furfural + Water + Furan, tetrahydro-2-methyl-
- Acetic acid + Water + Furan, tetrahydro-2-methyl-
- Butane, 2-chloro- + Furan, tetrahydro-2-methyl-
- Propane, 1-chloro-2-methyl- + Furan, tetrahydro-2-methyl-
- Butane, 1-chloro- + Furan, tetrahydro-2-methyl-
- Propane, 2-chloro-2-methyl- + Furan, tetrahydro-2-methyl-
- Benzene, fluoro- + Furan, tetrahydro-2-methyl-
- Benzene, chloro- + Furan, tetrahydro-2-methyl-
- Benzene + Furan, tetrahydro-2-methyl-
- Propene, hexafluoro- + Furan, tetrahydro-2-methyl-
- 1-Butanol + Furan, tetrahydro-2-methyl-
- 1-Propanol, 2-methyl- + Furan, tetrahydro-2-methyl-
- 2-Propanol, 2-methyl- + Furan, tetrahydro-2-methyl-
- Cyclohexane, chloro- + Furan, tetrahydro-2-methyl-
Find more mixtures with Furan, tetrahydro-2-methyl-.
Sources
- Crippen Method
- High-pressure vapor-liquid equilibria of the second generation biofuel blends (2-methylfuran + iso-octane) and (2-methyltetrahydrofuran + di-n-butyl ether): Experiments and PCP-SAFT modeling
- Liquid-liquid equilibrium of 2-methyltetrahydrofuran/water over wide temperature range: Measurements and rigorous regression
- Excess molar enthalpies of the ternary mixtures: (methyl tert-butyl ether or 2-methyltetrahydrofuran + cyclohexane + 2,2,4- trimethylpentane} at the temperature 298.15 K
- Excess molar enthalpies of the ternary mixtures: {tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether + n-dodecane} at the temperature 298.15 K
- Excess molar enthalpies of the ternary mixtures: (tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether + n-octane) at the temperature 298.15 K
- Excess molar enthalpies of the ternary mixtures (1-hexene + tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether) at the temperature 298.15K.
- Ternary and binary LLE measurements for solvent (2-methyltetrahydrofuran and cyclopentyl methyl ether) + furfural + water between 298 and 343 K
- Quaternary and ternary LLE measurements for solvent (2-methyltetrahydrofuran and cyclopentyl methyl ether) + furfural + acetic acid + water between 298 and 343 K
- Thermodynamic study of 2-methyl-tetrahydrofuran with isomeric chlorobutanes
- Thermophysical properties of the binary mixtures of 2-methyl-tetrahydrofuran with benzene and halobenzenes
- Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
- Solubility Measurement and Thermodynamic Modeling of N-(4-Methylphenyl-Z-3-chloro-2-(phenylthio)propenamide in 12 Pure Solvents at Temperatures Ranging from 278.15 to 318.15 K
- Isothermal Vapor-Liquid Equilibrium Data for the Binary Systems Consisting of 1,1,2,3,3,3-Hexafluoro-1-propene and Either Methylcyclohexane, Cyclohexane, n-Hexane, 2-Methyltetrahydrofuran, or 2,2,3,3,4,4,4-Heptafluoro-1-butanol
- Viscosities of Binary Mixtures of Isomeric Butanols or Isomeric Chlorobutanes with 2-Methyltetrahydrofuran
- Study of the Surface Tension of Chlorocyclohexane or Bromocyclohexane with Some Cyclic Ethers
- Excess Enthalpy, Density, Speed of Sound, and Viscosity for 2-Methyltetrahydrofuran + 1-Butanol at (283.15, 298.15, and, 313.15) K
- Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Tetrahydropyran and + 2-Methyltetrahydrofuran at (293.15, 303.15, and 313.15) K
- Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Poly(ethylene glycols) + 2-Methyltetrahydrofuran at (293.15, 303.15, and 313.15) K
- Joback Method
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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Outlier This icon means
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