- InChI
- InChI=1S/C6H12O/c1-2-3-4-5-6-7/h3-4,7H,2,5-6H2,1H3/b4-3-
- InChI Key
- UFLHIIWVXFIJGU-ARJAWSKDSA-N
- Formula
- C6H12O
- SMILES
- CCC=CCCO
- Molecular Weight1
- 100.16
- Other Names
-
- cis-3-hexen-1-ol
- cis-3-hexenol
- 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).
- 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).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : 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 |
|---|---|---|---|
| ΔfG° | -56.96 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -202.18 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 15.59 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 45.59 | kJ/mol | Joback Calculated Property |
| log10WS | -1.45 | Crippen Calculated Property | |
| logPoct/wat | 1.335 | Crippen Calculated Property | |
| McVol | 96.970 | ml/mol | McGowan Calculated Property |
| Pc | 3673.09 | kPa | Joback Calculated Property |
| Inp | [833.00; 858.00] |
|
|
| Inp | 858.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 833.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 836.00 | NIST | |
| I | [1379.00; 1395.00] |
|
|
| I | 1379.00 | NIST | |
| I | 1395.00 | NIST | |
| I | 1392.00 | NIST | |
| I | 1390.00 | NIST | |
| I | 1387.00 | NIST | |
| I | 1389.00 | NIST | |
| I | 1393.00 | NIST | |
| I | 1394.00 | NIST | |
| I | 1385.00 | NIST | |
| I | 1385.00 | NIST | |
| I | 1379.00 | NIST | |
| Tboil | 433.02 | K | Joback Calculated Property |
| Tc | 601.76 | K | Joback Calculated Property |
| Tfus | 213.12 | K | Joback Calculated Property |
| Vc | 0.370 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [191.78; 240.99] | J/mol×K | [433.02; 601.76] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 190 200 210 220 230 240 450 500 550 600 | ||||
| Cp,gas | 191.78 | J/mol×K | 433.02 | Joback Calculated Property |
| Cp,gas | 200.94 | J/mol×K | 461.14 | Joback Calculated Property |
| Cp,gas | 209.69 | J/mol×K | 489.27 | Joback Calculated Property |
| Cp,gas | 218.06 | J/mol×K | 517.39 | Joback Calculated Property |
| Cp,gas | 226.05 | J/mol×K | 545.51 | Joback Calculated Property |
| Cp,gas | 233.69 | J/mol×K | 573.64 | Joback Calculated Property |
| Cp,gas | 240.99 | J/mol×K | 601.76 | Joback Calculated Property |
| η | [0.0002006; 0.0918576] | Pa×s | [213.12; 433.02] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 0.02 0.04 0.06 0.08 0.1 250 300 350 400 | ||||
| η | 0.0918576 | Pa×s | 213.12 | Joback Calculated Property |
| η | 0.0156415 | Pa×s | 249.77 | Joback Calculated Property |
| η | 0.0041899 | Pa×s | 286.42 | Joback Calculated Property |
| η | 0.0015133 | Pa×s | 323.07 | Joback Calculated Property |
| η | 0.0006726 | Pa×s | 359.72 | Joback Calculated Property |
| η | 0.0003473 | Pa×s | 396.37 | Joback Calculated Property |
| η | 0.0002006 | Pa×s | 433.02 | Joback Calculated Property |
| Pvap | [3.01e-04; 0.30] | kPa | [238.15; 308.15] |
|
|
T(K) Vapor pressure (kPa) 0 0.05 0.1 0.15 0.2 0.25 0.3 240 260 280 300 | ||||
| Pvap | 3.03e-04 | kPa | 238.15 | Vapor p... |
| Pvap | 3.04e-04 | kPa | 238.15 | Vapor p... |
| Pvap | 3.01e-04 | kPa | 238.15 | Vapor p... |
| Pvap | 5.80e-04 | kPa | 243.15 | Vapor p... |
| Pvap | 5.77e-04 | kPa | 243.15 | Vapor p... |
| Pvap | 5.79e-04 | kPa | 243.15 | Vapor p... |
| Pvap | 1.06e-03 | kPa | 248.15 | Vapor p... |
| Pvap | 1.07e-03 | kPa | 248.15 | Vapor p... |
| Pvap | 1.07e-03 | kPa | 248.15 | Vapor p... |
| Pvap | 1.92e-03 | kPa | 253.15 | Vapor p... |
| Pvap | 1.92e-03 | kPa | 253.15 | Vapor p... |
| Pvap | 1.93e-03 | kPa | 253.15 | Vapor p... |
| Pvap | 3.38e-03 | kPa | 258.15 | Vapor p... |
| Pvap | 3.39e-03 | kPa | 258.15 | Vapor p... |
| Pvap | 3.40e-03 | kPa | 258.15 | Vapor p... |
| Pvap | 5.80e-03 | kPa | 263.15 | Vapor p... |
| Pvap | 5.80e-03 | kPa | 263.15 | Vapor p... |
| Pvap | 5.81e-03 | kPa | 263.15 | Vapor p... |
| Pvap | 9.73e-03 | kPa | 268.15 | Vapor p... |
| Pvap | 9.73e-03 | kPa | 268.15 | Vapor p... |
| Pvap | 9.74e-03 | kPa | 268.15 | Vapor p... |
| Pvap | 0.02 | kPa | 273.65 | Vapor p... |
| Pvap | 0.02 | kPa | 273.65 | Vapor p... |
| Pvap | 0.02 | kPa | 273.65 | Vapor p... |
| Pvap | 0.03 | kPa | 278.15 | Vapor p... |
| Pvap | 0.03 | kPa | 278.15 | Vapor p... |
| Pvap | 0.03 | kPa | 278.15 | Vapor p... |
| Pvap | 0.04 | kPa | 283.15 | Vapor p... |
| Pvap | 0.04 | kPa | 283.15 | Vapor p... |
| Pvap | 0.04 | kPa | 283.15 | Vapor p... |
| Pvap | 0.06 | kPa | 288.15 | Vapor p... |
| Pvap | 0.06 | kPa | 288.15 | Vapor p... |
| Pvap | 0.06 | kPa | 288.15 | Vapor p... |
| Pvap | 0.09 | kPa | 293.15 | Vapor p... |
| Pvap | 0.09 | kPa | 293.15 | Vapor p... |
| Pvap | 0.09 | kPa | 293.15 | Vapor p... |
| Pvap | 0.14 | kPa | 298.15 | Vapor p... |
| Pvap | 0.14 | kPa | 298.15 | Vapor p... |
| Pvap | 0.14 | kPa | 298.15 | Vapor p... |
| Pvap | 0.21 | kPa | 303.15 | Vapor p... |
| Pvap | 0.21 | kPa | 303.15 | Vapor p... |
| Pvap | 0.21 | kPa | 303.15 | Vapor p... |
| Pvap | 0.30 | kPa | 308.15 | Vapor p... |
| Pvap | 0.30 | kPa | 308.15 | Vapor p... |
| Pvap | 0.30 | kPa | 308.15 | Vapor p... |
| ρl | [833.27; 856.22] | kg/m3 | [288.15; 318.15] |
|
|
T(K) Liquid Density (kg/m3) 835 840 845 850 855 290 300 310 | ||||
| ρl | 856.22 | kg/m3 | 288.15 | Thermal... |
| ρl | 852.44 | kg/m3 | 293.15 | Thermal... |
| ρl | 848.64 | kg/m3 | 298.15 | Thermal... |
| ρl | 840.99 | kg/m3 | 308.15 | Thermal... |
| ρl | 833.27 | kg/m3 | 318.15 | Thermal... |
Similar Compounds
Find more compounds similar to (Z)-3-Hexen-1-ol.
Mixtures
Sources
- Crippen Method
- Crippen Method
- Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
- Thermal and Volumetric Properties of Four Aqueous Aroma Compounds at Infinite Dilution
- Green Leaf Volatiles on Atmospheric Air/Water Interfaces: A Combined Experimental and Molecular Simulation Study
- Joback Method
- McGowan Method
- NIST Webbook
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.