- 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
- 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).
- 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 |
|---|---|---|---|
| ΔcH°liquid | -4655.37 ± 0.50 | kJ/mol | NIST |
| ΔfG° | 93.46 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -67.66 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 9.08 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 34.30 | kJ/mol | NIST |
| log10WS | -2.36 | Crippen 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 | Outlier 661.00 | NIST | |
| Inp | 655.50 | NIST | |
| Inp | 649.30 | NIST | |
| Tboil | 355.80 | K | Joback Calculated Property |
| Tc | 528.70 | K | Gas-Liq... |
| Tfus | 151.89 | K | Joback Calculated Property |
| Vc | 0.403 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [180.32; 243.44] | J/mol×K | [355.80; 526.72] |
|
| Cp,gas | 180.32 | J/mol×K | 355.80 | Joback Calculated Property |
| Cp,gas | 191.94 | J/mol×K | 384.29 | Joback Calculated Property |
| Cp,gas | 203.10 | J/mol×K | 412.77 | Joback Calculated Property |
| Cp,gas | 213.82 | J/mol×K | 441.26 | Joback Calculated Property |
| Cp,gas | 224.10 | J/mol×K | 469.74 | Joback Calculated Property |
| Cp,gas | 233.97 | J/mol×K | 498.23 | Joback Calculated Property |
| Cp,gas | 243.44 | J/mol×K | 526.72 | Joback Calculated Property |
| η | [0.0002256; 0.0078928] | Pa×s | [151.89; 355.80] |
|
| η | 0.0078928 | Pa×s | 151.89 | Joback Calculated Property |
| η | 0.0025390 | Pa×s | 185.88 | Joback Calculated Property |
| η | 0.0011597 | Pa×s | 219.86 | Joback Calculated Property |
| η | 0.0006534 | Pa×s | 253.84 | Joback Calculated Property |
| η | 0.0004215 | Pa×s | 287.83 | Joback Calculated Property |
| η | 0.0002983 | Pa×s | 321.82 | Joback Calculated Property |
| η | 0.0002256 | Pa×s | 355.80 | Joback Calculated Property |
| ΔvapH | 33.50 | kJ/mol | 353.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.62] | kPa | [261.07; 383.00] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| 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
- 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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Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.