- InChI
- InChI=1S/C5H10O/c1-3-5-6-4-2/h4H,2-3,5H2,1H3
- InChI Key
- OVGRCEFMXPHEBL-UHFFFAOYSA-N
- Formula
- C5H10O
- SMILES
- C=COCCC
- Molecular Weight1
- 86.13
- 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).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- 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° | -25.94 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -153.32 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 8.61 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 28.46 | kJ/mol | Joback Calculated Property |
| log10WS | -1.35 | Crippen Calculated Property | |
| logPoct/wat | 1.556 | Crippen Calculated Property | |
| McVol | 82.880 | ml/mol | McGowan Calculated Property |
| Pc | 3572.80 | kPa | Joback Calculated Property |
| Tboil | 332.90 | K | Joback Calculated Property |
| Tc | 500.59 | K | Joback Calculated Property |
| Tfus | 166.58 | K | Joback Calculated Property |
| Vc | 0.315 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [135.21; 180.14] | J/mol×K | [332.90; 500.59] | 
|
| Cp,gas | 135.21 | J/mol×K | 332.90 | Joback Calculated Property |
| Cp,gas | 143.28 | J/mol×K | 360.85 | Joback Calculated Property |
| Cp,gas | 151.11 | J/mol×K | 388.80 | Joback Calculated Property |
| Cp,gas | 158.71 | J/mol×K | 416.74 | Joback Calculated Property |
| Cp,gas | 166.08 | J/mol×K | 444.69 | Joback Calculated Property |
| Cp,gas | 173.22 | J/mol×K | 472.64 | Joback Calculated Property |
| Cp,gas | 180.14 | J/mol×K | 500.59 | Joback Calculated Property |
| η | [0.0002010; 0.0024826] | Pa×s | [166.58; 332.90] |
|
| η | 0.0024826 | Pa×s | 166.58 | Joback Calculated Property |
| η | 0.0012110 | Pa×s | 194.30 | Joback Calculated Property |
| η | 0.0007067 | Pa×s | 222.02 | Joback Calculated Property |
| η | 0.0004648 | Pa×s | 249.74 | Joback Calculated Property |
| η | 0.0003324 | Pa×s | 277.46 | Joback Calculated Property |
| η | 0.0002526 | Pa×s | 305.18 | Joback Calculated Property |
| η | 0.0002010 | Pa×s | 332.90 | Joback Calculated Property |
| Pvap | [20.00; 101.70] | kPa | [296.02; 337.90] |
|
| Pvap | 20.00 | kPa | 296.02 | Isother... |
| Pvap | 25.00 | kPa | 301.62 | Isother... |
| Pvap | 30.00 | kPa | 305.44 | Isother... |
| Pvap | 35.00 | kPa | 309.37 | Isother... |
| Pvap | 40.00 | kPa | 312.65 | Isother... |
| Pvap | 45.00 | kPa | 315.13 | Isother... |
| Pvap | 50.00 | kPa | 317.88 | Isother... |
| Pvap | 55.00 | kPa | 320.29 | Isother... |
| Pvap | 60.00 | kPa | 322.72 | Isother... |
| Pvap | 65.00 | kPa | 324.90 | Isother... |
| Pvap | 70.00 | kPa | 326.95 | Isother... |
| Pvap | 75.00 | kPa | 328.89 | Isother... |
| Pvap | 80.00 | kPa | 330.76 | Isother... |
| Pvap | 85.00 | kPa | 332.86 | Isother... |
| Pvap | 90.00 | kPa | 334.22 | Isother... |
| Pvap | 95.00 | kPa | 336.28 | Isother... |
| Pvap | 100.00 | kPa | 337.38 | Isother... |
| Pvap | 101.70 | kPa | 337.90 | Isother... |
| n0 | 1.39094 ± 0.00005 | 298.15 | Binary ... | |
| ρl | [762.69; 768.97] | kg/m3 | [293.15; 298.15] |
|
| ρl | 768.97 ± 0.01 | kg/m3 | 293.15 | Isother... |
| ρl | 762.98 ± 0.01 | kg/m3 | 298.15 | Binary ... |
| ρl | 762.96 | kg/m3 | 298.15 | Liquid ... |
| ρl | 762.69 ± 0.01 | kg/m3 | 298.15 | Binary ... |
Similar Compounds
Find more compounds similar to propoxyethylene.
Sources
- Crippen Method
- Crippen Method
- Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
- Binary LLE for Propyl Vinyl Ether (PVE) + Water, Ternary LLE for PVE + Methanol or Ethanol + Water at 298.15 K, and VE and centsR at 293.15 K for the Mixture of PVE + Ethanol + 2,2,4-Trimethylpentane
- Liquid Liquid Equilibrium for Ternary Systems of Propyl Vinyl Ether + C3 or C4 Alcohols + Water at 298.15 K and Excess Molar Enthalpies for Ternary and Constituent Binary Systems of Propyl Vinyl Ether + Ethanol + Isooctane at 303.15 K
- Binary and Ternary Vapor-Liquid Equilibrium at 323.15 K and Excess Molar Volumes at 298.15 K for the Mixtures of Propyl Vinyl Ether + 1-Propanol + Toluene
- Joback Method
- McGowan Method
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.