![Heptane, 3-[(ethenyloxy)methyl]-](/cid/76-852-2/Heptane-3-ethenyloxy-methyl.png "Heptane, 3-[(ethenyloxy)methyl]-")
- InChI
- InChI=1S/C10H20O/c1-4-7-8-10(5-2)9-11-6-3/h6,10H,3-5,7-9H2,1-2H3
- InChI Key
- DSSAWHFZNWVJEC-UHFFFAOYSA-N
- Formula
- C10H20O
- SMILES
- C=COCC(CC)CCCC
- Molecular Weight1
- 156.27
- CAS
- 103-44-6
- Other Names
-
- (2-Ethyl-1-hexyl) vinyl ether
- 1-Ethenoxy-2-ethylhexane
- 2-Ethylhexyl vinyl ether
- Ether, 2-ethylhexyl vinyl
- Rapi-cure EHVE
- Vinyl 2-ethylhexyl ether
- 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.
- 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° | 13.72 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -261.80 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 18.04 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 39.21 | kJ/mol | Joback Calculated Property |
| log10WS | -3.20 | Crippen Calculated Property | |
| logPoct/wat | 3.363 | Crippen Calculated Property | |
| McVol | 153.330 | ml/mol | McGowan Calculated Property |
| Pc | 2173.43 | kPa | Joback Calculated Property |
| Inp | [1011.00; 1038.00] |
|
|
| Inp | 1036.00 | NIST | |
| Inp | 1011.00 | NIST | |
| Inp | 1026.00 | NIST | |
| Inp | 1038.00 | NIST | |
| I | [1165.00; 1179.00] |
|
|
| I | 1179.00 | NIST | |
| I | 1165.00 | NIST | |
| I | 1168.00 | NIST | |
| Tboil | 446.86 | K | Joback Calculated Property |
| Tc | 616.05 | K | Joback Calculated Property |
| Tfus | 207.93 | K | Joback Calculated Property |
| Vc | 0.589 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [325.63; 405.76] | J/mol×K | [446.86; 616.05] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 320 340 360 380 400 450 500 550 600 | ||||
| Cp,gas | 325.63 | J/mol×K | 446.86 | Joback Calculated Property |
| Cp,gas | 340.29 | J/mol×K | 475.06 | Joback Calculated Property |
| Cp,gas | 354.41 | J/mol×K | 503.26 | Joback Calculated Property |
| Cp,gas | 368.01 | J/mol×K | 531.46 | Joback Calculated Property |
| Cp,gas | 381.10 | J/mol×K | 559.65 | Joback Calculated Property |
| Cp,gas | 393.67 | J/mol×K | 587.85 | Joback Calculated Property |
| Cp,gas | 405.76 | J/mol×K | 616.05 | Joback Calculated Property |
| η | [0.0001936; 0.0061809] | Pa×s | [207.93; 446.86] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 6.00e-3 300 400 | ||||
| η | 0.0061809 | Pa×s | 207.93 | Joback Calculated Property |
| η | 0.0021823 | Pa×s | 247.75 | Joback Calculated Property |
| η | 0.0010280 | Pa×s | 287.57 | Joback Calculated Property |
| η | 0.0005816 | Pa×s | 327.39 | Joback Calculated Property |
| η | 0.0003723 | Pa×s | 367.22 | Joback Calculated Property |
| η | 0.0002600 | Pa×s | 407.04 | Joback Calculated Property |
| η | 0.0001936 | Pa×s | 446.86 | Joback Calculated Property |
| ΔvapH | 44.70 | kJ/mol | 390.50 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [364.62; 486.19] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.72878e+01 | |||
| Coefficient B | -4.92691e+03 | |||
| Coefficient C | -7.48050e+01 | |||
| Temperature range, min. | 364.62 | |||
| Temperature range, max. | 486.19 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 | ||||
| Pvap | 1.33 | kPa | 364.62 | Calculated Property |
| Pvap | 2.84 | kPa | 378.13 | Calculated Property |
| Pvap | 5.68 | kPa | 391.64 | Calculated Property |
| Pvap | 10.73 | kPa | 405.14 | Calculated Property |
| Pvap | 19.28 | kPa | 418.65 | Calculated Property |
| Pvap | 33.14 | kPa | 432.16 | Calculated Property |
| Pvap | 54.75 | kPa | 445.67 | Calculated Property |
| Pvap | 87.33 | kPa | 459.17 | Calculated Property |
| Pvap | 134.94 | kPa | 472.68 | Calculated Property |
| Pvap | 202.64 | kPa | 486.19 | Calculated Property |
Similar Compounds
Find more compounds similar to Heptane, 3-[(ethenyloxy)methyl]-.
Sources
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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