- InChI
- InChI=1S/C16H22Cl2O3/c1-3-5-6-12(4-2)10-21-16(19)11-20-15-8-7-13(17)9-14(15)18/h7-9,12H,3-6,10-11H2,1-2H3
- InChI Key
- QZSFJRIWRPJUOH-UHFFFAOYSA-N
- Formula
- C16H22Cl2O3
- SMILES
-
CCCCC(CC)COC(=O)COc1ccc(Cl)cc1
Cl - Molecular Weight1
- 333.25
- CAS
- 1928-43-4
- Other Names
-
- 2,4-D 2-ethylhexyl ester
- 2,4-Dichlorophenoxyacetic acid 2-ethylhexyl ester
- 2-Ethylhexyl (2,4-dichlorophenoxy)acetate
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfusH° : Enthalpy of fusion 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).
- Tboil : Normal Boiling Point Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfusH° | 40.89 | kJ/mol | Joback Calculated Property |
| log10WS | -5.78 | Relay (1.0) Calculated Property | |
| logPoct/wat | 5.132 | Crippen Calculated Property | |
| McVol | 250.330 | ml/mol | McGowan Calculated Property |
| Pc | 1561.05 | kPa | Joback Calculated Property |
| Tboil | 615.93 | K | Relay (1.0) Calculated Property |
| Tfus | 282.65 | K | Relay (1.0) Calculated Property |
Cheméo can also estimate Critical Temperature, Critical Volume, Enthalpy of formation at standard conditions, Enthalpy of vaporization at standard conditions, Standard Gibbs free energy of formation, Acentric Factor, Ionization energy for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 83.00 | kJ/mol | 517.50 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [350.98; 763.87] | 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 | 5.80460e+01 | |||
| Coefficient B | 1.22744e+00 | |||
| Coefficient C | -5.82120e-04 | |||
| Coefficient D | 6.05000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 350.98 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 422.11 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 486.47 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 544.27 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 595.70 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 640.93 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 680.18 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 713.62 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 741.45 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 763.87 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0008574; 0.0000946] | Pa×s | [430.94; 673.20] |
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 | -1.31881e+01 | |||
| Coefficient B | 2.64017e+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. | 430.94 | |||
| Temperature range, max. | 673.20 | |||
| η | 0.0008574 | Pa×s | 430.94 | Calculated Property |
| η | 0.0005981 | Pa×s | 457.86 | Calculated Property |
| η | 0.0004342 | Pa×s | 484.78 | Calculated Property |
| η | 0.0003261 | Pa×s | 511.69 | Calculated Property |
| η | 0.0002519 | Pa×s | 538.61 | Calculated Property |
| η | 0.0001995 | Pa×s | 565.53 | Calculated Property |
| η | 0.0001614 | Pa×s | 592.45 | Calculated Property |
| η | 0.0001330 | Pa×s | 619.36 | Calculated Property |
| η | 0.0001113 | Pa×s | 646.28 | Calculated Property |
| η | 0.0000946 | Pa×s | 673.20 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [368.13; 906.02] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 7.55905e+00 | |||
| Coefficient B | -1.74981e+03 | |||
| Coefficient C | -1.27490e+02 | |||
| Temperature range, min. | 368.13 | |||
| Temperature range, max. | 906.02 | |||
| Pvap | 1.33 | kPa | 368.13 | Calculated Property |
| Pvap | 5.66 | kPa | 427.90 | Calculated Property |
| Pvap | 14.89 | kPa | 487.66 | Calculated Property |
| Pvap | 29.73 | kPa | 547.43 | Calculated Property |
| Pvap | 49.97 | kPa | 607.19 | Calculated Property |
| Pvap | 74.85 | kPa | 666.96 | Calculated Property |
| Pvap | 103.44 | kPa | 726.72 | Calculated Property |
| Pvap | 134.80 | kPa | 786.49 | Calculated Property |
| Pvap | 168.10 | kPa | 846.25 | Calculated Property |
| Pvap | 202.65 | kPa | 906.02 | Calculated Property |
Similar Compounds
Find more compounds similar to Acetic acid, (2,4-dichlorophenoxy)-, 2-ethylhexyl ester.
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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