- InChI
- InChI=1S/C6H12/c1-4-5-6(2)3/h4-6H,1-3H3/b5-4+
- InChI Key
- LGAQJENWWYGFSN-SNAWJCMRSA-N
- Formula
- C6H12
- SMILES
- C/C=C/C(C)C
- Molecular Weight1
- 84.16
- CAS
- 674-76-0
- Other Names
-
- (E)-(CH3)2CHCH=CHCH3
- (E)-4-methyl-2-pentene
- (E)-4-methylpent-2-ene
- 4-Methyl-2-pentene, (E)-
- 4-Methyl-2-pentene, trans-
- 4-Methylpentene-2, trans-
- 4-methyl-trans-2-pentene
- trans-4-methyl-2-pentene
- ω : Acentric Factor.
- 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).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- 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.
- Ip : 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 | [0.2552; 0.2900] |
|
|
| ω | 0.2552 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.2900 | KDB | |
| μ | 0.11 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | [74.35; 79.67] | kJ/mol |
|
| ΔfG° | 74.35 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | 79.67 | kJ/mol | KDB |
| Δc,grossH | 3984.59 | kJ/mol | KDB |
| Δc,netH | 3720.496 | kJ/mol | KDB |
| ΔfH°gas | [-61.50; -54.35] | kJ/mol |
|
| ΔfH°gas | -54.35 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -61.50 | kJ/mol | KDB |
| ΔfusH° | 7.98 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [30.00; 30.00] | kJ/mol |
|
| ΔvapH° | 30.00 | kJ/mol | NIST |
| ΔvapH° | 30.00 | kJ/mol | NIST |
| ΔvapH° | 30.00 | kJ/mol | NIST |
| IE | [8.91; 8.97] | eV |
|
| IE | 8.97 ± 0.01 | eV | NIST |
| IE | 8.91 | eV | NIST |
| IE | 8.97 ± 0.01 | eV | NIST |
| logPoct/wat | 2.219 | Crippen Calculated Property | |
| McVol | 91.100 | ml/mol | McGowan Calculated Property |
| Pc | [3040.00; 3220.00] | kPa |
|
| Pc | 3220.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 3040.00 | kPa | KDB |
| Ptriple | 3.45e-07 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [547.00; 575.50] |
|
|
| Inp | 570.40 | NIST | |
| Inp | 561.90 | NIST | |
| Inp | 569.00 | NIST | |
| Inp | 569.00 | NIST | |
| Inp | 569.00 | NIST | |
| Inp | 561.70 | NIST | |
| Inp | 569.10 | NIST | |
| Inp | 568.80 | NIST | |
| Inp | 562.10 | NIST | |
| Inp | 561.90 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 563.00 | NIST | |
| Inp | 563.00 | NIST | |
| Inp | 561.90 | NIST | |
| Inp | 562.00 | NIST | |
| Inp | 562.00 | NIST | |
| Inp | 565.80 | NIST | |
| Inp | 562.00 | NIST | |
| Inp | 562.00 | NIST | |
| Inp | 561.80 | NIST | |
| Inp | 567.00 | NIST | |
| Inp | 557.00 | NIST | |
| Inp | 565.00 | NIST | |
| Inp | 562.00 | NIST | |
| Inp | 562.00 | NIST | |
| Inp | 563.00 | NIST | |
| Inp | 563.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 558.00 | NIST | |
| Inp | 559.00 | NIST | |
| Inp | 557.00 | NIST | |
| Inp | 575.50 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 568.70 | NIST | |
| Inp | 562.00 | NIST | |
| Inp | 561.70 | NIST | |
| Inp | 562.00 | NIST | |
| Inp | 563.00 | NIST | |
| Inp | 572.00 | NIST | |
| Inp | 571.00 | NIST | |
| Inp | 572.00 | NIST | |
| Inp | 571.00 | NIST | |
| Inp | Outlier 547.00 | NIST | |
| Inp | 569.00 | NIST | |
| Inp | 562.00 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 573.00 | NIST | |
| Inp | 574.00 | NIST | |
| Inp | 570.40 | NIST | |
| Inp | 561.70 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 562.00 | NIST | |
| Inp | 561.80 | NIST | |
| Inp | 559.00 | NIST | |
| Inp | 575.50 | NIST | |
| Ip | [590.00; 592.00] |
|
|
| Ip | 592.00 | NIST | |
| Ip | 590.00 | NIST | |
| Ip | 592.00 | NIST | |
| Tboil | [330.90; 331.95] | K |
|
| Tboil | 331.76 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 331.70 | K | KDB |
| Tboil | 331.70 | K | NIST |
| Tboil | 331.76 ± 0.10 | K | NIST |
| Tboil | 331.70 ± 0.40 | K | NIST |
| Tboil | 331.95 ± 0.50 | K | NIST |
| Tboil | 331.65 ± 0.40 | K | NIST |
| Tboil | Outlier 330.90 ± 1.00 | K | NIST |
| Tboil | 331.10 ± 1.00 | K | NIST |
| Tboil | 331.25 ± 1.00 | K | NIST |
| Tboil | 331.95 ± 1.00 | K | NIST |
| Tboil | 331.60 ± 1.50 | K | NIST |
| Tboil | 331.25 ± 0.60 | K | NIST |
| Tboil | 331.80 ± 1.00 | K | NIST |
| Tc | [493.00; 501.00] | K |
|
| Tc | 501.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 493.00 | K | KDB |
| Tfus | [132.00; 132.36] | K |
|
| Tfus | 132.36 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 132.00 | K | KDB |
| Ttriple | 132.35 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 3.64 | ChemSep v8.3 pure component data Compiled value | |
| URi | 4.27 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.346; 0.360] | m3/kmol |
|
| Vc | 0.346 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.360 | m3/kmol | KDB |
| Zc | [0.2669880; 0.2670000] |
|
|
| Zc | 0.2670000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2669880 | KDB | |
| Zra | 0.27 | ChemSep v8.3 pure component data Compiled value |
Cheméo can also estimate Log10 of Water solubility in mol/l for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [27.95; 31.20] | kJ/mol | [303.00; 331.70] |
|
| ΔvapH | 31.20 | kJ/mol | 303.00 | NIST |
| ΔvapH | 27.95 | kJ/mol | 331.70 | KDB |
| n0 | 1.38583 | 298.15 | KDB | |
| ρl | 669.00 | kg/m3 | 293.00 | KDB |
| γ | 0.02 | N/m | 298.20 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [111.91; 345.29] | 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 | 9.53770e+01 | |||
| Coefficient B | -6.22830e+02 | |||
| Coefficient C | 5.90624e+00 | |||
| Coefficient D | 7.45450e-05 | |||
| Coefficient E | -3.63180e-08 | |||
| Temperature range, min. | 200.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 111.91 | J/mol×K | 200.00 | Calculated Property |
| Cp,gas | 156.90 | J/mol×K | 344.44 | Calculated Property |
| Cp,gas | 201.02 | J/mol×K | 488.89 | Calculated Property |
| Cp,gas | 237.33 | J/mol×K | 633.33 | Calculated Property |
| Cp,gas | 266.34 | J/mol×K | 777.78 | Calculated Property |
| Cp,gas | 289.55 | J/mol×K | 922.22 | Calculated Property |
| Cp,gas | 308.22 | J/mol×K | 1066.67 | Calculated Property |
| Cp,gas | 323.30 | J/mol×K | 1211.11 | Calculated Property |
| Cp,gas | 335.49 | J/mol×K | 1355.56 | Calculated Property |
| Cp,gas | 345.29 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [127.76; 203.21] | J/mol×K | [132.35; 331.75] |
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 | 2.22790e+01 | |||
| Coefficient B | 6.50610e+00 | |||
| Coefficient C | 3.95124e+00 | |||
| Coefficient D | 5.81820e-03 | |||
| Coefficient E | -6.38700e-06 | |||
| Temperature range, min. | 132.35 | |||
| Temperature range, max. | 331.75 | |||
| Cp,liquid | 127.76 | J/mol×K | 132.35 | Calculated Property |
| Cp,liquid | 136.69 | J/mol×K | 154.51 | Calculated Property |
| Cp,liquid | 145.82 | J/mol×K | 176.66 | Calculated Property |
| Cp,liquid | 155.00 | J/mol×K | 198.82 | Calculated Property |
| Cp,liquid | 164.09 | J/mol×K | 220.97 | Calculated Property |
| Cp,liquid | 172.94 | J/mol×K | 243.13 | Calculated Property |
| Cp,liquid | 181.41 | J/mol×K | 265.28 | Calculated Property |
| Cp,liquid | 189.37 | J/mol×K | 287.44 | Calculated Property |
| Cp,liquid | 196.68 | J/mol×K | 309.59 | Calculated Property |
| Cp,liquid | 203.21 | J/mol×K | 331.75 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0075877; 0.0001268] | Pa×s | [132.35; 405.00] |
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 | -1.10380e+01 | |||
| Coefficient B | 8.05550e+02 | |||
| Coefficient C | 1.46400e-02 | |||
| Coefficient D | -7.23590e-08 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 132.35 | |||
| Temperature range, max. | 405.00 | |||
| η | 0.0075877 | Pa×s | 132.35 | Calculated Property |
| η | 0.0024478 | Pa×s | 162.64 | Calculated Property |
| η | 0.0011267 | Pa×s | 192.94 | Calculated Property |
| η | 0.0006401 | Pa×s | 223.23 | Calculated Property |
| η | 0.0004162 | Pa×s | 253.53 | Calculated Property |
| η | 0.0002967 | Pa×s | 283.82 | Calculated Property |
| η | 0.0002257 | Pa×s | 314.12 | Calculated Property |
| η | 0.0001801 | Pa×s | 344.41 | Calculated Property |
| η | 0.0001490 | Pa×s | 374.71 | Calculated Property |
| η | 0.0001268 | Pa×s | 405.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [39.90; 0.00] | kJ/mol | [132.35; 501.00] |
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 | 5.39850e+01 | |||
| Coefficient B | 1.49660e+00 | |||
| Coefficient C | -2.47840e+00 | |||
| Coefficient D | 2.28570e+00 | |||
| Coefficient E | -8.59910e-01 | |||
| Critical temperature, Tc (K) | 5.01000e+02 | |||
| Temperature range, min. | 132.35 | |||
| Temperature range, max. | 501.00 | |||
| ΔvapH | 39.90 | kJ/mol | 132.35 | Calculated Property |
| ΔvapH | 37.20 | kJ/mol | 173.31 | Calculated Property |
| ΔvapH | 34.79 | kJ/mol | 214.27 | Calculated Property |
| ΔvapH | 32.48 | kJ/mol | 255.23 | Calculated Property |
| ΔvapH | 30.11 | kJ/mol | 296.19 | Calculated Property |
| ΔvapH | 27.55 | kJ/mol | 337.16 | Calculated Property |
| ΔvapH | 24.63 | kJ/mol | 378.12 | Calculated Property |
| ΔvapH | 21.07 | kJ/mol | 419.08 | Calculated Property |
| ΔvapH | 16.14 | kJ/mol | 460.04 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 501.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [238.98; 355.05] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.41425e+01 | |||
| Coefficient B | -2.82675e+03 | |||
| Coefficient C | -3.49530e+01 | |||
| Temperature range, min. | 238.98 | |||
| Temperature range, max. | 355.05 | |||
| Pvap | 1.33 | kPa | 238.98 | Calculated Property |
| Pvap | 3.04 | kPa | 251.88 | Calculated Property |
| Pvap | 6.31 | kPa | 264.77 | Calculated Property |
| Pvap | 12.14 | kPa | 277.67 | Calculated Property |
| Pvap | 21.84 | kPa | 290.57 | Calculated Property |
| Pvap | 37.15 | kPa | 303.46 | Calculated Property |
| Pvap | 60.19 | kPa | 316.36 | Calculated Property |
| Pvap | 93.47 | kPa | 329.26 | Calculated Property |
| Pvap | 139.89 | kPa | 342.15 | Calculated Property |
| Pvap | 202.67 | kPa | 355.05 | Calculated Property |
| Pvap | [3.52e-07; 3219.55] | kPa | [132.35; 501.00] |
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 | 7.47832e+01 | |||
| Coefficient B | -5.97280e+03 | |||
| Coefficient C | -9.14080e+00 | |||
| Coefficient D | 8.12850e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 132.35 | |||
| Temperature range, max. | 501.00 | |||
| Pvap | 3.52e-07 | kPa | 132.35 | Calculated Property |
| Pvap | 1.42e-03 | kPa | 173.31 | Calculated Property |
| Pvap | 0.17 | kPa | 214.27 | Calculated Property |
| Pvap | 3.50 | kPa | 255.23 | Calculated Property |
| Pvap | 27.41 | kPa | 296.19 | Calculated Property |
| Pvap | 120.01 | kPa | 337.16 | Calculated Property |
| Pvap | 363.84 | kPa | 378.12 | Calculated Property |
| Pvap | 867.75 | kPa | 419.08 | Calculated Property |
| Pvap | 1763.73 | kPa | 460.04 | Calculated Property |
| Pvap | 3219.55 | kPa | 501.00 | Calculated Property |
| Pvap | [3.45e-07; 3216.52] | kPa | [132.35; 501.00] |
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 | 7.48595e+01 | |||
| Coefficient B | -5.97972e+03 | |||
| Coefficient C | -9.14972e+00 | |||
| Coefficient D | 8.09678e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 132.35 | |||
| Temperature range, max. | 501.00 | |||
| Pvap | 3.45e-07 | kPa | 132.35 | Calculated Property |
| Pvap | 1.41e-03 | kPa | 173.31 | Calculated Property |
| Pvap | 0.17 | kPa | 214.27 | Calculated Property |
| Pvap | 3.49 | kPa | 255.23 | Calculated Property |
| Pvap | 27.39 | kPa | 296.19 | Calculated Property |
| Pvap | 120.04 | kPa | 337.16 | Calculated Property |
| Pvap | 364.02 | kPa | 378.12 | Calculated Property |
| Pvap | 868.05 | kPa | 419.08 | Calculated Property |
| Pvap | 1763.45 | kPa | 460.04 | Calculated Property |
| Pvap | 3216.52 | kPa | 501.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [801.67; 241.31] | kg/m3 | [132.35; 501.00] |
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 | 6.50730e+01 | |||
| Coefficient B | 2.69660e-01 | |||
| Coefficient C | 5.01000e+02 | |||
| Coefficient D | 2.85780e-01 | |||
| Temperature range, min. | 132.35 | |||
| Temperature range, max. | 501.00 | |||
| ρl | 801.67 | kg/m3 | 132.35 | Calculated Property |
| ρl | 770.43 | kg/m3 | 173.31 | Calculated Property |
| ρl | 737.67 | kg/m3 | 214.27 | Calculated Property |
| ρl | 702.98 | kg/m3 | 255.23 | Calculated Property |
| ρl | 665.84 | kg/m3 | 296.19 | Calculated Property |
| ρl | 625.37 | kg/m3 | 337.16 | Calculated Property |
| ρl | 580.09 | kg/m3 | 378.12 | Calculated Property |
| ρl | 527.01 | kg/m3 | 419.08 | Calculated Property |
| ρl | 457.99 | kg/m3 | 460.04 | Calculated Property |
| ρl | 241.31 | kg/m3 | 501.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 1.54e-05] | N/m | [132.35; 496.58] |
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 | -8.86500e-03 | |||
| Coefficient B | 2.80190e+01 | |||
| Coefficient C | -3.27950e+00 | |||
| Coefficient D | 2.91390e-04 | |||
| Coefficient E | -6.67320e-06 | |||
| Comment | Range stopped where the equation turns negative; ChemSep gives it to 501 K. | |||
| Temperature range, min. | 132.35 | |||
| Temperature range, max. | 496.58 | |||
| γ | 0.03 | N/m | 132.35 | Calculated Property |
| γ | 0.03 | N/m | 172.82 | Calculated Property |
| γ | 0.02 | N/m | 213.29 | Calculated Property |
| γ | 0.02 | N/m | 253.76 | Calculated Property |
| γ | 0.02 | N/m | 294.23 | Calculated Property |
| γ | 0.01 | N/m | 334.70 | Calculated Property |
| γ | 0.01 | N/m | 375.17 | Calculated Property |
| γ | 0.01 | N/m | 415.64 | Calculated Property |
| γ | 0.00 | N/m | 456.11 | Calculated Property |
| γ | 1.54e-05 | N/m | 496.58 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.00; 0.10] | W/m×K | [132.35; 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 | 6.23480e-05 | |||
| Coefficient B | 1.07720e+00 | |||
| Coefficient C | -1.74790e+01 | |||
| Coefficient D | 1.16240e+05 | |||
| Temperature range, min. | 132.35 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.00 | W/m×K | 132.35 | Calculated Property |
| λgas | 0.01 | W/m×K | 228.76 | Calculated Property |
| λgas | 0.02 | W/m×K | 325.16 | Calculated Property |
| λgas | 0.03 | W/m×K | 421.57 | Calculated Property |
| λgas | 0.04 | W/m×K | 517.97 | Calculated Property |
| λgas | 0.05 | W/m×K | 614.38 | Calculated Property |
| λgas | 0.06 | W/m×K | 710.78 | Calculated Property |
| λgas | 0.07 | W/m×K | 807.19 | Calculated Property |
| λgas | 0.08 | W/m×K | 903.59 | Calculated Property |
| λgas | 0.10 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.15; 0.10] | W/m×K | [132.35; 331.75] |
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 | -2.24100e-02 | |||
| Coefficient B | 4.54230e+00 | |||
| Coefficient C | -1.70380e+00 | |||
| Coefficient D | -4.84450e-04 | |||
| Coefficient E | -2.48340e-06 | |||
| Temperature range, min. | 132.35 | |||
| Temperature range, max. | 331.75 | |||
| λliquid | 0.15 | W/m×K | 132.35 | Calculated Property |
| λliquid | 0.14 | W/m×K | 154.51 | Calculated Property |
| λliquid | 0.14 | W/m×K | 176.66 | Calculated Property |
| λliquid | 0.13 | W/m×K | 198.82 | Calculated Property |
| λliquid | 0.13 | W/m×K | 220.97 | Calculated Property |
| λliquid | 0.12 | W/m×K | 243.13 | Calculated Property |
| λliquid | 0.11 | W/m×K | 265.28 | Calculated Property |
| λliquid | 0.11 | W/m×K | 287.44 | Calculated Property |
| λliquid | 0.10 | W/m×K | 309.59 | Calculated Property |
| λliquid | 0.10 | W/m×K | 331.75 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Pentene, 4-methyl-, (E)-.
Sources
- KDB Vapor Pressure Data
- 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
- Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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