- InChI
- InChI=1S/C14H26O4/c1-3-17-13(15)11-9-7-5-6-8-10-12-14(16)18-4-2/h3-12H2,1-2H3
- InChI Key
- ONKUXPIBXRRIDU-UHFFFAOYSA-N
- Formula
- C14H26O4
- SMILES
- CCOC(=O)CCCCCCCCC(=O)OCC
- Molecular Weight1
- 258.35
- CAS
- 110-40-7
- Other Names
-
- Bisoflex DES
- Decanedioic acid, 1,10-diethyl ester
- Diethyl 1,10-decanedioate
- Diethyl decanedioate
- Diethyl sebacate
- Ethyl sebacate
- NSC 8911
- Sebacic acid, diethyl ester
- 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).
- ρl : Liquid Density (kg/m3).
- 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° | -400.84 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -821.89 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 37.59 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 65.07 | kJ/mol | Joback Calculated Property |
| log10WS | -3.51 | Aq. Sol... | |
| logPoct/wat | 3.233 | Crippen Calculated Property | |
| McVol | 223.000 | ml/mol | McGowan Calculated Property |
| Pc | 1639.10 | kPa | Joback Calculated Property |
| Inp | [1745.00; 1804.00] |
|
|
| Inp | 1804.00 | NIST | |
| Inp | 1746.00 | NIST | |
| Inp | 1759.00 | NIST | |
| Inp | 1764.00 | NIST | |
| Inp | 1759.00 | NIST | |
| Inp | 1752.00 | NIST | |
| Inp | 1746.00 | NIST | |
| Inp | 1745.00 | NIST | |
| Inp | 1804.00 | NIST | |
| I | 2272.00 | NIST | |
| Tboil | 585.20 | K | NIST |
| Tc | 740.00 | K | Vapor-l... |
| Tfus | 276.65 | K | Aq. Sol... |
| Vc | 0.868 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [622.19; 705.29] | J/mol×K | [672.30; 848.26] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 620 640 660 680 700 700 750 800 850 | ||||
| Cp,gas | 622.19 | J/mol×K | 672.30 | Joback Calculated Property |
| Cp,gas | 637.83 | J/mol×K | 701.63 | Joback Calculated Property |
| Cp,gas | 652.75 | J/mol×K | 730.95 | Joback Calculated Property |
| Cp,gas | 666.95 | J/mol×K | 760.28 | Joback Calculated Property |
| Cp,gas | 680.44 | J/mol×K | 789.61 | Joback Calculated Property |
| Cp,gas | 693.22 | J/mol×K | 818.93 | Joback Calculated Property |
| Cp,gas | 705.29 | J/mol×K | 848.26 | Joback Calculated Property |
| η | [0.0001198; 0.0014859] | Pa×s | [391.86; 672.30] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 2.00e-4 4.00e-4 6.00e-4 8.00e-4 1.00e-3 1.20e-3 1.40e-3 1.60e-3 400 500 600 | ||||
| η | 0.0014859 | Pa×s | 391.86 | Joback Calculated Property |
| η | 0.0007810 | Pa×s | 438.60 | Joback Calculated Property |
| η | 0.0004646 | Pa×s | 485.34 | Joback Calculated Property |
| η | 0.0003028 | Pa×s | 532.08 | Joback Calculated Property |
| η | 0.0002115 | Pa×s | 578.82 | Joback Calculated Property |
| η | 0.0001558 | Pa×s | 625.56 | Joback Calculated Property |
| η | 0.0001198 | Pa×s | 672.30 | Joback Calculated Property |
| ΔvapH | 74.10 | kJ/mol | 488.50 | NIST |
| ρl | 959.18 | kg/m3 | 298.20 | Modelin... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [445.42; 616.82] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.74579e+01 | |||
| Coefficient B | -7.11540e+03 | |||
| Coefficient C | -3.10220e+01 | |||
| Temperature range, min. | 445.42 | |||
| Temperature range, max. | 616.82 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 600 | ||||
| Pvap | 1.33 | kPa | 445.42 | Calculated Property |
| Pvap | 2.83 | kPa | 464.46 | Calculated Property |
| Pvap | 5.66 | kPa | 483.51 | Calculated Property |
| Pvap | 10.68 | kPa | 502.55 | Calculated Property |
| Pvap | 19.18 | kPa | 521.60 | Calculated Property |
| Pvap | 32.97 | kPa | 540.64 | Calculated Property |
| Pvap | 54.53 | kPa | 559.69 | Calculated Property |
| Pvap | 87.07 | kPa | 578.73 | Calculated Property |
| Pvap | 134.73 | kPa | 597.78 | Calculated Property |
| Pvap | 202.63 | kPa | 616.82 | Calculated Property |
Similar Compounds
Find more compounds similar to Decanedioic acid, diethyl ester.
Mixtures
- Decanedioic acid, diethyl ester + Formic acid + Water
- Decanedioic acid, diethyl ester + Oxalic acid + Water
Sources
- Crippen Method
- Modeling phase equilibria of ternary systems (water + formic acid + ester or alcohol) through UNIFAC-original, SERLAS, NRTL, NRTL-modified, and three-suffix Margules: Parameter estimation using genetic algorithm
- Vapor-liquid critical temperatures and pressures of dicarboxylic acid diethyl esters
- Comparison of Extractability of Oxalic Acid from Dilute Aqueous Solutions Using Dioctylamine and Trioctylphosphine Oxide
- Joback Method
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.