- InChI
- InChI=1S/C9H20/c1-5-6-7-8-9(2,3)4/h5-8H2,1-4H3
- InChI Key
- PSABUFWDVWCFDP-UHFFFAOYSA-N
- Formula
- C9H20
- SMILES
- CCCCCC(C)(C)C
- Molecular Weight1
- 128.26
- CAS
- 1071-26-7
- Other Names
-
- 2,2-Dimethylheptane
- 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).
- 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).
- ΔfH°liquid : Liquid phase 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).
- 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 | [0.3830; 0.3900] |
|
|
| ω | 0.3830 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.3900 | KDB | |
| AP | 352.150 | K | KDB |
| ΔcH°liquid | -6111.74 ± 0.84 | kJ/mol | NIST |
| μ | 0.00 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | [16.75; 17.90] | kJ/mol |
|
| ΔfG° | 17.90 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | 16.75 | kJ/mol | KDB |
| Δc,grossH | 6111.74 | kJ/mol | KDB |
| Δc,netH | 5671.622 | kJ/mol | KDB |
| ΔfH°gas | [-247.00; -246.10] | kJ/mol |
|
| ΔfH°gas | -246.10 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -247.00 | kJ/mol | KDB |
| ΔfH°gas | -246.10 | kJ/mol | NIST |
| ΔfH°liquid | -288.20 ± 1.00 | kJ/mol | NIST |
| ΔfusH° | 11.65 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 42.30 | kJ/mol | NIST |
| IE | 9.50 | eV | Relay (1.0) Calculated Property |
| log10WS | -5.30 | Relay (1.0) Calculated Property | |
| logPoct/wat | 3.613 | Crippen Calculated Property | |
| McVol | 137.670 | ml/mol | McGowan Calculated Property |
| Pc | [2350.00; 2350.00] | kPa |
|
| Pc | 2350.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value |
| Pc | 2350.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 2350.00 | kPa | KDB |
| Pc | 2350.00 ± 40.00 | kPa | NIST |
| Pc | 2350.00 ± 41.37 | kPa | NIST |
| Ptriple | 1.53e-07 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [808.00; 829.90] |
|
|
| Inp | 816.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 813.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 818.00 | NIST | |
| Inp | 815.10 | NIST | |
| Inp | 816.10 | NIST | |
| Inp | 820.00 | NIST | |
| Inp | 820.00 | NIST | |
| Inp | 817.10 | NIST | |
| Inp | 816.00 | NIST | |
| Inp | 816.50 | NIST | |
| Inp | 817.10 | NIST | |
| Inp | 817.70 | NIST | |
| Inp | 811.60 | NIST | |
| Inp | 814.20 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 816.00 | NIST | |
| Inp | 810.00 | NIST | |
| Inp | 811.00 | NIST | |
| Inp | 811.00 | NIST | |
| Inp | 812.00 | NIST | |
| Inp | 813.00 | NIST | |
| Inp | 820.00 | NIST | |
| Inp | Outlier 808.00 | NIST | |
| Inp | 816.00 | NIST | |
| Inp | 817.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 816.00 | NIST | |
| Inp | 817.00 | NIST | |
| Inp | 817.00 | NIST | |
| Inp | 812.00 | NIST | |
| Inp | Outlier 829.90 | NIST | |
| Inp | 816.00 | NIST | |
| Inp | Outlier 824.70 | NIST | |
| Inp | 818.90 | NIST | |
| Inp | 816.53 | NIST | |
| Inp | 818.34 | NIST | |
| Inp | 820.00 | NIST | |
| Inp | 819.00 | NIST | |
| Inp | 817.00 | NIST | |
| Inp | 819.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 819.00 | NIST | |
| Inp | 820.00 | NIST | |
| Inp | 818.00 | NIST | |
| Inp | 817.00 | NIST | |
| Inp | 820.00 | NIST | |
| Inp | 818.00 | NIST | |
| Inp | 818.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 816.00 | NIST | |
| Inp | 816.00 | NIST | |
| Inp | 819.00 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 817.00 | NIST | |
| Inp | Outlier 829.90 | NIST | |
| Inp | 819.00 | NIST | |
| Inp | 815.00 | NIST | |
| Tboil | [401.15; 406.04] | K |
|
| Tboil | 405.97 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 405.80 | K | KDB |
| Tboil | 405.90 ± 0.40 | K | NIST |
| Tboil | 404.65 ± 2.00 | K | NIST |
| Tboil | Outlier 401.15 ± 2.00 | K | NIST |
| Tboil | 405.87 ± 0.30 | K | NIST |
| Tboil | 406.04 ± 0.20 | K | NIST |
| Tboil | 406.04 ± 0.30 | K | NIST |
| Tboil | 405.99 ± 0.30 | K | NIST |
| Tboil | 405.45 ± 0.60 | K | NIST |
| Tboil | 405.84 ± 0.50 | K | NIST |
| Tboil | 403.65 ± 1.50 | K | NIST |
| Tboil | 403.55 ± 1.00 | K | NIST |
| Tc | [576.69; 577.80] | K |
|
| Tc | 576.70 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value |
| Tc | 577.80 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 576.70 | K | KDB |
| Tc | 576.70 ± 0.50 | K | NIST |
| Tc | 576.69 ± 0.50 | K | NIST |
| Tfus | [159.84; 160.15] | K |
|
| Tfus | 160.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 160.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 160.00 | K | KDB |
| Tfus | 160.11 ± 0.04 | K | NIST |
| Tfus | 160.12 ± 0.03 | K | NIST |
| Tfus | 160.15 ± 0.02 | K | NIST |
| Tfus | 160.11 ± 0.05 | K | NIST |
| Tfus | 160.12 ± 0.03 | K | NIST |
| Tfus | 160.15 ± 0.02 | K | NIST |
| Tfus | 160.01 ± 0.20 | K | NIST |
| Tfus | 159.84 ± 0.30 | K | NIST |
| Tfus | 160.01 ± 0.30 | K | NIST |
| Tfus | 159.84 ± 0.30 | K | NIST |
| Tfus | 159.87 ± 0.20 | K | NIST |
| Ttriple | 160.15 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 5.55 | ChemSep v8.3 pure component data Compiled value | |
| URi | 6.52 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.525; 0.528] | m3/kmol |
|
| Vc | 0.525 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.528 | m3/kmol | KDB |
| Zc | [0.2570000; 0.2590160] |
|
|
| Zc | 0.2570000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2590160 | KDB | |
| Zra | 0.26 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 34.77 | kJ/mol | 405.90 | KDB |
| n0 | 1.39930 | 298.15 | KDB | |
| ρl | 711.00 | kg/m3 | 293.00 | KDB |
| γ | 0.02 | N/m | 298.20 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [132.86; 585.09] | 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 | 1.19340e+02 | |||
| Coefficient B | -5.82530e+02 | |||
| Coefficient C | 6.47824e+00 | |||
| Coefficient D | 6.76750e-05 | |||
| Coefficient E | -2.12290e-08 | |||
| Temperature range, min. | 150.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 132.86 | J/mol×K | 150.00 | Calculated Property |
| Cp,gas | 214.43 | J/mol×K | 300.00 | Calculated Property |
| Cp,gas | 302.41 | J/mol×K | 450.00 | Calculated Property |
| Cp,gas | 374.10 | J/mol×K | 600.00 | Calculated Property |
| Cp,gas | 430.51 | J/mol×K | 750.00 | Calculated Property |
| Cp,gas | 475.26 | J/mol×K | 900.00 | Calculated Property |
| Cp,gas | 511.28 | J/mol×K | 1050.00 | Calculated Property |
| Cp,gas | 540.68 | J/mol×K | 1200.00 | Calculated Property |
| Cp,gas | 564.94 | J/mol×K | 1350.00 | Calculated Property |
| Cp,gas | 585.09 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [219.27; 344.33] | J/mol×K | [160.15; 405.84] |
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 | 1.88490e+02 | |||
| Coefficient B | -1.26200e+02 | |||
| Coefficient C | 3.25324e+00 | |||
| Coefficient D | 6.53610e-03 | |||
| Coefficient E | -3.31540e-06 | |||
| Temperature range, min. | 160.15 | |||
| Temperature range, max. | 405.84 | |||
| Cp,liquid | 219.27 | J/mol×K | 160.15 | Calculated Property |
| Cp,liquid | 228.48 | J/mol×K | 187.45 | Calculated Property |
| Cp,liquid | 238.70 | J/mol×K | 214.75 | Calculated Property |
| Cp,liquid | 250.03 | J/mol×K | 242.05 | Calculated Property |
| Cp,liquid | 262.53 | J/mol×K | 269.35 | Calculated Property |
| Cp,liquid | 276.28 | J/mol×K | 296.64 | Calculated Property |
| Cp,liquid | 291.32 | J/mol×K | 323.94 | Calculated Property |
| Cp,liquid | 307.68 | J/mol×K | 351.24 | Calculated Property |
| Cp,liquid | 325.35 | J/mol×K | 378.54 | Calculated Property |
| Cp,liquid | 344.33 | J/mol×K | 405.84 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0254001; 0.0001582] | Pa×s | [160.15; 462.40] |
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 | -1.16540e+01 | |||
| Coefficient B | 1.25040e+03 | |||
| Coefficient C | 3.44500e-02 | |||
| Coefficient D | -6.06180e-08 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 160.15 | |||
| Temperature range, max. | 462.40 | |||
| η | 0.0254001 | Pa×s | 160.15 | Calculated Property |
| η | 0.0066005 | Pa×s | 193.73 | Calculated Property |
| η | 0.0025555 | Pa×s | 227.32 | Calculated Property |
| η | 0.0012636 | Pa×s | 260.90 | Calculated Property |
| η | 0.0007338 | Pa×s | 294.48 | Calculated Property |
| η | 0.0004763 | Pa×s | 328.07 | Calculated Property |
| η | 0.0003350 | Pa×s | 361.65 | Calculated Property |
| η | 0.0002501 | Pa×s | 395.23 | Calculated Property |
| η | 0.0001954 | Pa×s | 428.82 | Calculated Property |
| η | 0.0001582 | Pa×s | 462.40 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [49.36; 5.74] | kJ/mol | [160.15; 576.70] |
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 | 5.67758e+01 | |||
| Coefficient B | 4.20266e-01 | |||
| Coefficient C | 6.06766e-02 | |||
| Coefficient D | -5.89710e-02 | |||
| Coefficient E | -5.65229e-02 | |||
| Critical temperature, Tc (K) | 5.77800e+02 | |||
| Temperature range, min. | 160.15 | |||
| Temperature range, max. | 576.70 | |||
| ΔvapH | 49.36 | kJ/mol | 160.15 | Calculated Property |
| ΔvapH | 46.91 | kJ/mol | 206.43 | Calculated Property |
| ΔvapH | 44.32 | kJ/mol | 252.72 | Calculated Property |
| ΔvapH | 41.56 | kJ/mol | 299.00 | Calculated Property |
| ΔvapH | 38.62 | kJ/mol | 345.28 | Calculated Property |
| ΔvapH | 35.42 | kJ/mol | 391.57 | Calculated Property |
| ΔvapH | 31.85 | kJ/mol | 437.85 | Calculated Property |
| ΔvapH | 27.60 | kJ/mol | 484.13 | Calculated Property |
| ΔvapH | 21.81 | kJ/mol | 530.42 | Calculated Property |
| ΔvapH | 5.74 | kJ/mol | 576.70 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [295.68; 433.29] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.43315e+01 | |||
| Coefficient B | -3.46987e+03 | |||
| Coefficient C | -4.86060e+01 | |||
| Temperature range, min. | 295.68 | |||
| Temperature range, max. | 433.29 | |||
| Pvap | 1.33 | kPa | 295.68 | Calculated Property |
| Pvap | 3.02 | kPa | 310.97 | Calculated Property |
| Pvap | 6.26 | kPa | 326.26 | Calculated Property |
| Pvap | 12.02 | kPa | 341.55 | Calculated Property |
| Pvap | 21.63 | kPa | 356.84 | Calculated Property |
| Pvap | 36.83 | kPa | 372.13 | Calculated Property |
| Pvap | 59.75 | kPa | 387.42 | Calculated Property |
| Pvap | 92.99 | kPa | 402.71 | Calculated Property |
| Pvap | 139.50 | kPa | 418.00 | Calculated Property |
| Pvap | 202.64 | kPa | 433.29 | Calculated Property |
| Pvap | [1.31e-08; 3363.66] | kPa | [160.15; 576.70] |
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 | 1.66269e+02 | |||
| Coefficient B | -1.08916e+04 | |||
| Coefficient C | -2.30435e+01 | |||
| Coefficient D | 2.17483e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 160.15 | |||
| Temperature range, max. | 576.70 | |||
| Pvap | 1.31e-08 | kPa | 160.15 | Calculated Property |
| Pvap | 2.28e-04 | kPa | 206.43 | Calculated Property |
| Pvap | 0.05 | kPa | 252.72 | Calculated Property |
| Pvap | 1.53 | kPa | 299.00 | Calculated Property |
| Pvap | 14.05 | kPa | 345.28 | Calculated Property |
| Pvap | 67.66 | kPa | 391.57 | Calculated Property |
| Pvap | 224.80 | kPa | 437.85 | Calculated Property |
| Pvap | 605.37 | kPa | 484.13 | Calculated Property |
| Pvap | 1460.03 | kPa | 530.42 | Calculated Property |
| Pvap | 3363.66 | kPa | 576.70 | Calculated Property |
| Pvap | [5.15e-08; 2348.28] | kPa | [160.15; 576.80] |
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 | 1.02542e+02 | |||
| Coefficient B | -8.54380e+03 | |||
| Coefficient C | -1.30419e+01 | |||
| Coefficient D | 8.85387e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 160.15 | |||
| Temperature range, max. | 576.80 | |||
| Pvap | 5.15e-08 | kPa | 160.15 | Calculated Property |
| Pvap | 3.42e-04 | kPa | 206.44 | Calculated Property |
| Pvap | 0.06 | kPa | 252.74 | Calculated Property |
| Pvap | 1.52 | kPa | 299.03 | Calculated Property |
| Pvap | 13.92 | kPa | 345.33 | Calculated Property |
| Pvap | 68.00 | kPa | 391.62 | Calculated Property |
| Pvap | 223.32 | kPa | 437.92 | Calculated Property |
| Pvap | 567.53 | kPa | 484.21 | Calculated Property |
| Pvap | 1219.41 | kPa | 530.51 | Calculated Property |
| Pvap | 2348.28 | kPa | 576.80 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [800.18; 258.00] | kg/m3 | [160.15; 576.70] |
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 | 2.55600e+01 | |||
| Coefficient B | 1.69440e-01 | |||
| Coefficient C | 5.77800e+02 | |||
| Coefficient D | 1.90980e-01 | |||
| Temperature range, min. | 160.15 | |||
| Temperature range, max. | 576.70 | |||
| ρl | 800.18 | kg/m3 | 160.15 | Calculated Property |
| ρl | 771.10 | kg/m3 | 206.43 | Calculated Property |
| ρl | 740.16 | kg/m3 | 252.72 | Calculated Property |
| ρl | 706.90 | kg/m3 | 299.00 | Calculated Property |
| ρl | 670.66 | kg/m3 | 345.28 | Calculated Property |
| ρl | 630.39 | kg/m3 | 391.57 | Calculated Property |
| ρl | 584.29 | kg/m3 | 437.85 | Calculated Property |
| ρl | 528.71 | kg/m3 | 484.13 | Calculated Property |
| ρl | 453.68 | kg/m3 | 530.42 | Calculated Property |
| ρl | 258.00 | kg/m3 | 576.70 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 7.03e-06] | N/m | [160.15; 573.78] |
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 | -8.02500e-03 | |||
| Coefficient B | 4.09380e+01 | |||
| Coefficient C | -3.40140e+00 | |||
| Coefficient D | 7.35540e-04 | |||
| Coefficient E | -5.82060e-06 | |||
| Comment | Range stopped where the equation turns negative; ChemSep gives it to 576.7 K. | |||
| Temperature range, min. | 160.15 | |||
| Temperature range, max. | 573.78 | |||
| γ | 0.03 | N/m | 160.15 | Calculated Property |
| γ | 0.03 | N/m | 206.11 | Calculated Property |
| γ | 0.02 | N/m | 252.07 | Calculated Property |
| γ | 0.02 | N/m | 298.03 | Calculated Property |
| γ | 0.02 | N/m | 343.99 | Calculated Property |
| γ | 0.01 | N/m | 389.95 | Calculated Property |
| γ | 0.01 | N/m | 435.91 | Calculated Property |
| γ | 0.01 | N/m | 481.87 | Calculated Property |
| γ | 0.00 | N/m | 527.82 | Calculated Property |
| γ | 7.03e-06 | N/m | 573.78 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.00; 0.09] | W/m×K | [160.15; 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 | 2.35820e-05 | |||
| Coefficient B | 1.19660e+00 | |||
| Coefficient C | -1.48340e+02 | |||
| Coefficient D | 1.44910e+05 | |||
| Temperature range, min. | 160.15 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.00 | W/m×K | 160.15 | Calculated Property |
| λgas | 0.01 | W/m×K | 253.47 | Calculated Property |
| λgas | 0.01 | W/m×K | 346.78 | Calculated Property |
| λgas | 0.02 | W/m×K | 440.10 | Calculated Property |
| λgas | 0.04 | W/m×K | 533.42 | Calculated Property |
| λgas | 0.05 | W/m×K | 626.73 | Calculated Property |
| λgas | 0.06 | W/m×K | 720.05 | Calculated Property |
| λgas | 0.07 | W/m×K | 813.37 | Calculated Property |
| λgas | 0.08 | W/m×K | 906.68 | Calculated Property |
| λgas | 0.09 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.13; 0.08] | W/m×K | [160.15; 405.84] |
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 | -4.96100e-02 | |||
| Coefficient B | 4.53640e+00 | |||
| Coefficient C | -1.65700e+00 | |||
| Coefficient D | -3.87740e-04 | |||
| Coefficient E | -1.44650e-06 | |||
| Temperature range, min. | 160.15 | |||
| Temperature range, max. | 405.84 | |||
| λliquid | 0.13 | W/m×K | 160.15 | Calculated Property |
| λliquid | 0.12 | W/m×K | 187.45 | Calculated Property |
| λliquid | 0.12 | W/m×K | 214.75 | Calculated Property |
| λliquid | 0.11 | W/m×K | 242.05 | Calculated Property |
| λliquid | 0.11 | W/m×K | 269.35 | Calculated Property |
| λliquid | 0.10 | W/m×K | 296.64 | Calculated Property |
| λliquid | 0.10 | W/m×K | 323.94 | Calculated Property |
| λliquid | 0.09 | W/m×K | 351.24 | Calculated Property |
| λliquid | 0.09 | W/m×K | 378.54 | Calculated Property |
| λliquid | 0.08 | W/m×K | 405.84 | Calculated Property |
Similar Compounds
Find more compounds similar to Heptane, 2,2-dimethyl-.
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).
- IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 ChEDL chemicals 1.5.2, from Daubert, T. E. Vapor-Liquid Critical Properties of Elements and Compounds. 5. Branched Alkanes and Cycloalkanes. J. Chem. Eng. Data 1996, 41, 365-372.
- 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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