- InChI
- InChI=1S/C9H20/c1-6-9(4,5)7-8(2)3/h8H,6-7H2,1-5H3
- InChI Key
- SVEMKBCPZYWEPH-UHFFFAOYSA-N
- Formula
- C9H20
- SMILES
- CCC(C)(C)CC(C)C
- Molecular Weight1
- 128.26
- CAS
- 16747-30-1
- Other Names
-
- 2,4,4-Trimethylhexane
- ω : Acentric Factor.
- 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).
- 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).
- 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 | 0.3522 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°liquid | -6119.73 ± 0.75 | kJ/mol | NIST |
| μ | 0.00 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | 25.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -240.30 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°liquid | -280.20 ± 0.92 | kJ/mol | NIST |
| ΔfusH° | 8.13 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 41.10 | kJ/mol | NIST |
| IE | 9.48 | eV | Relay (1.0) Calculated Property |
| log10WS | -5.09 | Relay (1.0) Calculated Property | |
| logPoct/wat | 3.469 | Crippen Calculated Property | |
| McVol | 137.670 | ml/mol | McGowan Calculated Property |
| Pc | 2500.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 3.07e-07 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [805.00; 816.00] |
|
|
| Inp | 810.10 | NIST | |
| Inp | 810.00 | NIST | |
| Inp | 806.90 | NIST | |
| Inp | 809.80 | NIST | |
| Inp | 808.70 | NIST | |
| Inp | 808.80 | NIST | |
| Inp | 809.00 | NIST | |
| Inp | 809.70 | NIST | |
| Inp | 808.00 | NIST | |
| Inp | 811.00 | NIST | |
| Inp | 808.30 | NIST | |
| Inp | 810.00 | NIST | |
| Inp | Outlier 805.00 | NIST | |
| Inp | 808.00 | NIST | |
| Inp | 811.00 | NIST | |
| Inp | 810.00 | NIST | |
| Inp | 809.00 | NIST | |
| Inp | 808.00 | NIST | |
| Inp | 810.10 | NIST | |
| Inp | 812.20 | NIST | |
| Inp | 807.42 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 812.00 | NIST | |
| Inp | 808.00 | NIST | |
| Inp | 807.00 | NIST | |
| Inp | Outlier 816.00 | NIST | |
| Inp | 811.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 808.00 | NIST | |
| Inp | 810.00 | NIST | |
| Inp | 810.00 | NIST | |
| Inp | 812.00 | NIST | |
| Inp | 810.00 | NIST | |
| Inp | 808.00 | NIST | |
| Inp | 811.00 | NIST | |
| Tboil | [402.30; 404.05] | K |
|
| Tboil | 403.81 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 403.90 | K | NIST |
| Tboil | 403.79 ± 0.03 | K | NIST |
| Tboil | 403.60 ± 0.25 | K | NIST |
| Tboil | 404.05 ± 0.50 | K | NIST |
| Tboil | 403.95 ± 0.50 | K | NIST |
| Tboil | Outlier 402.30 ± 0.40 | K | NIST |
| Tc | 583.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [155.45; 159.95] | K |
|
| Tfus | 159.95 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 159.78 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 159.77 ± 0.04 | K | NIST |
| Tfus | 159.77 ± 0.05 | K | NIST |
| Tfus | 155.45 ± 0.50 | K | NIST |
| Ttriple | 159.78 | 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 | 0.509 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2600000 | ChemSep v8.3 pure component data Compiled value | |
| Zra | 0.26 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 38.50 | kJ/mol | 364.50 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [142.38; 595.24] | J/mol×K | [200.00; 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 | 8.41700e+01 | |||
| Coefficient B | -4.52220e+02 | |||
| Coefficient C | 6.25924e+00 | |||
| Coefficient D | 3.51970e-04 | |||
| Coefficient E | -1.10760e-07 | |||
| Temperature range, min. | 200.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 142.38 | J/mol×K | 200.00 | Calculated Property |
| Cp,gas | 240.89 | J/mol×K | 344.44 | Calculated Property |
| Cp,gas | 323.98 | J/mol×K | 488.89 | Calculated Property |
| Cp,gas | 390.21 | J/mol×K | 633.33 | Calculated Property |
| Cp,gas | 443.62 | J/mol×K | 777.78 | Calculated Property |
| Cp,gas | 487.31 | J/mol×K | 922.22 | Calculated Property |
| Cp,gas | 523.26 | J/mol×K | 1066.67 | Calculated Property |
| Cp,gas | 552.73 | J/mol×K | 1211.11 | Calculated Property |
| Cp,gas | 576.54 | J/mol×K | 1355.56 | Calculated Property |
| Cp,gas | 595.24 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [197.59; 344.95] | J/mol×K | [200.00; 403.81] |
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 | 3.67950e+01 | |||
| Coefficient B | -7.94140e+01 | |||
| Coefficient C | 4.78124e+00 | |||
| Coefficient D | 4.10980e-03 | |||
| Coefficient E | -3.14940e-06 | |||
| Temperature range, min. | 200.00 | |||
| Temperature range, max. | 403.81 | |||
| Cp,liquid | 197.59 | J/mol×K | 200.00 | Calculated Property |
| Cp,liquid | 215.10 | J/mol×K | 222.65 | Calculated Property |
| Cp,liquid | 232.40 | J/mol×K | 245.29 | Calculated Property |
| Cp,liquid | 249.50 | J/mol×K | 267.94 | Calculated Property |
| Cp,liquid | 266.38 | J/mol×K | 290.58 | Calculated Property |
| Cp,liquid | 282.96 | J/mol×K | 313.23 | Calculated Property |
| Cp,liquid | 299.20 | J/mol×K | 335.87 | Calculated Property |
| Cp,liquid | 315.00 | J/mol×K | 358.52 | Calculated Property |
| Cp,liquid | 330.29 | J/mol×K | 381.16 | Calculated Property |
| Cp,liquid | 344.95 | J/mol×K | 403.81 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0365612; 0.0000822] | Pa×s | [159.78; 524.70] |
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 | -6.97480e+00 | |||
| Coefficient B | 1.19410e+03 | |||
| Coefficient C | -7.50250e-01 | |||
| Coefficient D | -2.94520e-08 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 159.78 | |||
| Temperature range, max. | 524.70 | |||
| η | 0.0365612 | Pa×s | 159.78 | Calculated Property |
| η | 0.0067954 | Pa×s | 200.33 | Calculated Property |
| η | 0.0021685 | Pa×s | 240.87 | Calculated Property |
| η | 0.0009441 | Pa×s | 281.42 | Calculated Property |
| η | 0.0004998 | Pa×s | 321.97 | Calculated Property |
| η | 0.0003017 | Pa×s | 362.51 | Calculated Property |
| η | 0.0001999 | Pa×s | 403.06 | Calculated Property |
| η | 0.0001417 | Pa×s | 443.61 | Calculated Property |
| η | 0.0001058 | Pa×s | 484.15 | Calculated Property |
| η | 0.0000822 | Pa×s | 524.70 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [47.22; 6.30] | kJ/mol | [159.78; 581.00] |
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 | 5.55510e+01 | |||
| Coefficient B | 6.33160e-01 | |||
| Coefficient C | -6.05320e-01 | |||
| Coefficient D | 5.95930e-01 | |||
| Coefficient E | -2.40620e-01 | |||
| Critical temperature, Tc (K) | 5.83000e+02 | |||
| Temperature range, min. | 159.78 | |||
| Temperature range, max. | 581.00 | |||
| ΔvapH | 47.22 | kJ/mol | 159.78 | Calculated Property |
| ΔvapH | 44.97 | kJ/mol | 206.58 | Calculated Property |
| ΔvapH | 42.66 | kJ/mol | 253.38 | Calculated Property |
| ΔvapH | 40.21 | kJ/mol | 300.19 | Calculated Property |
| ΔvapH | 37.54 | kJ/mol | 346.99 | Calculated Property |
| ΔvapH | 34.55 | kJ/mol | 393.79 | Calculated Property |
| ΔvapH | 31.07 | kJ/mol | 440.59 | Calculated Property |
| ΔvapH | 26.81 | kJ/mol | 487.40 | Calculated Property |
| ΔvapH | 20.92 | kJ/mol | 534.20 | Calculated Property |
| ΔvapH | 6.30 | kJ/mol | 581.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [293.82; 431.43] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.41409e+01 | |||
| Coefficient B | -3.35035e+03 | |||
| Coefficient C | -5.19800e+01 | |||
| Temperature range, min. | 293.82 | |||
| Temperature range, max. | 431.43 | |||
| Pvap | 1.33 | kPa | 293.82 | Calculated Property |
| Pvap | 3.04 | kPa | 309.11 | Calculated Property |
| Pvap | 6.31 | kPa | 324.40 | Calculated Property |
| Pvap | 12.13 | kPa | 339.69 | Calculated Property |
| Pvap | 21.84 | kPa | 354.98 | Calculated Property |
| Pvap | 37.15 | kPa | 370.27 | Calculated Property |
| Pvap | 60.18 | kPa | 385.56 | Calculated Property |
| Pvap | 93.46 | kPa | 400.85 | Calculated Property |
| Pvap | 139.87 | kPa | 416.14 | Calculated Property |
| Pvap | 202.65 | kPa | 431.43 | Calculated Property |
| Pvap | [5.50e-08; 2500.00] | kPa | [159.78; 564.38] |
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 | 1.36205e+02 | |||
| Coefficient B | -9.54153e+03 | |||
| Coefficient C | -1.84559e+01 | |||
| Coefficient D | 1.71318e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | Range stopped where the equation exceeds Pc; ChemSep gives it to 581 K. | |||
| Temperature range, min. | 159.78 | |||
| Temperature range, max. | 564.38 | |||
| Pvap | 5.50e-08 | kPa | 159.78 | Calculated Property |
| Pvap | 3.71e-04 | kPa | 204.74 | Calculated Property |
| Pvap | 0.06 | kPa | 249.69 | Calculated Property |
| Pvap | 1.45 | kPa | 294.65 | Calculated Property |
| Pvap | 12.52 | kPa | 339.60 | Calculated Property |
| Pvap | 58.88 | kPa | 384.56 | Calculated Property |
| Pvap | 192.28 | kPa | 429.51 | Calculated Property |
| Pvap | 504.14 | kPa | 474.47 | Calculated Property |
| Pvap | 1162.21 | kPa | 519.42 | Calculated Property |
| Pvap | 2500.00 | kPa | 564.38 | Calculated Property |
| Pvap | [1.35; 2441.51] | kPa | [293.15; 581.50] |
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 | 8.66959e+01 | |||
| Coefficient B | -7.69356e+03 | |||
| Coefficient C | -1.06981e+01 | |||
| Coefficient D | 7.20088e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 293.15 | |||
| Temperature range, max. | 581.50 | |||
| Pvap | 1.35 | kPa | 293.15 | Calculated Property |
| Pvap | 6.80 | kPa | 325.19 | Calculated Property |
| Pvap | 24.30 | kPa | 357.23 | Calculated Property |
| Pvap | 67.80 | kPa | 389.27 | Calculated Property |
| Pvap | 157.65 | kPa | 421.31 | Calculated Property |
| Pvap | 320.10 | kPa | 453.34 | Calculated Property |
| Pvap | 586.90 | kPa | 485.38 | Calculated Property |
| Pvap | 996.11 | kPa | 517.42 | Calculated Property |
| Pvap | 1594.43 | kPa | 549.46 | Calculated Property |
| Pvap | 2441.51 | kPa | 581.50 | Calculated Property |
| Pvap | [6.40; 104.03] | kPa | [323.80; 404.79] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.37957e+01 | |||
| Coefficient B | -3.17306e+03 | |||
| Coefficient C | -5.80460e+01 | |||
| Reference | Forziati, Norris, et al., 1949 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 323.80 | |||
| Temperature range, max. | 404.79 | |||
| Pvap | 6.40 | kPa | 323.80 | Calculated Property |
| Pvap | 9.46 | kPa | 332.80 | Calculated Property |
| Pvap | 13.64 | kPa | 341.80 | Calculated Property |
| Pvap | 19.24 | kPa | 350.80 | Calculated Property |
| Pvap | 26.58 | kPa | 359.80 | Calculated Property |
| Pvap | 36.04 | kPa | 368.79 | Calculated Property |
| Pvap | 48.04 | kPa | 377.79 | Calculated Property |
| Pvap | 63.03 | kPa | 386.79 | Calculated Property |
| Pvap | 81.52 | kPa | 395.79 | Calculated Property |
| Pvap | 104.03 | kPa | 404.79 | Calculated Property |
| Pvap | [6.40; 104.03] | kPa | [323.80; 404.79] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.37957e+01 | |||
| Coefficient B | -3.17306e+03 | |||
| Coefficient C | -5.80460e+01 | |||
| Reference | Forziati, Norris, et al., 1949, 2 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 323.80 | |||
| Temperature range, max. | 404.79 | |||
| Pvap | 6.40 | kPa | 323.80 | Calculated Property |
| Pvap | 9.46 | kPa | 332.80 | Calculated Property |
| Pvap | 13.64 | kPa | 341.80 | Calculated Property |
| Pvap | 19.24 | kPa | 350.80 | Calculated Property |
| Pvap | 26.58 | kPa | 359.80 | Calculated Property |
| Pvap | 36.04 | kPa | 368.79 | Calculated Property |
| Pvap | 48.04 | kPa | 377.79 | Calculated Property |
| Pvap | 63.03 | kPa | 386.79 | Calculated Property |
| Pvap | 81.52 | kPa | 395.79 | Calculated Property |
| Pvap | 104.03 | kPa | 404.79 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [811.92; 262.53] | kg/m3 | [159.78; 581.00] |
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 | 1.26390e+01 | |||
| Coefficient B | 1.18620e-01 | |||
| Coefficient C | 5.83000e+02 | |||
| Coefficient D | 1.51610e-01 | |||
| Temperature range, min. | 159.78 | |||
| Temperature range, max. | 581.00 | |||
| ρl | 811.92 | kg/m3 | 159.78 | Calculated Property |
| ρl | 783.40 | kg/m3 | 206.58 | Calculated Property |
| ρl | 752.86 | kg/m3 | 253.38 | Calculated Property |
| ρl | 719.82 | kg/m3 | 300.19 | Calculated Property |
| ρl | 683.57 | kg/m3 | 346.99 | Calculated Property |
| ρl | 642.95 | kg/m3 | 393.79 | Calculated Property |
| ρl | 596.02 | kg/m3 | 440.59 | Calculated Property |
| ρl | 538.80 | kg/m3 | 487.40 | Calculated Property |
| ρl | 460.47 | kg/m3 | 534.20 | Calculated Property |
| ρl | 262.53 | kg/m3 | 581.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 2.14e-05] | N/m | [159.78; 579.74] |
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 | -1.61640e-02 | |||
| Coefficient B | 1.11870e+01 | |||
| Coefficient C | -2.91500e+00 | |||
| Coefficient D | -6.58850e-04 | |||
| Coefficient E | -2.51710e-06 | |||
| Comment | Range stopped where the equation turns negative; ChemSep gives it to 581 K. | |||
| Temperature range, min. | 159.78 | |||
| Temperature range, max. | 579.74 | |||
| γ | 0.03 | N/m | 159.78 | Calculated Property |
| γ | 0.03 | N/m | 206.44 | Calculated Property |
| γ | 0.02 | N/m | 253.10 | Calculated Property |
| γ | 0.02 | N/m | 299.77 | Calculated Property |
| γ | 0.02 | N/m | 346.43 | Calculated Property |
| γ | 0.01 | N/m | 393.09 | Calculated Property |
| γ | 0.01 | N/m | 439.75 | Calculated Property |
| γ | 0.01 | N/m | 486.41 | Calculated Property |
| γ | 0.00 | N/m | 533.07 | Calculated Property |
| γ | 2.14e-05 | N/m | 579.74 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.00; 0.10] | W/m×K | [159.78; 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 | 2.81310e-05 | |||
| Coefficient B | 1.18250e+00 | |||
| Coefficient C | -1.03570e+02 | |||
| Coefficient D | 1.42450e+05 | |||
| Temperature range, min. | 159.78 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.00 | W/m×K | 159.78 | Calculated Property |
| λgas | 0.01 | W/m×K | 253.14 | Calculated Property |
| λgas | 0.02 | W/m×K | 346.50 | Calculated Property |
| λgas | 0.03 | W/m×K | 439.85 | Calculated Property |
| λgas | 0.04 | W/m×K | 533.21 | Calculated Property |
| λgas | 0.05 | W/m×K | 626.57 | Calculated Property |
| λgas | 0.06 | W/m×K | 719.93 | Calculated Property |
| λgas | 0.07 | W/m×K | 813.28 | Calculated Property |
| λgas | 0.08 | W/m×K | 906.64 | Calculated Property |
| λgas | 0.10 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.13; 0.08] | W/m×K | [159.78; 403.81] |
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 | -6.12130e-02 | |||
| Coefficient B | 3.61150e+00 | |||
| Coefficient C | -1.56870e+00 | |||
| Coefficient D | -4.81980e-04 | |||
| Coefficient E | -1.13400e-06 | |||
| Temperature range, min. | 159.78 | |||
| Temperature range, max. | 403.81 | |||
| λliquid | 0.13 | W/m×K | 159.78 | Calculated Property |
| λliquid | 0.13 | W/m×K | 186.89 | Calculated Property |
| λliquid | 0.12 | W/m×K | 214.01 | Calculated Property |
| λliquid | 0.12 | W/m×K | 241.12 | Calculated Property |
| λliquid | 0.11 | W/m×K | 268.24 | Calculated Property |
| λliquid | 0.10 | W/m×K | 295.35 | Calculated Property |
| λliquid | 0.10 | W/m×K | 322.47 | Calculated Property |
| λliquid | 0.09 | W/m×K | 349.58 | Calculated Property |
| λliquid | 0.09 | W/m×K | 376.70 | Calculated Property |
| λliquid | 0.08 | W/m×K | 403.81 | Calculated Property |
Similar Compounds
Find more compounds similar to Hexane, 2,4,4-trimethyl-.
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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