Property | Value | Unit | Source |
---|---|---|---|

Δ_{f}G° |
-48.53 | kJ/mol | Joback Calculated Property |

Δ_{f}H°_{gas} |
-366.48 | kJ/mol | Joback Calculated Property |

Δ_{fus}H° |
27.91 | kJ/mol | Joback Calculated Property |

Δ_{vap}H° |
60.03 | kJ/mol | Joback Calculated Property |

log_{10}WS |
-4.40 | Crippen Calculated Property | |

logP_{oct/wat} |
4.060 | Crippen Calculated Property | |

McVol | 205.890 | ml/mol | McGowan Calculated Property |

P_{c} |
1935.54 | kPa | Joback Calculated Property |

I_{np} |
[1674.00; 1735.00] | ||

I_{np} |
1735.00 | NIST | |

I_{np} |
1674.00 | NIST | |

I_{np} |
1735.00 | NIST | |

I_{np} |
1674.00 | NIST | |

I | [2598.00; 2598.00] | ||

I | 2598.00 | NIST | |

I | 2598.00 | NIST | |

T_{boil} |
645.13 | K | Joback Calculated Property |

T_{c} |
846.21 | K | Joback Calculated Property |

T_{fus} |
342.39 | K | Joback Calculated Property |

V_{c} |
0.785 | m^{3}/kmol |
Joback Calculated Property |

Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|

C_{p,gas} |
[546.83; 635.49] | J/mol×K | [645.13; 846.21] | |

C_{p,gas} |
546.83 | J/mol×K | 645.13 | Joback Calculated Property |

C_{p,gas} |
563.95 | J/mol×K | 678.64 | Joback Calculated Property |

C_{p,gas} |
580.10 | J/mol×K | 712.16 | Joback Calculated Property |

C_{p,gas} |
595.30 | J/mol×K | 745.67 | Joback Calculated Property |

C_{p,gas} |
609.57 | J/mol×K | 779.18 | Joback Calculated Property |

C_{p,gas} |
622.96 | J/mol×K | 812.70 | Joback Calculated Property |

C_{p,gas} |
635.49 | J/mol×K | 846.21 | Joback Calculated Property |

η | [0.0001267; 0.0024547] | Pa×s | [342.39; 645.13] | |

η | 0.0024547 | Pa×s | 342.39 | Joback Calculated Property |

η | 0.0010907 | Pa×s | 392.85 | Joback Calculated Property |

η | 0.0005830 | Pa×s | 443.30 | Joback Calculated Property |

η | 0.0003541 | Pa×s | 493.76 | Joback Calculated Property |

η | 0.0002360 | Pa×s | 544.22 | Joback Calculated Property |

η | 0.0001684 | Pa×s | 594.67 | Joback Calculated Property |

η | 0.0001267 | Pa×s | 645.13 | Joback Calculated Property |

ρ_{l} |
[910.61; 981.12] | kg/m^{3} |
[273.15; 363.15] | |

ρ_{l} |
981.12 | kg/m^{3} |
273.15 | Tempera... |

ρ_{l} |
977.18 | kg/m^{3} |
278.15 | Tempera... |

ρ_{l} |
973.25 | kg/m^{3} |
283.15 | Tempera... |

ρ_{l} |
969.32 | kg/m^{3} |
288.15 | Tempera... |

ρ_{l} |
965.40 | kg/m^{3} |
293.15 | Tempera... |

ρ_{l} |
961.49 | kg/m^{3} |
298.15 | Tempera... |

ρ_{l} |
957.57 | kg/m^{3} |
303.15 | Tempera... |

ρ_{l} |
949.73 | kg/m^{3} |
313.15 | Tempera... |

ρ_{l} |
941.92 | kg/m^{3} |
323.15 | Tempera... |

ρ_{l} |
934.11 | kg/m^{3} |
333.15 | Tempera... |

ρ_{l} |
926.28 | kg/m^{3} |
343.15 | Tempera... |

ρ_{l} |
918.45 | kg/m^{3} |
353.15 | Tempera... |

ρ_{l} |
910.61 | kg/m^{3} |
363.15 | Tempera... |

D^{*}_{i} |
[2.18e-05; 6.38e-04] | m^{2}/s |
[258.42; 352.41] | |

D^{*}_{i} |
2.26e-05 | m^{2}/s |
258.42 | Viscous... |

D^{*}_{i} |
2.18e-05 | m^{2}/s |
258.44 | Viscous... |

D^{*}_{i} |
2.21e-05 | m^{2}/s |
258.46 | Viscous... |

D^{*}_{i} |
3.30e-05 | m^{2}/s |
264.21 | Viscous... |

D^{*}_{i} |
3.31e-05 | m^{2}/s |
264.21 | Viscous... |

D^{*}_{i} |
5.57e-05 | m^{2}/s |
273.42 | Viscous... |

D^{*}_{i} |
5.61e-05 | m^{2}/s |
273.50 | Viscous... |

D^{*}_{i} |
5.67e-05 | m^{2}/s |
273.67 | Viscous... |

D^{*}_{i} |
7.32e-05 | m^{2}/s |
278.40 | Viscous... |

D^{*}_{i} |
7.24e-05 | m^{2}/s |
278.43 | Viscous... |

D^{*}_{i} |
7.27e-05 | m^{2}/s |
278.45 | Viscous... |

D^{*}_{i} |
7.33e-05 | m^{2}/s |
278.50 | Viscous... |

D^{*}_{i} |
1.10e-04 | m^{2}/s |
288.41 | Viscous... |

D^{*}_{i} |
1.11e-04 | m^{2}/s |
288.46 | Viscous... |

D^{*}_{i} |
1.34e-04 | m^{2}/s |
293.37 | Viscous... |

D^{*}_{i} |
1.35e-04 | m^{2}/s |
293.38 | Viscous... |

D^{*}_{i} |
1.63e-04 | m^{2}/s |
298.06 | Viscous... |

D^{*}_{i} |
1.64e-04 | m^{2}/s |
298.09 | Viscous... |

D^{*}_{i} |
1.65e-04 | m^{2}/s |
298.14 | Viscous... |

D^{*}_{i} |
1.60e-04 | m^{2}/s |
298.27 | Viscous... |

D^{*}_{i} |
1.60e-04 | m^{2}/s |
298.29 | Viscous... |

D^{*}_{i} |
2.25e-04 | m^{2}/s |
307.92 | Viscous... |

D^{*}_{i} |
2.26e-04 | m^{2}/s |
308.07 | Viscous... |

D^{*}_{i} |
2.22e-04 | m^{2}/s |
308.26 | Viscous... |

D^{*}_{i} |
2.21e-04 | m^{2}/s |
308.30 | Viscous... |

D^{*}_{i} |
2.54e-04 | m^{2}/s |
313.05 | Viscous... |

D^{*}_{i} |
2.54e-04 | m^{2}/s |
313.06 | Viscous... |

D^{*}_{i} |
2.91e-04 | m^{2}/s |
317.99 | Viscous... |

D^{*}_{i} |
2.92e-04 | m^{2}/s |
318.06 | Viscous... |

D^{*}_{i} |
3.74e-04 | m^{2}/s |
327.81 | Viscous... |

D^{*}_{i} |
3.74e-04 | m^{2}/s |
327.87 | Viscous... |

D^{*}_{i} |
4.18e-04 | m^{2}/s |
332.77 | Viscous... |

D^{*}_{i} |
4.18e-04 | m^{2}/s |
332.80 | Viscous... |

D^{*}_{i} |
4.22e-04 | m^{2}/s |
333.30 | Viscous... |

D^{*}_{i} |
4.72e-04 | m^{2}/s |
337.81 | Viscous... |

D^{*}_{i} |
4.71e-04 | m^{2}/s |
337.81 | Viscous... |

D^{*}_{i} |
5.84e-04 | m^{2}/s |
347.49 | Viscous... |

D^{*}_{i} |
5.82e-04 | m^{2}/s |
347.52 | Viscous... |

D^{*}_{i} |
6.38e-04 | m^{2}/s |
352.18 | Viscous... |

D^{*}_{i} |
6.36e-04 | m^{2}/s |
352.33 | Viscous... |

D^{*}_{i} |
6.36e-04 | m^{2}/s |
352.41 | Viscous... |

Find more compounds similar to *Benzoic acid, 2-ethylhexyl ester*.

- Crippen Method
- Crippen Method
- Viscous Calibration Liquids for Self-diffusion Measurements
- Temperature and Pressure Dependence of the Viscosities of 2-Ethylhexyl Benzoate, Bis(2-ethylhexyl) Phthalate, 2,6,10,15,19,23-Hexamethyltetracosane (Squalane), and Diisodecyl Phthalate
- Joback Method
- McGowan Method
- NIST Webbook

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