- InChI
- InChI=1S/C15H28O2/c1-3-5-6-7-8-9-10-11-12-13-14-17-15(16)4-2/h4H,2-3,5-14H2,1H3
- InChI Key
- PBOSTUDLECTMNL-UHFFFAOYSA-N
- Formula
- C15H28O2
- SMILES
- C=CC(=O)OCCCCCCCCCCCC
- Molecular Weight1
- 240.38
- CAS
- 2156-97-0
- Other Names
-
- 2-Propenoic acid, dodecyl ester
- 2-Propenoic acid, n-dodecyl ester
- Acrylic acid, dodecyl ester
- Ageflex FA-12
- Lauryl acrylate
- NSC 24177
- SR 335
- n-Dodecyl acrylate
- n-Lauryl acrylate
- n-Lauryl acrylate (monomer)
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- 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).
- 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).
- 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 |
|---|---|---|---|
| ω | 0.8026 | Relay (1.0) Calculated Property | |
| ΔfH°gas | -559.00 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 37.70 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 80.76 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.89 | eV | Relay (1.0) Calculated Property |
| log10WS | -5.34 | Relay (1.0) Calculated Property | |
| logPoct/wat | 4.636 | Crippen Calculated Property | |
| McVol | 225.350 | ml/mol | McGowan Calculated Property |
| Pc | 1466.85 | kPa | Joback Calculated Property |
| Inp | [1675.00; 1675.00] |
|
|
| Inp | 1675.00 | NIST | |
| Inp | 1675.00 | NIST | |
| I | [1996.00; 1996.00] |
|
|
| I | 1996.00 | NIST | |
| I | 1996.00 | NIST | |
| Tboil | 552.40 | K | Relay (1.0) Calculated Property |
| Tc | 736.91 | K | Relay (1.0) Calculated Property |
| Tfus | 272.98 | K | Relay (1.0) Calculated Property |
| Vc | 0.867 | m3/kmol | Relay (1.0) Calculated Property |
Cheméo can also estimate Standard Gibbs free energy of formation for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 64.60 | kJ/mol | 502.50 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [330.22; 772.79] | 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 | 1.16710e+01 | |||
| Coefficient B | 1.35402e+00 | |||
| Coefficient C | -7.20500e-04 | |||
| Coefficient D | 1.27600e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 330.22 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 406.17 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 474.48 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 535.56 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 589.82 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 637.65 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 679.46 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 715.65 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 746.62 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 772.79 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0039425; 0.0001933] | Pa×s | [299.38; 535.45] |
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 | -1.23747e+01 | |||
| Coefficient B | 2.04740e+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. | 299.38 | |||
| Temperature range, max. | 535.45 | |||
| η | 0.0039425 | Pa×s | 299.38 | Calculated Property |
| η | 0.0022726 | Pa×s | 325.61 | Calculated Property |
| η | 0.0014221 | Pa×s | 351.84 | Calculated Property |
| η | 0.0009497 | Pa×s | 378.07 | Calculated Property |
| η | 0.0006684 | Pa×s | 404.30 | Calculated Property |
| η | 0.0004909 | Pa×s | 430.53 | Calculated Property |
| η | 0.0003736 | Pa×s | 456.76 | Calculated Property |
| η | 0.0002929 | Pa×s | 482.99 | Calculated Property |
| η | 0.0002354 | Pa×s | 509.22 | Calculated Property |
| η | 0.0001933 | Pa×s | 535.45 | Calculated Property |
Similar Compounds
Find more compounds similar to Dodecyl acrylate.
Mixtures
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Cloud-Point and Vapor-Liquid Behavior of Binary and Ternary Systems for the Poly(dodecyl acrylate) + Cosolvent and Dodecyl Acrylate in Supercritical Solvents
- Joback Method
- McGowan Method
- NIST Webbook
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