- InChI
- InChI=1S/C9H20/c1-4-6-7-8-9(3)5-2/h9H,4-8H2,1-3H3
- InChI Key
- SEEOMASXHIJCDV-UHFFFAOYSA-N
- Formula
- C9H20
- SMILES
- CCCCCC(C)CC
- Molecular Weight1
- 128.26
- CAS
- 2216-33-3
- Other Names
-
- 3-Methyloctane
- Isononane
- 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).
- μ : Dipole Moment (debye).
- 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).
- 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).
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.4123; 0.4130] |
|
|
| ω | 0.4123 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.4130 | KDB | |
| AP | 348.150 | K | KDB |
| μ | 0.00 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | 21.70 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| Δc,grossH | 6121.40 | kJ/mol | KDB |
| Δc,netH | 5681.286 | kJ/mol | KDB |
| ΔfH°gas | -233.60 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfusH° | 15.54 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 44.90 | kJ/mol | NIST |
| IE | 9.62 | eV | Relay (1.0) Calculated Property |
| log10WS | -5.42 | Relay (1.0) Calculated Property | |
| logPoct/wat | 3.613 | Crippen Calculated Property | |
| McVol | 137.670 | ml/mol | McGowan Calculated Property |
| Pc | [2340.00; 2340.00] | kPa |
|
| Pc | 2340.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 2340.00 | kPa | KDB |
| Ptriple | 8.99e-08 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [862.00; 880.00] |
|
|
| Inp | 874.00 | NIST | |
| Inp | 872.10 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 869.90 | NIST | |
| Inp | 870.50 | NIST | |
| Inp | 872.20 | NIST | |
| Inp | 872.30 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 871.70 | NIST | |
| Inp | 871.90 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 870.80 | NIST | |
| Inp | 871.10 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 871.10 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | Outlier 862.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 871.93 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 873.50 | NIST | |
| Inp | 871.40 | NIST | |
| Inp | 871.40 | NIST | |
| Inp | Outlier 863.40 | NIST | |
| Inp | 869.60 | NIST | |
| Inp | 870.74 | NIST | |
| Inp | 870.98 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 872.35 | NIST | |
| Inp | 872.61 | NIST | |
| Inp | 872.89 | NIST | |
| Inp | 871.93 | NIST | |
| Inp | 872.24 | NIST | |
| Inp | 872.56 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 871.90 | NIST | |
| Inp | 873.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | Outlier 880.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 873.50 | NIST | |
| Inp | 870.74 | NIST | |
| Inp | 872.61 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 872.10 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 871.10 | NIST | |
| Inp | Outlier 862.00 | NIST | |
| Tboil | [415.75; 417.40] | K |
|
| Tboil | 417.38 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 417.40 | K | KDB |
| Tboil | 416.00 ± 3.00 | K | NIST |
| Tboil | 417.36 ± 0.20 | K | NIST |
| Tboil | 417.33 ± 0.50 | K | NIST |
| Tboil | 417.40 ± 0.30 | K | NIST |
| Tboil | 417.40 ± 0.30 | K | NIST |
| Tboil | 417.33 ± 0.20 | K | NIST |
| Tboil | Outlier 415.75 ± 0.50 | K | NIST |
| Tboil | 417.33 ± 0.15 | K | NIST |
| Tboil | 416.55 ± 0.70 | K | NIST |
| Tboil | 416.55 ± 0.30 | K | NIST |
| Tboil | 416.55 ± 0.30 | K | NIST |
| Tboil | 416.65 ± 1.50 | K | NIST |
| Tc | [590.00; 590.15] | K |
|
| Tc | 590.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 590.00 | K | KDB |
| Tfus | [165.15; 166.00] | K |
|
| Tfus | 165.35 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 165.55 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 166.00 | K | KDB |
| Tfus | 165.15 ± 0.10 | K | NIST |
| Ttriple | 165.55 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 5.47 | ChemSep v8.3 pure component data Compiled value | |
| URi | 6.52 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.529; 0.529] | m3/kmol |
|
| Vc | 0.529 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.529 | m3/kmol | KDB |
| Zc | [0.2520000; 0.2523380] |
|
|
| Zc | 0.2520000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2523380 | KDB | |
| Zra | 0.25 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔfusH | 16.99 | kJ/mol | 165.60 | NIST |
| ΔvapH | 36.78 | kJ/mol | 417.40 | KDB |
| n0 | 1.40400 | 298.15 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [131.21; 563.59] | J/mol×K | [150.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 1.18620e+02 | |||
| Coefficient B | -5.96810e+02 | |||
| Coefficient C | 6.51024e+00 | |||
| Coefficient D | 8.82830e-06 | |||
| Coefficient E | -1.22710e-08 | |||
| Temperature range, min. | 150.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 131.21 | J/mol×K | 150.00 | Calculated Property |
| Cp,gas | 210.68 | J/mol×K | 300.00 | Calculated Property |
| Cp,gas | 297.28 | J/mol×K | 450.00 | Calculated Property |
| Cp,gas | 367.37 | J/mol×K | 600.00 | Calculated Property |
| Cp,gas | 421.77 | J/mol×K | 750.00 | Calculated Property |
| Cp,gas | 464.17 | J/mol×K | 900.00 | Calculated Property |
| Cp,gas | 497.64 | J/mol×K | 1050.00 | Calculated Property |
| Cp,gas | 524.41 | J/mol×K | 1200.00 | Calculated Property |
| Cp,gas | 546.02 | J/mol×K | 1350.00 | Calculated Property |
| Cp,gas | 563.59 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [226.87; 465.06] | J/mol×K | [165.00; 560.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 3.91630e+01 | |||
| Coefficient B | 2.53280e+01 | |||
| Coefficient C | 4.71824e+00 | |||
| Coefficient D | 2.15720e-03 | |||
| Coefficient E | 2.63690e-07 | |||
| Temperature range, min. | 165.00 | |||
| Temperature range, max. | 560.00 | |||
| Cp,liquid | 226.87 | J/mol×K | 165.00 | Calculated Property |
| Cp,liquid | 239.82 | J/mol×K | 208.89 | Calculated Property |
| Cp,liquid | 256.31 | J/mol×K | 252.78 | Calculated Property |
| Cp,liquid | 275.86 | J/mol×K | 296.67 | Calculated Property |
| Cp,liquid | 298.43 | J/mol×K | 340.56 | Calculated Property |
| Cp,liquid | 324.14 | J/mol×K | 384.44 | Calculated Property |
| Cp,liquid | 353.28 | J/mol×K | 428.33 | Calculated Property |
| Cp,liquid | 386.18 | J/mol×K | 472.22 | Calculated Property |
| Cp,liquid | 423.27 | J/mol×K | 516.11 | Calculated Property |
| Cp,liquid | 465.06 | J/mol×K | 560.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0119007; 0.0001301] | Pa×s | [165.55; 472.12] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.12520e+01 | |||
| Coefficient B | 1.14760e+03 | |||
| Coefficient C | -2.19990e-02 | |||
| Coefficient D | 4.37060e-08 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 165.55 | |||
| Temperature range, max. | 472.12 | |||
| η | 0.0119007 | Pa×s | 165.55 | Calculated Property |
| η | 0.0036331 | Pa×s | 199.61 | Calculated Property |
| η | 0.0015671 | Pa×s | 233.68 | Calculated Property |
| η | 0.0008371 | Pa×s | 267.74 | Calculated Property |
| η | 0.0005151 | Pa×s | 301.80 | Calculated Property |
| η | 0.0003498 | Pa×s | 335.87 | Calculated Property |
| η | 0.0002551 | Pa×s | 369.93 | Calculated Property |
| η | 0.0001962 | Pa×s | 403.99 | Calculated Property |
| η | 0.0001573 | Pa×s | 438.06 | Calculated Property |
| η | 0.0001301 | Pa×s | 472.12 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [52.76; 16.53] | kJ/mol | [165.55; 567.80] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 6.33780e+01 | |||
| Coefficient B | 6.76670e-01 | |||
| Coefficient C | -5.39960e-01 | |||
| Coefficient D | 4.56080e-01 | |||
| Coefficient E | -1.89580e-01 | |||
| Critical temperature, Tc (K) | 5.90150e+02 | |||
| Temperature range, min. | 165.55 | |||
| Temperature range, max. | 567.80 | |||
| ΔvapH | 52.76 | kJ/mol | 165.55 | Calculated Property |
| ΔvapH | 50.10 | kJ/mol | 210.24 | Calculated Property |
| ΔvapH | 47.41 | kJ/mol | 254.94 | Calculated Property |
| ΔvapH | 44.62 | kJ/mol | 299.63 | Calculated Property |
| ΔvapH | 41.65 | kJ/mol | 344.33 | Calculated Property |
| ΔvapH | 38.44 | kJ/mol | 389.02 | Calculated Property |
| ΔvapH | 34.83 | kJ/mol | 433.72 | Calculated Property |
| ΔvapH | 30.59 | kJ/mol | 478.41 | Calculated Property |
| ΔvapH | 25.18 | kJ/mol | 523.11 | Calculated Property |
| ΔvapH | 16.53 | kJ/mol | 567.80 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [304.28; 445.37] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.45076e+01 | |||
| Coefficient B | -3.67249e+03 | |||
| Coefficient C | -4.60190e+01 | |||
| Temperature range, min. | 304.28 | |||
| Temperature range, max. | 445.37 | |||
| Pvap | 1.33 | kPa | 304.28 | Calculated Property |
| Pvap | 3.01 | kPa | 319.96 | Calculated Property |
| Pvap | 6.22 | kPa | 335.63 | Calculated Property |
| Pvap | 11.92 | kPa | 351.31 | Calculated Property |
| Pvap | 21.45 | kPa | 366.99 | Calculated Property |
| Pvap | 36.54 | kPa | 382.66 | Calculated Property |
| Pvap | 59.38 | kPa | 398.34 | Calculated Property |
| Pvap | 92.57 | kPa | 414.02 | Calculated Property |
| Pvap | 139.17 | kPa | 429.69 | Calculated Property |
| Pvap | 202.65 | kPa | 445.37 | Calculated Property |
| Pvap | [1.14e-08; 2340.00] | kPa | [165.55; 572.94] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.62437e+02 | |||
| Coefficient B | -1.11704e+04 | |||
| Coefficient C | -2.22687e+01 | |||
| Coefficient D | 1.90112e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | Range stopped where the equation exceeds Pc; ChemSep gives it to 590.15 K. | |||
| Temperature range, min. | 165.55 | |||
| Temperature range, max. | 572.94 | |||
| Pvap | 1.14e-08 | kPa | 165.55 | Calculated Property |
| Pvap | 1.41e-04 | kPa | 210.82 | Calculated Property |
| Pvap | 0.03 | kPa | 256.08 | Calculated Property |
| Pvap | 0.98 | kPa | 301.35 | Calculated Property |
| Pvap | 9.60 | kPa | 346.61 | Calculated Property |
| Pvap | 48.76 | kPa | 391.88 | Calculated Property |
| Pvap | 166.97 | kPa | 437.14 | Calculated Property |
| Pvap | 451.55 | kPa | 482.41 | Calculated Property |
| Pvap | 1065.33 | kPa | 527.67 | Calculated Property |
| Pvap | 2340.00 | kPa | 572.94 | Calculated Property |
| Pvap | [8.72e-08; 2249.28] | kPa | [165.55; 590.15] |
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 | 8.28140e+01 | |||
| Coefficient B | -8.03661e+03 | |||
| Coefficient C | -9.91643e+00 | |||
| Coefficient D | 5.14767e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 165.55 | |||
| Temperature range, max. | 590.15 | |||
| Pvap | 8.72e-08 | kPa | 165.55 | Calculated Property |
| Pvap | 3.77e-04 | kPa | 212.73 | Calculated Property |
| Pvap | 0.06 | kPa | 259.91 | Calculated Property |
| Pvap | 1.40 | kPa | 307.08 | Calculated Property |
| Pvap | 13.00 | kPa | 354.26 | Calculated Property |
| Pvap | 65.01 | kPa | 401.44 | Calculated Property |
| Pvap | 217.98 | kPa | 448.62 | Calculated Property |
| Pvap | 559.39 | kPa | 495.79 | Calculated Property |
| Pvap | 1195.32 | kPa | 542.97 | Calculated Property |
| Pvap | 2249.28 | kPa | 590.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [812.12; 404.76] | kg/m3 | [165.55; 567.80] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 6.41147e+01 | |||
| Coefficient B | 2.64380e-01 | |||
| Coefficient C | 5.90150e+02 | |||
| Coefficient D | 2.91550e-01 | |||
| Temperature range, min. | 165.55 | |||
| Temperature range, max. | 567.80 | |||
| ρl | 812.12 | kg/m3 | 165.55 | Calculated Property |
| ρl | 781.40 | kg/m3 | 210.24 | Calculated Property |
| ρl | 749.31 | kg/m3 | 254.94 | Calculated Property |
| ρl | 715.56 | kg/m3 | 299.63 | Calculated Property |
| ρl | 679.68 | kg/m3 | 344.33 | Calculated Property |
| ρl | 641.02 | kg/m3 | 389.02 | Calculated Property |
| ρl | 598.48 | kg/m3 | 433.72 | Calculated Property |
| ρl | 550.03 | kg/m3 | 478.41 | Calculated Property |
| ρl | 491.11 | kg/m3 | 523.11 | Calculated Property |
| ρl | 404.76 | kg/m3 | 567.80 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 7.63e-04] | N/m | [165.55; 567.80] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -1.11160e-02 | |||
| Coefficient B | 1.77330e+01 | |||
| Coefficient C | -2.99900e+00 | |||
| Coefficient D | -4.69990e-04 | |||
| Coefficient E | -3.71710e-06 | |||
| Temperature range, min. | 165.55 | |||
| Temperature range, max. | 567.80 | |||
| γ | 0.04 | N/m | 165.55 | Calculated Property |
| γ | 0.03 | N/m | 210.24 | Calculated Property |
| γ | 0.03 | N/m | 254.94 | Calculated Property |
| γ | 0.02 | N/m | 299.63 | Calculated Property |
| γ | 0.02 | N/m | 344.33 | Calculated Property |
| γ | 0.01 | N/m | 389.02 | Calculated Property |
| γ | 0.01 | N/m | 433.72 | Calculated Property |
| γ | 0.01 | N/m | 478.41 | Calculated Property |
| γ | 0.00 | N/m | 523.11 | Calculated Property |
| γ | 7.63e-04 | N/m | 567.80 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.00; 0.09] | W/m×K | [165.55; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 4.09680e-05 | |||
| Coefficient B | 1.10960e+00 | |||
| Coefficient C | -1.78720e+02 | |||
| Coefficient D | 1.80220e+05 | |||
| Temperature range, min. | 165.55 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.00 | W/m×K | 165.55 | Calculated Property |
| λgas | 0.01 | W/m×K | 258.27 | Calculated Property |
| λgas | 0.01 | W/m×K | 350.98 | Calculated Property |
| λgas | 0.02 | W/m×K | 443.70 | Calculated Property |
| λgas | 0.03 | W/m×K | 536.42 | Calculated Property |
| λgas | 0.04 | W/m×K | 629.13 | Calculated Property |
| λgas | 0.06 | W/m×K | 721.85 | Calculated Property |
| λgas | 0.07 | W/m×K | 814.57 | Calculated Property |
| λgas | 0.08 | W/m×K | 907.28 | Calculated Property |
| λgas | 0.09 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.16; 0.09] | W/m×K | [165.55; 470.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K | |||
| Coefficient A | -1.64200e-01 | |||
| Coefficient B | 1.09100e+01 | |||
| Coefficient C | -1.12650e+00 | |||
| Coefficient D | -2.33660e-04 | |||
| Coefficient E | -7.96370e-07 | |||
| Temperature range, min. | 165.55 | |||
| Temperature range, max. | 470.00 | |||
| λliquid | 0.16 | W/m×K | 165.55 | Calculated Property |
| λliquid | 0.15 | W/m×K | 199.38 | Calculated Property |
| λliquid | 0.14 | W/m×K | 233.21 | Calculated Property |
| λliquid | 0.14 | W/m×K | 267.03 | Calculated Property |
| λliquid | 0.13 | W/m×K | 300.86 | Calculated Property |
| λliquid | 0.12 | W/m×K | 334.69 | Calculated Property |
| λliquid | 0.11 | W/m×K | 368.52 | Calculated Property |
| λliquid | 0.10 | W/m×K | 402.34 | Calculated Property |
| λliquid | 0.09 | W/m×K | 436.17 | Calculated Property |
| λliquid | 0.09 | W/m×K | 470.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Octane, 3-methyl-.
Sources
- KDB Vapor Pressure Data
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Cheméo Relay (1.0)
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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