- 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).
- 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 | |
| ΔfH°gas | -931.10 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 40.75 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 95.34 | 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 | 1535.46 | kPa | Joback Calculated Property |
| Inp | [309.45; 1853.70] |
|
|
| Inp | 309.45 | NIST | |
| Inp | 1851.00 | NIST | |
| Inp | 1853.70 | NIST | |
| Inp | 309.45 | NIST | |
| Inp | 1851.00 | NIST | |
| Inp | 1853.70 | NIST | |
| Tboil | 561.55 | K | Relay (1.0) Calculated Property |
| Tc | 739.62 | K | Relay (1.0) Calculated Property |
| Tfus | 304.30 | 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 |
|---|---|---|---|---|
| Cp,gas | [608.50; 693.46] | J/mol×K | [636.36; 807.35] |
|
| Cp,gas | 608.50 | J/mol×K | 636.36 | Joback Calculated Property |
| Cp,gas | 624.53 | J/mol×K | 664.86 | Joback Calculated Property |
| Cp,gas | 639.81 | J/mol×K | 693.36 | Joback Calculated Property |
| Cp,gas | 654.34 | J/mol×K | 721.85 | Joback Calculated Property |
| Cp,gas | 668.12 | J/mol×K | 750.35 | Joback Calculated Property |
| Cp,gas | 681.16 | J/mol×K | 778.85 | Joback Calculated Property |
| Cp,gas | 693.46 | J/mol×K | 807.35 | Joback Calculated Property |
| η | [0.0000987; 0.0031554] | Pa×s | [332.20; 636.36] |
|
| η | 0.0031554 | Pa×s | 332.20 | Joback Calculated Property |
| η | 0.0012085 | Pa×s | 382.89 | Joback Calculated Property |
| η | 0.0005793 | Pa×s | 433.59 | Joback Calculated Property |
| η | 0.0003239 | Pa×s | 484.28 | Joback Calculated Property |
| η | 0.0002022 | Pa×s | 534.97 | Joback Calculated Property |
| η | 0.0001369 | Pa×s | 585.67 | Joback Calculated Property |
| η | 0.0000987 | Pa×s | 636.36 | 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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