- InChI
- InChI=1S/C10H22/c1-4-6-7-9-10(3)8-5-2/h10H,4-9H2,1-3H3
- InChI Key
- IALRSQMWHFKJJA-UHFFFAOYSA-N
- Formula
- C10H22
- SMILES
- CCCCCC(C)CCC
- Molecular Weight1
- 142.28
- CAS
- 17301-94-9
- Other Names
-
- 4-Methylnonane
- 4-Methylnonane, (DL)-
- n-C3H7CH(CH3)(CH2)4CH3
- ω : Acentric Factor.
- AP : Aniline Point (K).
- 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).
- 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 | 0.4510 | KDB | |
| AP | 351.450 | K | KDB |
| ΔfG° | 30.88 | kJ/mol | Joback Calculated Property |
| Δc,grossH | 6775.57 | kJ/mol | KDB |
| Δc,netH | 6291.439 | kJ/mol | KDB |
| ΔfH°gas | -255.01 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 18.13 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 49.50 | 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 | 2140.00 | kPa | KDB |
| Inp | [955.00; 972.00] |
|
|
| Inp | 960.00 | NIST | |
| Inp | Outlier 972.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | Outlier 970.00 | NIST | |
| Inp | Outlier 970.00 | NIST | |
| Inp | 962.50 | NIST | |
| Inp | 962.40 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 959.30 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 960.80 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 960.63 | NIST | |
| Inp | 960.63 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 962.40 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | Outlier 955.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 967.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 963.80 | NIST | |
| Inp | 962.10 | NIST | |
| Inp | 961.60 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 963.54 | NIST | |
| Inp | 963.12 | NIST | |
| Inp | 963.33 | NIST | |
| Inp | 963.34 | NIST | |
| Inp | 962.48 | NIST | |
| Inp | 962.63 | NIST | |
| Inp | 962.67 | NIST | |
| Inp | Outlier 955.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 962.80 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 962.00 | NIST | |
| S°liquid | 425.50 | J/mol×K | NIST |
| Tboil | [438.85; 442.15] | K |
|
| Tboil | 438.90 | K | KDB |
| Tboil | 441.15 ± 2.00 | K | NIST |
| Tboil | 438.85 ± 0.50 | K | NIST |
| Tboil | 438.90 ± 0.50 | K | NIST |
| Tboil | 442.15 ± 2.00 | K | NIST |
| Tboil | 438.90 ± 0.50 | K | NIST |
| Tboil | 438.90 ± 0.30 | K | NIST |
| Tc | 610.50 | K | KDB |
| Tfus | [171.53; 174.69] | K |
|
| Tfus | 174.00 | K | KDB |
| Tfus | 174.69 ± 0.20 | K | NIST |
| Tfus | 171.53 ± 0.15 | K | NIST |
| Ttriple | 174.70 ± 0.20 | K | NIST |
| Vc | 0.575 | m3/kmol | KDB |
| Zc | 0.2424150 | 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 | 317.36 | 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 | [15.19; 15.19] | kJ/mol | [174.70; 174.70] |
|
| ΔfusH | 15.19 | kJ/mol | 174.70 | NIST |
| ΔfusH | 15.19 | kJ/mol | 174.70 | NIST |
| ΔvapH | 38.79 | kJ/mol | 438.90 | KDB |
| n0 | 1.40950 | 298.15 | KDB | |
| ρl | [626.00; 739.36] | kg/m3 | [283.15; 423.15] |
|
|
T(K) Liquid Density (kg/m3) 620 640 660 680 700 720 740 300 350 400 | ||||
| ρl | 739.36 | kg/m3 | 283.15 | Viscosi... |
| ρl | 735.55 | kg/m3 | 288.15 | Viscosi... |
| ρl | 731.74 | kg/m3 | 293.15 | Viscosi... |
| ρl | 727.93 | kg/m3 | 298.15 | Viscosi... |
| ρl | 728.35 | kg/m3 | 298.15 | Viscosi... |
| ρl | 724.10 | kg/m3 | 303.15 | Viscosi... |
| ρl | 720.25 | kg/m3 | 308.15 | Viscosi... |
| ρl | 716.40 | kg/m3 | 313.15 | Viscosi... |
| ρl | 712.53 | kg/m3 | 318.15 | Viscosi... |
| ρl | 708.63 | kg/m3 | 323.15 | Viscosi... |
| ρl | 708.82 | kg/m3 | 323.15 | Viscosi... |
| ρl | 704.73 | kg/m3 | 328.15 | Viscosi... |
| ρl | 700.81 | kg/m3 | 333.15 | Viscosi... |
| ρl | 696.87 | kg/m3 | 338.15 | Viscosi... |
| ρl | 692.92 | kg/m3 | 343.15 | Viscosi... |
| ρl | 688.94 | kg/m3 | 348.15 | Viscosi... |
| ρl | 689.00 | kg/m3 | 348.15 | Viscosi... |
| ρl | 684.94 | kg/m3 | 353.15 | Viscosi... |
| ρl | 680.92 | kg/m3 | 358.15 | Viscosi... |
| ρl | 676.88 | kg/m3 | 363.15 | Viscosi... |
| ρl | 668.81 | kg/m3 | 373.15 | Viscosi... |
| ρl | 647.86 | kg/m3 | 398.15 | Viscosi... |
| ρl | 626.00 | kg/m3 | 423.15 | Viscosi... |
| ΔfusS | 86.94 | J/mol×K | 174.70 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [320.68; 467.87] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.47150e+01 | |||
| Coefficient B | -3.97462e+03 | |||
| Coefficient C | -4.51930e+01 | |||
| Temperature range, min. | 320.68 | |||
| Temperature range, max. | 467.87 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 320.68 | Calculated Property |
| Pvap | 2.99 | kPa | 337.03 | Calculated Property |
| Pvap | 6.16 | kPa | 353.39 | Calculated Property |
| Pvap | 11.80 | kPa | 369.74 | Calculated Property |
| Pvap | 21.24 | kPa | 386.10 | Calculated Property |
| Pvap | 36.22 | kPa | 402.45 | Calculated Property |
| Pvap | 58.95 | kPa | 418.81 | Calculated Property |
| Pvap | 92.10 | kPa | 435.16 | Calculated Property |
| Pvap | 138.80 | kPa | 451.52 | Calculated Property |
| Pvap | 202.66 | kPa | 467.87 | Calculated Property |
| Pvap | [1.05e-07; 2093.44] | kPa | [174.45; 610.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.38814e+01 | |||
| Coefficient B | -8.08283e+03 | |||
| Coefficient C | -8.47077e+00 | |||
| Coefficient D | 3.60829e-06 | |||
| Temperature range, min. | 174.45 | |||
| Temperature range, max. | 610.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 200 400 600 | ||||
| Pvap | 1.05e-07 | kPa | 174.45 | Calculated Property |
| Pvap | 3.33e-04 | kPa | 222.84 | Calculated Property |
| Pvap | 0.04 | kPa | 271.24 | Calculated Property |
| Pvap | 1.12 | kPa | 319.63 | Calculated Property |
| Pvap | 10.60 | kPa | 368.03 | Calculated Property |
| Pvap | 54.80 | kPa | 416.42 | Calculated Property |
| Pvap | 190.04 | kPa | 464.82 | Calculated Property |
| Pvap | 502.11 | kPa | 513.21 | Calculated Property |
| Pvap | 1097.01 | kPa | 561.61 | Calculated Property |
| Pvap | 2093.44 | kPa | 610.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Nonane, 4-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
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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