- InChI
- InChI=1S/C7H14/c1-4-5-6-7(2)3/h4,7H,1,5-6H2,2-3H3
- InChI Key
- JIUFYGIESXPUPL-UHFFFAOYSA-N
- Formula
- C7H14
- SMILES
- C=CCCC(C)C
- Molecular Weight1
- 98.19
- CAS
- 3524-73-0
- Other Names
-
- 5-methyl-1-hexene
- 5-methylhex-1-ene
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (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).
- 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).
- Pvap : Vapor pressure (kPa).
- Inp : Non-polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.2687 | Relay (1.0) Calculated Property | |
| ΔcH°liquid | -4655.37 ± 0.50 | kJ/mol | NIST |
| ΔfG° | 93.46 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -73.25 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 9.08 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 34.30 | kJ/mol | NIST |
| IE | 9.51 | eV | Relay (1.0) Calculated Property |
| log10WS | -3.69 | Relay (1.0) Calculated Property | |
| logPoct/wat | 2.609 | Crippen Calculated Property | |
| McVol | 105.190 | ml/mol | McGowan Calculated Property |
| Pc | 2953.69 | kPa | Joback Calculated Property |
| Inp | [639.40; 661.00] |
|
|
| Inp | 656.40 | NIST | |
| Inp | 649.00 | NIST | |
| Inp | 649.00 | NIST | |
| Inp | 657.00 | NIST | |
| Inp | 657.00 | NIST | |
| Inp | 650.60 | NIST | |
| Inp | 650.00 | NIST | |
| Inp | 650.00 | NIST | |
| Inp | 652.00 | NIST | |
| Inp | 652.00 | NIST | |
| Inp | 650.00 | NIST | |
| Inp | 651.00 | NIST | |
| Inp | 654.00 | NIST | |
| Inp | 649.00 | NIST | |
| Inp | 651.00 | NIST | |
| Inp | 652.00 | NIST | |
| Inp | 652.00 | NIST | |
| Inp | 655.50 | NIST | |
| Inp | Outlier 639.40 | NIST | |
| Inp | 658.20 | NIST | |
| Inp | 649.00 | NIST | |
| Inp | Outlier 661.00 | NIST | |
| Inp | 649.30 | NIST | |
| Inp | 650.00 | NIST | |
| Inp | 651.00 | NIST | |
| Inp | 646.00 | NIST | |
| Inp | 653.00 | NIST | |
| Inp | 652.00 | NIST | |
| Inp | 657.00 | NIST | |
| Inp | 652.00 | NIST | |
| Inp | 654.00 | NIST | |
| Inp | 655.50 | NIST | |
| Inp | 649.30 | NIST | |
| Inp | Outlier 661.00 | NIST | |
| Tboil | [355.65; 374.00] | K |
|
| Tboil | 358.50 | K | NIST |
| Tboil | Outlier 374.00 ± 2.00 | K | NIST |
| Tboil | 358.65 ± 2.00 | K | NIST |
| Tboil | 358.65 ± 0.50 | K | NIST |
| Tboil | 358.56 ± 0.30 | K | NIST |
| Tboil | 358.56 ± 0.50 | K | NIST |
| Tboil | 358.65 ± 0.50 | K | NIST |
| Tboil | 358.55 ± 0.30 | K | NIST |
| Tboil | 358.80 ± 0.30 | K | NIST |
| Tboil | 357.75 ± 0.50 | K | NIST |
| Tboil | 357.85 ± 0.70 | K | NIST |
| Tboil | 358.90 ± 0.60 | K | NIST |
| Tboil | 357.85 ± 0.50 | K | NIST |
| Tboil | 358.15 ± 2.00 | K | NIST |
| Tboil | 355.65 ± 3.00 | K | NIST |
| Tboil | 358.65 ± 1.00 | K | NIST |
| Tc | 528.70 | K | Gas-Liquid Critical Temperatures of Some Alkenes, Amines, and Cyclic Hydrocarbons |
| Tfus | 135.76 | K | Relay (1.0) Calculated Property |
| Vc | 0.384 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 33.50 | kJ/mol | 353.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [143.85; 352.49] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | -8.14800e+00 | |||
| Coefficient B | 6.54740e-01 | |||
| Coefficient C | -3.83100e-04 | |||
| Coefficient D | 8.90000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 143.85 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 179.48 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 211.33 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 239.70 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 264.87 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 287.11 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 306.71 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 323.96 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 339.12 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 352.49 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0078928; 0.0002036] | Pa×s | [151.89; 370.09] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.10451e+01 | |||
| Coefficient B | 9.42220e+02 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 151.89 | |||
| Temperature range, max. | 370.09 | |||
| η | 0.0078928 | Pa×s | 151.89 | Calculated Property |
| η | 0.0033605 | Pa×s | 176.13 | Calculated Property |
| η | 0.0017592 | Pa×s | 200.38 | Calculated Property |
| η | 0.0010590 | Pa×s | 224.62 | Calculated Property |
| η | 0.0007038 | Pa×s | 248.87 | Calculated Property |
| η | 0.0005029 | Pa×s | 273.11 | Calculated Property |
| η | 0.0003796 | Pa×s | 297.36 | Calculated Property |
| η | 0.0002989 | Pa×s | 321.60 | Calculated Property |
| η | 0.0002434 | Pa×s | 345.85 | Calculated Property |
| η | 0.0002036 | Pa×s | 370.09 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.62] | kPa | [261.07; 383.00] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.40537e+01 | |||
| Coefficient B | -2.92081e+03 | |||
| Coefficient C | -4.88990e+01 | |||
| Temperature range, min. | 261.07 | |||
| Temperature range, max. | 383.00 | |||
| Pvap | 1.33 | kPa | 261.07 | Calculated Property |
| Pvap | 3.05 | kPa | 274.62 | Calculated Property |
| Pvap | 6.34 | kPa | 288.17 | Calculated Property |
| Pvap | 12.19 | kPa | 301.71 | Calculated Property |
| Pvap | 21.94 | kPa | 315.26 | Calculated Property |
| Pvap | 37.29 | kPa | 328.81 | Calculated Property |
| Pvap | 60.37 | kPa | 342.36 | Calculated Property |
| Pvap | 93.67 | kPa | 355.90 | Calculated Property |
| Pvap | 140.03 | kPa | 369.45 | Calculated Property |
| Pvap | 202.62 | kPa | 383.00 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Hexene, 5-methyl-.
Sources
- Cheméo Relay (1.0)
- 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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