- InChI
- InChI=1S/C6H12/c1-3-5-6-4-2/h3,5H,4,6H2,1-2H3/b5-3+
- InChI Key
- RYPKRALMXUUNKS-HWKANZROSA-N
- Formula
- C6H12
- SMILES
- CC=CCCC
- Molecular Weight1
- 84.16
- CAS
- 4050-45-7
- Other Names
-
- (E)-2-C6H12
- (E)-2-hexene
- trans-2-hexene
- trans-hex-2-ene
- 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).
- 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).
- 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 | [0.2420; 0.2990] |
|
|
| ω | 0.2990 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.2886 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.2420 | KDB | |
| AP | 299.150 | K | KDB |
| μ | 0.00 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | [76.49; 76.75] | kJ/mol |
|
| ΔfG° | 76.75 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | 76.49 | kJ/mol | KDB |
| Δc,grossH | 3990.57 | kJ/mol | KDB |
| Δc,netH | 3726.480 | kJ/mol | KDB |
| ΔfH°gas | [-55.80; -51.00] | kJ/mol |
|
| ΔfH°gas | -53.81 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -53.93 | kJ/mol | KDB |
| ΔfH°gas | -51.00 ± 0.80 | kJ/mol | NIST |
| ΔfH°gas | -52.10 ± 1.00 | kJ/mol | NIST |
| ΔfH°gas | -52.50 | kJ/mol | NIST |
| ΔfH°gas | -51.60 ± 0.80 | kJ/mol | NIST |
| ΔfH°gas | -55.80 ± 1.30 | kJ/mol | NIST |
| ΔfH°liquid | [-87.40; -82.60] | kJ/mol |
|
| ΔfH°liquid | -82.60 ± 0.80 | kJ/mol | NIST |
| ΔfH°liquid | -83.70 ± 1.00 | kJ/mol | NIST |
| ΔfH°liquid | -83.22 ± 0.84 | kJ/mol | NIST |
| ΔfH°liquid | -87.40 ± 1.30 | kJ/mol | NIST |
| ΔfusH° | 11.50 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [31.50; 32.20] | kJ/mol |
|
| ΔvapH° | 32.20 | kJ/mol | NIST |
| ΔvapH° | 31.60 | kJ/mol | NIST |
| ΔvapH° | 31.50 | kJ/mol | NIST |
| ΔvapH° | 31.50 | kJ/mol | NIST |
| IE | [8.93; 9.16] | eV |
|
| IE | 8.97 ± 0.02 | eV | NIST |
| IE | 8.93 | eV | NIST |
| IE | 8.97 ± 0.01 | eV | NIST |
| IE | 9.16 ± 0.01 | eV | NIST |
| logPoct/wat | 2.363 | Crippen Calculated Property | |
| McVol | 91.100 | ml/mol | McGowan Calculated Property |
| Pc | [3120.81; 3270.00] | kPa |
|
| Pc | 3120.81 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 3168.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 3270.00 | kPa | KDB |
| Ptriple | 1.79e-06 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [596.00; 613.00] |
|
|
| Inp | 604.90 | NIST | |
| Inp | 596.80 | NIST | |
| Inp | 596.00 | NIST | |
| Inp | 609.00 | NIST | |
| Inp | 607.00 | NIST | |
| Inp | 607.00 | NIST | |
| Inp | 607.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 606.00 | NIST | |
| Inp | 596.90 | NIST | |
| Inp | 596.70 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 596.60 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 597.30 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 596.60 | NIST | |
| Inp | 596.00 | NIST | |
| Inp | 596.00 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 606.50 | NIST | |
| Inp | 596.80 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 596.40 | NIST | |
| Inp | 596.70 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | Outlier 613.00 | NIST | |
| Inp | 596.00 | NIST | |
| Inp | 605.50 | NIST | |
| Inp | 606.00 | NIST | |
| Inp | 604.60 | NIST | |
| Inp | 606.00 | NIST | |
| Inp | 603.38 | NIST | |
| Inp | 603.43 | NIST | |
| Inp | 603.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 596.90 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | Outlier 613.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 596.00 | NIST | |
| Inp | 606.00 | NIST | |
| Inp | 603.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 607.00 | NIST | |
| Inp | 607.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 596.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 604.60 | NIST | |
| Inp | 604.90 | NIST | |
| Inp | 607.00 | NIST | |
| Inp | 606.00 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 596.60 | NIST | |
| Inp | 596.80 | NIST | |
| Inp | Outlier 613.00 | NIST | |
| Inp | 596.90 | NIST | |
| Inp | 605.50 | NIST | |
| Ip | [648.00; 663.40] |
|
|
| Ip | 663.00 | NIST | |
| Ip | 663.00 | NIST | |
| Ip | 663.40 | NIST | |
| Ip | 663.40 | NIST | |
| Ip | 663.40 | NIST | |
| Ip | 663.40 | NIST | |
| Ip | 660.00 | NIST | |
| Ip | Outlier 648.00 | NIST | |
| Ip | 663.00 | NIST | |
| Ip | 663.40 | NIST | |
| Tboil | [339.15; 341.25] | K |
|
| Tboil | 341.02 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 341.00 | K | KDB |
| Tboil | 341.10 | K | NIST |
| Tboil | 341.10 ± 0.40 | K | NIST |
| Tboil | 340.24 ± 0.20 | K | NIST |
| Tboil | 341.02 ± 0.30 | K | NIST |
| Tboil | Outlier 339.15 ± 2.00 | K | NIST |
| Tboil | 341.06 ± 0.30 | K | NIST |
| Tboil | 340.27 ± 0.40 | K | NIST |
| Tboil | 340.28 ± 0.30 | K | NIST |
| Tboil | 341.06 ± 0.40 | K | NIST |
| Tboil | 341.23 ± 0.40 | K | NIST |
| Tboil | 341.23 ± 0.50 | K | NIST |
| Tboil | 341.23 ± 0.30 | K | NIST |
| Tboil | 341.25 ± 0.50 | K | NIST |
| Tc | [508.00; 516.00] | K |
|
| Tc | 509.00 | K | Gas-Liquid Critical Temperatures of Some Alkenes, Amines, and Cyclic Hydrocarbons |
| Tc | 508.00 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 509.80 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 516.00 | K | KDB |
| Tfus | [139.65; 140.17] | K |
|
| Tfus | 140.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 140.17 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 140.00 | K | KDB |
| Tfus | 140.17 ± 0.04 | K | NIST |
| Tfus | 140.08 ± 0.20 | K | NIST |
| Tfus | 139.99 ± 0.40 | K | NIST |
| Tfus | 139.75 ± 0.40 | K | NIST |
| Tfus | 139.75 ± 0.60 | K | NIST |
| Tfus | 139.65 ± 1.50 | K | NIST |
| Ttriple | 140.17 | 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 | [0.345; 0.351] | m3/kmol |
|
| Vc | 0.351 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.345 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.351 | m3/kmol | KDB |
| Zc | [0.2580000; 0.2675280] |
|
|
| Zc | 0.2580000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2675280 | KDB | |
| Zra | 0.26 | 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 | 28.91 | kJ/mol | 341.00 | KDB |
| n0 | 1.39073 | 298.15 | KDB | |
| ρl | 678.00 | kg/m3 | 293.00 | KDB |
| γ | 0.02 | N/m | 298.20 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [107.58; 346.62] | 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 | 9.68390e+01 | |||
| Coefficient B | -7.58810e+02 | |||
| Coefficient C | 6.20424e+00 | |||
| Coefficient D | -1.89110e-04 | |||
| Coefficient E | 4.70570e-08 | |||
| Temperature range, min. | 200.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 107.58 | J/mol×K | 200.00 | Calculated Property |
| Cp,gas | 148.34 | J/mol×K | 344.44 | Calculated Property |
| Cp,gas | 193.47 | J/mol×K | 488.89 | Calculated Property |
| Cp,gas | 231.83 | J/mol×K | 633.33 | Calculated Property |
| Cp,gas | 262.51 | J/mol×K | 777.78 | Calculated Property |
| Cp,gas | 286.85 | J/mol×K | 922.22 | Calculated Property |
| Cp,gas | 306.33 | J/mol×K | 1066.67 | Calculated Property |
| Cp,gas | 322.20 | J/mol×K | 1211.11 | Calculated Property |
| Cp,gas | 335.39 | J/mol×K | 1355.56 | Calculated Property |
| Cp,gas | 346.62 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [158.03; 196.03] | J/mol×K | [140.17; 341.02] |
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 | 1.45330e+02 | |||
| Coefficient B | 5.91610e+02 | |||
| Coefficient C | -6.45691e+00 | |||
| Coefficient D | 4.01760e-02 | |||
| Coefficient E | -4.34490e-05 | |||
| Temperature range, min. | 140.17 | |||
| Temperature range, max. | 341.02 | |||
| Cp,liquid | 158.03 | J/mol×K | 140.17 | Calculated Property |
| Cp,liquid | 158.33 | J/mol×K | 162.49 | Calculated Property |
| Cp,liquid | 159.99 | J/mol×K | 184.80 | Calculated Property |
| Cp,liquid | 162.74 | J/mol×K | 207.12 | Calculated Property |
| Cp,liquid | 166.49 | J/mol×K | 229.44 | Calculated Property |
| Cp,liquid | 171.22 | J/mol×K | 251.75 | Calculated Property |
| Cp,liquid | 176.80 | J/mol×K | 274.07 | Calculated Property |
| Cp,liquid | 183.04 | J/mol×K | 296.39 | Calculated Property |
| Cp,liquid | 189.61 | J/mol×K | 318.70 | Calculated Property |
| Cp,liquid | 196.03 | J/mol×K | 341.02 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0053389; 0.0001940] | Pa×s | [140.17; 341.02] |
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 | -1.12960e+01 | |||
| Coefficient B | 7.98850e+02 | |||
| Coefficient C | 7.46880e-02 | |||
| Coefficient D | -2.57650e-07 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 140.17 | |||
| Temperature range, max. | 341.02 | |||
| η | 0.0053389 | Pa×s | 140.17 | Calculated Property |
| η | 0.0024634 | Pa×s | 162.49 | Calculated Property |
| η | 0.0013709 | Pa×s | 184.80 | Calculated Property |
| η | 0.0008659 | Pa×s | 207.12 | Calculated Property |
| η | 0.0005981 | Pa×s | 229.44 | Calculated Property |
| η | 0.0004411 | Pa×s | 251.75 | Calculated Property |
| η | 0.0003418 | Pa×s | 274.07 | Calculated Property |
| η | 0.0002751 | Pa×s | 296.39 | Calculated Property |
| η | 0.0002282 | Pa×s | 318.70 | Calculated Property |
| η | 0.0001940 | Pa×s | 341.02 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [38.09; 12.59] | kJ/mol | [140.17; 490.35] |
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 | 4.40220e+01 | |||
| Coefficient B | 5.63356e-01 | |||
| Coefficient C | -4.97314e-01 | |||
| Coefficient D | 3.06975e-01 | |||
| Coefficient E | 1.61359e-02 | |||
| Critical temperature, Tc (K) | 5.09800e+02 | |||
| Temperature range, min. | 140.17 | |||
| Temperature range, max. | 490.35 | |||
| ΔvapH | 38.09 | kJ/mol | 140.17 | Calculated Property |
| ΔvapH | 36.59 | kJ/mol | 179.08 | Calculated Property |
| ΔvapH | 35.06 | kJ/mol | 217.99 | Calculated Property |
| ΔvapH | 33.43 | kJ/mol | 256.90 | Calculated Property |
| ΔvapH | 31.62 | kJ/mol | 295.81 | Calculated Property |
| ΔvapH | 29.53 | kJ/mol | 334.71 | Calculated Property |
| ΔvapH | 27.01 | kJ/mol | 373.62 | Calculated Property |
| ΔvapH | 23.83 | kJ/mol | 412.53 | Calculated Property |
| ΔvapH | 19.53 | kJ/mol | 451.44 | Calculated Property |
| ΔvapH | 12.59 | kJ/mol | 490.35 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.68] | kPa | [246.08; 364.88] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.41268e+01 | |||
| Coefficient B | -2.88478e+03 | |||
| Coefficient C | -3.76300e+01 | |||
| Temperature range, min. | 246.08 | |||
| Temperature range, max. | 364.88 | |||
| Pvap | 1.33 | kPa | 246.08 | Calculated Property |
| Pvap | 3.04 | kPa | 259.28 | Calculated Property |
| Pvap | 6.32 | kPa | 272.48 | Calculated Property |
| Pvap | 12.15 | kPa | 285.68 | Calculated Property |
| Pvap | 21.86 | kPa | 298.88 | Calculated Property |
| Pvap | 37.18 | kPa | 312.08 | Calculated Property |
| Pvap | 60.22 | kPa | 325.28 | Calculated Property |
| Pvap | 93.51 | kPa | 338.48 | Calculated Property |
| Pvap | 139.92 | kPa | 351.68 | Calculated Property |
| Pvap | 202.68 | kPa | 364.88 | Calculated Property |
| Pvap | [5.46e-07; 3168.00] | kPa | [140.17; 500.99] |
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 | 9.58535e+01 | |||
| Coefficient B | -6.85825e+03 | |||
| Coefficient C | -1.24647e+01 | |||
| Coefficient D | 1.34849e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | Range stopped where the equation exceeds Pc; ChemSep gives it to 509.8 K. | |||
| Temperature range, min. | 140.17 | |||
| Temperature range, max. | 500.99 | |||
| Pvap | 5.46e-07 | kPa | 140.17 | Calculated Property |
| Pvap | 1.50e-03 | kPa | 180.26 | Calculated Property |
| Pvap | 0.15 | kPa | 220.35 | Calculated Property |
| Pvap | 3.01 | kPa | 260.44 | Calculated Property |
| Pvap | 22.95 | kPa | 300.53 | Calculated Property |
| Pvap | 99.97 | kPa | 340.62 | Calculated Property |
| Pvap | 307.39 | kPa | 380.71 | Calculated Property |
| Pvap | 757.26 | kPa | 420.80 | Calculated Property |
| Pvap | 1619.25 | kPa | 460.90 | Calculated Property |
| Pvap | 3168.00 | kPa | 500.99 | Calculated Property |
| Pvap | [8.22e-07; 3151.45] | kPa | [140.17; 513.00] |
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 | 7.51774e+01 | |||
| Coefficient B | -6.19923e+03 | |||
| Coefficient C | -9.12514e+00 | |||
| Coefficient D | 7.24225e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 140.17 | |||
| Temperature range, max. | 513.00 | |||
| Pvap | 8.22e-07 | kPa | 140.17 | Calculated Property |
| Pvap | 2.05e-03 | kPa | 181.60 | Calculated Property |
| Pvap | 0.20 | kPa | 223.02 | Calculated Property |
| Pvap | 3.84 | kPa | 264.45 | Calculated Property |
| Pvap | 28.87 | kPa | 305.87 | Calculated Property |
| Pvap | 123.62 | kPa | 347.30 | Calculated Property |
| Pvap | 369.45 | kPa | 388.72 | Calculated Property |
| Pvap | 870.87 | kPa | 430.15 | Calculated Property |
| Pvap | 1749.37 | kPa | 471.57 | Calculated Property |
| Pvap | 3151.45 | kPa | 513.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [802.58; 243.91] | kg/m3 | [140.17; 509.80] |
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 | 6.60989e+01 | |||
| Coefficient B | 2.71000e-01 | |||
| Coefficient C | 5.09800e+02 | |||
| Coefficient D | 2.85710e-01 | |||
| Temperature range, min. | 140.17 | |||
| Temperature range, max. | 509.80 | |||
| ρl | 802.58 | kg/m3 | 140.17 | Calculated Property |
| ρl | 771.56 | kg/m3 | 181.24 | Calculated Property |
| ρl | 739.01 | kg/m3 | 222.31 | Calculated Property |
| ρl | 704.54 | kg/m3 | 263.38 | Calculated Property |
| ρl | 667.61 | kg/m3 | 304.45 | Calculated Property |
| ρl | 627.36 | kg/m3 | 345.52 | Calculated Property |
| ρl | 582.29 | kg/m3 | 386.59 | Calculated Property |
| ρl | 529.42 | kg/m3 | 427.66 | Calculated Property |
| ρl | 460.61 | kg/m3 | 468.73 | Calculated Property |
| ρl | 243.91 | kg/m3 | 509.80 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 7.20e-04] | N/m | [140.17; 490.35] |
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 | -2.41830e-02 | |||
| Coefficient B | -3.21660e-01 | |||
| Coefficient C | -2.49940e+00 | |||
| Coefficient D | -1.83730e-03 | |||
| Coefficient E | -1.21350e-06 | |||
| Temperature range, min. | 140.17 | |||
| Temperature range, max. | 490.35 | |||
| γ | 0.04 | N/m | 140.17 | Calculated Property |
| γ | 0.03 | N/m | 179.08 | Calculated Property |
| γ | 0.03 | N/m | 217.99 | Calculated Property |
| γ | 0.02 | N/m | 256.90 | Calculated Property |
| γ | 0.02 | N/m | 295.81 | Calculated Property |
| γ | 0.01 | N/m | 334.71 | Calculated Property |
| γ | 0.01 | N/m | 373.62 | Calculated Property |
| γ | 0.01 | N/m | 412.53 | Calculated Property |
| γ | 0.00 | N/m | 451.44 | Calculated Property |
| γ | 7.20e-04 | N/m | 490.35 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.00; 0.09] | W/m×K | [140.17; 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 | 9.48530e-05 | |||
| Coefficient B | 1.01750e+00 | |||
| Coefficient C | 2.83660e+00 | |||
| Coefficient D | 1.54410e+05 | |||
| Temperature range, min. | 140.17 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.00 | W/m×K | 140.17 | Calculated Property |
| λgas | 0.01 | W/m×K | 235.71 | Calculated Property |
| λgas | 0.01 | W/m×K | 331.24 | Calculated Property |
| λgas | 0.02 | W/m×K | 426.78 | Calculated Property |
| λgas | 0.04 | W/m×K | 522.32 | Calculated Property |
| λgas | 0.05 | W/m×K | 617.85 | Calculated Property |
| λgas | 0.06 | W/m×K | 713.39 | Calculated Property |
| λgas | 0.07 | W/m×K | 808.93 | Calculated Property |
| λgas | 0.08 | W/m×K | 904.46 | Calculated Property |
| λgas | 0.09 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.17; 0.11] | W/m×K | [140.17; 341.02] |
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 | -9.10760e-02 | |||
| Coefficient B | -1.43520e-01 | |||
| Coefficient C | -1.19630e+00 | |||
| Coefficient D | -9.38010e-04 | |||
| Coefficient E | -7.12300e-07 | |||
| Temperature range, min. | 140.17 | |||
| Temperature range, max. | 341.02 | |||
| λliquid | 0.17 | W/m×K | 140.17 | Calculated Property |
| λliquid | 0.16 | W/m×K | 162.49 | Calculated Property |
| λliquid | 0.16 | W/m×K | 184.80 | Calculated Property |
| λliquid | 0.15 | W/m×K | 207.12 | Calculated Property |
| λliquid | 0.14 | W/m×K | 229.44 | Calculated Property |
| λliquid | 0.14 | W/m×K | 251.75 | Calculated Property |
| λliquid | 0.13 | W/m×K | 274.07 | Calculated Property |
| λliquid | 0.12 | W/m×K | 296.39 | Calculated Property |
| λliquid | 0.12 | W/m×K | 318.70 | Calculated Property |
| λliquid | 0.11 | W/m×K | 341.02 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Hexene, (E)-.
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).
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- 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
- Gas-Liquid Critical Temperatures of Some Alkenes, Amines, and Cyclic Hydrocarbons
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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