- InChI
- InChI=1S/C10H22/c1-4-5-6-7-8-9-10(2)3/h10H,4-9H2,1-3H3
- InChI Key
- SGVYKUFIHHTIFL-UHFFFAOYSA-N
- Formula
- C10H22
- SMILES
- CCCCCCCC(C)C
- Molecular Weight1
- 142.28
- CAS
- 871-83-0
- Other Names
-
- 2-Methylnonane
- ω : Acentric Factor.
- AP : Aniline Point (K).
- ΔcH°liquid : Standard liquid enthalpy of combustion (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).
- Δc,grossH : Heat of Combustion, Gross form (kJ/mol).
- Δc,netH : Heat of Combustion, Net Form (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 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).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-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).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.4590 | KDB | |
| AP | 353.450 | K | KDB |
| ΔcH°liquid | -6769.50 ± 2.30 | kJ/mol | NIST |
| ΔfG° | 30.88 | kJ/mol | Joback Calculated Property |
| Δc,grossH | 6772.98 | kJ/mol | KDB |
| Δc,netH | 6288.845 | kJ/mol | KDB |
| ΔfH°gas | -260.20 | kJ/mol | NIST |
| ΔfH°liquid | -309.80 ± 2.40 | kJ/mol | NIST |
| ΔfusH° | 18.13 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [49.64; 51.00] | kJ/mol |
|
| ΔvapH° | 49.64 | kJ/mol | NIST |
| ΔvapH° | 51.00 | kJ/mol | NIST |
| log10WS | -3.77 | Crippen Calculated Property | |
| logPoct/wat | 4.003 | Crippen Calculated Property | |
| McVol | 151.760 | ml/mol | McGowan Calculated Property |
| Pc | 2100.00 | kPa | KDB |
| Inp | [962.00; 987.00] |
|
|
| Inp | 964.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | Outlier 976.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 965.20 | NIST | |
| Inp | 965.10 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 963.90 | NIST | |
| Inp | 964.70 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 967.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 964.43 | NIST | |
| Inp | 964.43 | NIST | |
| Inp | 963.80 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 971.70 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 966.20 | NIST | |
| Inp | 962.60 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 964.80 | NIST | |
| Inp | 968.60 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 965.96 | NIST | |
| Inp | 966.07 | NIST | |
| Inp | 966.05 | NIST | |
| Inp | 965.23 | NIST | |
| Inp | 965.28 | NIST | |
| Inp | 965.28 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | Outlier 980.70 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 965.40 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | Outlier 987.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 973.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 965.20 | NIST | |
| Inp | 964.43 | NIST | |
| Inp | 971.70 | NIST | |
| S°liquid | 420.10 | J/mol×K | NIST |
| Tboil | [440.00; 440.20] | K |
|
| Tboil | 440.20 | K | KDB |
| Tboil | 440.00 | K | NIST |
| Tboil | 440.20 | K | NIST |
| Tboil | 440.15 ± 0.15 | K | NIST |
| Tboil | 440.00 ± 0.30 | K | NIST |
| Tc | [610.30; 610.70] | K |
|
| Tc | 610.30 | K | KDB |
| Tc | 610.70 | K | NIST |
| Tfus | [198.79; 201.50] | K |
|
| Tfus | 199.00 | K | KDB |
| Tfus | 201.50 ± 0.15 | K | NIST |
| Tfus | 198.79 ± 0.20 | K | NIST |
| Ttriple | 198.80 ± 0.20 | K | NIST |
| Vc | 0.596 | m3/kmol | KDB |
| Zc | 0.2466530 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [315.29; 399.91] | J/mol×K | [427.76; 593.73] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 320 340 360 380 400 450 500 550 | ||||
| Cp,gas | 315.29 | J/mol×K | 427.76 | Joback Calculated Property |
| Cp,gas | 330.79 | J/mol×K | 455.42 | Joback Calculated Property |
| Cp,gas | 345.71 | J/mol×K | 483.08 | Joback Calculated Property |
| Cp,gas | 360.07 | J/mol×K | 510.75 | Joback Calculated Property |
| Cp,gas | 373.88 | J/mol×K | 538.41 | Joback Calculated Property |
| Cp,gas | 387.16 | J/mol×K | 566.07 | Joback Calculated Property |
| Cp,gas | 399.91 | J/mol×K | 593.73 | Joback Calculated Property |
| Cp,liquid | 313.30 | J/mol×K | 298.10 | NIST |
| η | [0.0002265; 0.0108083] | Pa×s | [187.46; 427.76] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 2.00e-3 4.00e-3 6.00e-3 8.00e-3 0.01 200 300 400 | ||||
| η | 0.0108083 | Pa×s | 187.46 | Joback Calculated Property |
| η | 0.0032190 | Pa×s | 227.51 | Joback Calculated Property |
| η | 0.0013777 | Pa×s | 267.56 | Joback Calculated Property |
| η | 0.0007355 | Pa×s | 307.61 | Joback Calculated Property |
| η | 0.0004537 | Pa×s | 347.66 | Joback Calculated Property |
| η | 0.0003093 | Pa×s | 387.71 | Joback Calculated Property |
| η | 0.0002265 | Pa×s | 427.76 | Joback Calculated Property |
| ΔfusH | [17.49; 17.49] | kJ/mol | [198.80; 198.80] |
|
| ΔfusH | 17.49 | kJ/mol | 198.80 | NIST |
| ΔfusH | 17.49 | kJ/mol | 198.80 | NIST |
| ΔfusH | 17.49 | kJ/mol | 198.80 | NIST |
| ΔvapH | [38.23; 47.30] | kJ/mol | [328.00; 440.20] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 38 40 42 44 46 48 350 400 | ||||
| ΔvapH | 47.30 ± 0.20 | kJ/mol | 328.00 | NIST |
| ΔvapH | 46.20 ± 0.20 | kJ/mol | 343.00 | NIST |
| ΔvapH | 45.00 ± 0.20 | kJ/mol | 358.00 | NIST |
| ΔvapH | 46.40 ± 0.20 | kJ/mol | 382.50 | NIST |
| ΔvapH | 39.20 | kJ/mol | 440.20 | KDB |
| ΔvapH | 38.23 | kJ/mol | 440.20 | NIST |
| n0 | 1.40750 | 298.15 | KDB | |
| ρl | [621.59; 735.13] | kg/m3 | [283.15; 423.15] |
|
|
T(K) Liquid Density (kg/m3) 620 640 660 680 700 720 740 300 350 400 | ||||
| ρl | 734.70 | kg/m3 | 283.15 | Density... |
| ρl | 734.50 | kg/m3 | 283.15 | Density... |
| ρl | 735.13 | kg/m3 | 283.15 | Viscosi... |
| ρl | 731.33 | kg/m3 | 288.15 | Viscosi... |
| ρl | 727.47 | kg/m3 | 293.15 | Viscosi... |
| ρl | 727.10 | kg/m3 | 293.15 | Density... |
| ρl | 726.90 | kg/m3 | 293.15 | Density... |
| ρl | 723.54 | kg/m3 | 298.15 | Viscosi... |
| ρl | 723.63 | kg/m3 | 298.15 | Viscosi... |
| ρl | 719.40 | kg/m3 | 303.15 | Density... |
| ρl | 719.96 | kg/m3 | 303.15 | Viscosi... |
| ρl | 719.30 | kg/m3 | 303.15 | Density... |
| ρl | 716.11 | kg/m3 | 308.15 | Viscosi... |
| ρl | 712.27 | kg/m3 | 313.15 | Viscosi... |
| ρl | 711.70 | kg/m3 | 313.15 | Density... |
| ρl | 711.60 | kg/m3 | 313.15 | Density... |
| ρl | 708.49 | kg/m3 | 318.15 | Viscosi... |
| ρl | 704.63 | kg/m3 | 323.15 | Viscosi... |
| ρl | 704.14 | kg/m3 | 323.15 | Viscosi... |
| ρl | 703.90 | kg/m3 | 323.15 | Density... |
| ρl | 703.90 | kg/m3 | 323.15 | Density... |
| ρl | 700.72 | kg/m3 | 328.15 | Viscosi... |
| ρl | 696.00 | kg/m3 | 333.15 | Density... |
| ρl | 696.79 | kg/m3 | 333.15 | Viscosi... |
| ρl | 692.85 | kg/m3 | 338.15 | Viscosi... |
| ρl | 688.88 | kg/m3 | 343.15 | Viscosi... |
| ρl | 688.10 | kg/m3 | 343.15 | Density... |
| ρl | 684.90 | kg/m3 | 348.15 | Viscosi... |
| ρl | 684.45 | kg/m3 | 348.15 | Viscosi... |
| ρl | 680.89 | kg/m3 | 353.15 | Viscosi... |
| ρl | 680.20 | kg/m3 | 353.15 | Density... |
| ρl | 676.83 | kg/m3 | 358.15 | Viscosi... |
| ρl | 672.10 | kg/m3 | 363.15 | Density... |
| ρl | 672.81 | kg/m3 | 363.15 | Viscosi... |
| ρl | 664.00 | kg/m3 | 373.15 | Density... |
| ρl | 664.34 | kg/m3 | 373.15 | Viscosi... |
| ρl | 643.46 | kg/m3 | 398.15 | Viscosi... |
| ρl | 621.59 | kg/m3 | 423.15 | Viscosi... |
| ΔfusS | 87.97 | J/mol×K | 198.80 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [324.60; 468.87] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.44006e+01 | |||
| Coefficient B | -3.68356e+03 | |||
| Coefficient C | -6.35970e+01 | |||
| Temperature range, min. | 324.60 | |||
| Temperature range, max. | 468.87 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 324.60 | Calculated Property |
| Pvap | 3.02 | kPa | 340.63 | Calculated Property |
| Pvap | 6.24 | kPa | 356.66 | Calculated Property |
| Pvap | 11.98 | kPa | 372.69 | Calculated Property |
| Pvap | 21.56 | kPa | 388.72 | Calculated Property |
| Pvap | 36.72 | kPa | 404.75 | Calculated Property |
| Pvap | 59.61 | kPa | 420.78 | Calculated Property |
| Pvap | 92.83 | kPa | 436.81 | Calculated Property |
| Pvap | 139.39 | kPa | 452.84 | Calculated Property |
| Pvap | 202.66 | kPa | 468.87 | Calculated Property |
| Pvap | [2.49e-06; 2121.01] | kPa | [198.50; 610.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.28452e+02 | |||
| Coefficient B | -1.05839e+04 | |||
| Coefficient C | -1.67146e+01 | |||
| Coefficient D | 1.00957e-05 | |||
| Temperature range, min. | 198.50 | |||
| Temperature range, max. | 610.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 200 400 600 | ||||
| Pvap | 2.49e-06 | kPa | 198.50 | Calculated Property |
| Pvap | 2.07e-03 | kPa | 244.22 | Calculated Property |
| Pvap | 0.14 | kPa | 289.94 | Calculated Property |
| Pvap | 2.33 | kPa | 335.67 | Calculated Property |
| Pvap | 16.80 | kPa | 381.39 | Calculated Property |
| Pvap | 71.70 | kPa | 427.11 | Calculated Property |
| Pvap | 217.96 | kPa | 472.83 | Calculated Property |
| Pvap | 529.93 | kPa | 518.56 | Calculated Property |
| Pvap | 1112.09 | kPa | 564.28 | Calculated Property |
| Pvap | 2121.01 | kPa | 610.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Nonane, 2-methyl-.
Mixtures
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
- Liquid Viscosity and Interfacial Tension of Binary and Ternary Mixtures Containing n-Octacosane by Surface Light Scattering
- Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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