- InChI
- InChI=1S/C14H26O4/c1-17-13(15)11-9-7-5-3-4-6-8-10-12-14(16)18-2/h3-12H2,1-2H3
- InChI Key
- IZMOTZDBVPMOFE-UHFFFAOYSA-N
- Formula
- C14H26O4
- SMILES
- COC(=O)CCCCCCCCCCC(=O)OC
- Molecular Weight1
- 258.35
- CAS
- 1731-79-9
- Other Names
-
- 1,12-Dimethyl dodecanedioate
- Dimethyl 1,10-decanedicarboxylate
- Dimethyl 1,12-dodecanedioate
- Dimethyl dodecanedioate
- dimethyl 1,12-dodecanoate
- dimethyl dodecanoate
- dodecanedioic acid dimethyl ester
- ω : Acentric Factor.
- 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).
- 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).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (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 | 0.8397 | Relay (1.0) Calculated Property | |
| ΔfG° | -400.84 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -931.10 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 37.59 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 94.43 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.51 | eV | Relay (1.0) Calculated Property |
| log10WS | -3.90 | Relay (1.0) Calculated Property | |
| logPoct/wat | 3.233 | Crippen Calculated Property | |
| McVol | 223.000 | ml/mol | McGowan Calculated Property |
| Pc | 1639.10 | kPa | Joback Calculated Property |
| Inp | [309.45; 1853.70] |
|
|
| Inp | 1851.00 | NIST | |
| Inp | 1853.70 | NIST | |
| Inp | 309.45 | NIST | |
| Inp | 309.45 | NIST | |
| Inp | 1851.00 | NIST | |
| Inp | 1853.70 | NIST | |
| Tboil | 561.55 | K | Relay (1.0) Calculated Property |
| Tc | 736.92 | K | Relay (1.0) Calculated Property |
| Tfus | 307.48 | K | Relay (1.0) Calculated Property |
| Vc | 0.866 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [622.19; 705.29] | J/mol×K | [672.30; 848.26] |
|
| 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] |
|
| 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 |
| ρl | [927.00; 959.40] | kg/m3 | [313.15; 352.15] |
|
| ρl | 959.40 | kg/m3 | 313.15 | Phase Equilibria for the Hydroesterification of 10-Undecenoic Acid Methyl Ester |
| ρl | 951.00 | kg/m3 | 323.15 | Phase Equilibria for the Hydroesterification of 10-Undecenoic Acid Methyl Ester |
| ρl | 943.10 | kg/m3 | 333.15 | Phase Equilibria for the Hydroesterification of 10-Undecenoic Acid Methyl Ester |
| ρl | 934.40 | kg/m3 | 343.15 | Phase Equilibria for the Hydroesterification of 10-Undecenoic Acid Methyl Ester |
| ρl | 927.00 | kg/m3 | 352.15 | Phase Equilibria for the Hydroesterification of 10-Undecenoic Acid Methyl Ester |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [441.20; 460.50] | K | [1.00; 1.90] |
|
| Tboilr | 441.20 | K | 1.00 | NIST |
| Tboilr | 460.50 ± 0.50 | K | 1.90 | NIST |
Similar Compounds
Find more compounds similar to Dodecanedioic acid, dimethyl ester.
Mixtures
- Dodecane + Dodecanedioic acid, dimethyl ester
- Dodecanedioic acid, dimethyl ester + 10-Undecenoic acid, methyl ester
- Carbon monoxide + Dodecanedioic acid, dimethyl ester
- Carbon monoxide + Methyl Alcohol + Dodecanedioic acid, dimethyl ester
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Phase Equilibria for the Hydroesterification of 10-Undecenoic Acid Methyl Ester
- Joback Method
- McGowan Method
- NIST Webbook
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