- InChI
- InChI=1S/C12H24O/c1-3-5-6-7-8-9-10-11-12-13-4-2/h4H,2-3,5-12H2,1H3
- InChI Key
- NSOAQRMLVFRWIT-UHFFFAOYSA-N
- Formula
- C12H24O
- SMILES
- C=COCCCCCCCCCC
- Molecular Weight1
- 184.32
- CAS
- 765-05-9
- Other Names
-
- 1-(Vinyloxy)decane
- Decyl vinyl ether
- Ether, decyl vinyl
- ω : Acentric Factor.
- 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).
- 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).
- 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 | 0.6516 | Relay (1.0) Calculated Property | |
| ΔfG° | 33.00 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -318.24 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 26.74 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 62.45 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.03 | eV | Relay (1.0) Calculated Property |
| log10WS | -5.10 | Relay (1.0) Calculated Property | |
| logPoct/wat | 4.287 | Crippen Calculated Property | |
| McVol | 181.510 | ml/mol | McGowan Calculated Property |
| Pc | 1818.50 | kPa | Joback Calculated Property |
| Tboil | 497.80 ± 2.00 | K | NIST |
| Tc | 666.72 | K | Relay (1.0) Calculated Property |
| Tfus | 232.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Vc | 0.704 | m3/kmol | Relay (1.0) Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [265.64; 628.41] | 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 | 1.44890e+01 | |||
| Coefficient B | 1.06062e+00 | |||
| Coefficient C | -5.40900e-04 | |||
| Coefficient D | 9.42000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 265.64 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 326.19 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 380.97 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 430.31 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 474.48 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 513.80 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 548.55 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 579.04 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 605.56 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 628.41 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0054473; 0.0002232] | Pa×s | [232.15; 460.01] |
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 | -1.16623e+01 | |||
| Coefficient B | 1.49729e+03 | |||
| 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. | 232.15 | |||
| Temperature range, max. | 460.01 | |||
| η | 0.0054473 | Pa×s | 232.15 | Calculated Property |
| η | 0.0028890 | Pa×s | 257.47 | Calculated Property |
| η | 0.0017164 | Pa×s | 282.78 | Calculated Property |
| η | 0.0011109 | Pa×s | 308.10 | Calculated Property |
| η | 0.0007681 | Pa×s | 333.42 | Calculated Property |
| η | 0.0005595 | Pa×s | 358.74 | Calculated Property |
| η | 0.0004249 | Pa×s | 384.05 | Calculated Property |
| η | 0.0003339 | Pa×s | 409.37 | Calculated Property |
| η | 0.0002698 | Pa×s | 434.69 | Calculated Property |
| η | 0.0002232 | Pa×s | 460.01 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [371.32; 533.78] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.44089e+01 | |||
| Coefficient B | -4.15428e+03 | |||
| Coefficient C | -7.71340e+01 | |||
| Temperature range, min. | 371.32 | |||
| Temperature range, max. | 533.78 | |||
| Pvap | 1.33 | kPa | 371.32 | Calculated Property |
| Pvap | 3.02 | kPa | 389.37 | Calculated Property |
| Pvap | 6.24 | kPa | 407.42 | Calculated Property |
| Pvap | 11.98 | kPa | 425.47 | Calculated Property |
| Pvap | 21.55 | kPa | 443.52 | Calculated Property |
| Pvap | 36.70 | kPa | 461.58 | Calculated Property |
| Pvap | 59.59 | kPa | 479.63 | Calculated Property |
| Pvap | 92.81 | kPa | 497.68 | Calculated Property |
| Pvap | 139.36 | kPa | 515.73 | Calculated Property |
| Pvap | 202.65 | kPa | 533.78 | Calculated Property |
Similar Compounds
Find more compounds similar to Decane, 1-(ethenyloxy)-.
Sources
- 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).
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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