- InChI
- InChI=1S/C6H10O4/c1-3-9-5(7)6(8)10-4-2/h3-4H2,1-2H3
- InChI Key
- WYACBZDAHNBPPB-UHFFFAOYSA-N
- Formula
- C6H10O4
- SMILES
- CCOC(=O)C(=O)OCC
- Molecular Weight1
- 146.14
- CAS
- 95-92-1
- Other Names
-
- C2H5OCOCOOC2H5
- DIETHYL ESTER OXALIC ACID
- DIETHYL ETHANEDIOATE
- DIETHYL OXALATE
- Diethyl ester of oxalic acid
- Diethylester kyseliny stavelove
- Ethanedioic acid, 1,2-diethyl ester
- Ethyl oxalate
- NSC 8851
- Oxalic acid, diethyl ester
- Oxalic ether
- UN 2525
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase 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).
- ΔfH°liquid : Liquid phase 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).
- 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).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : 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 |
|---|---|---|---|
| ΔcH°liquid | [-2984.70; -2981.30] | kJ/mol |
|
| ΔcH°liquid | -2981.30 | kJ/mol | NIST |
| ΔcH°liquid | -2984.70 ± 8.40 | kJ/mol | NIST |
| ΔfG° | -468.20 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -656.77 | kJ/mol | Joback Calculated Property |
| ΔfH°liquid | [-809.73; -807.72] | kJ/mol |
|
| ΔfH°liquid | -809.73 | kJ/mol | NIST |
| ΔfH°liquid | -807.72 | kJ/mol | NIST |
| ΔfusH° | 16.87 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 47.26 | kJ/mol | Joback Calculated Property |
| IE | [9.80; 10.19] | eV |
|
| IE | 9.80 | eV | NIST |
| IE | 10.19 | eV | NIST |
| log10WS | -0.06 | Crippen Calculated Property | |
| logPoct/wat | 0.113 | Crippen Calculated Property | |
| McVol | 110.280 | ml/mol | McGowan Calculated Property |
| Pc | [2140.00; 3060.00] | kPa |
|
| Pc | 3060.00 | kPa | Critica... |
| Pc | 2140.00 ± 4.00 | kPa | NIST |
| ρc | 323.26 ± 2.92 | kg/m3 | NIST |
| Inp | [938.00; 948.00] |
|
|
| Inp | 940.00 | NIST | |
| Inp | 940.00 | NIST | |
| Inp | 948.00 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 940.00 | NIST | |
| Inp | 948.00 | NIST | |
| Inp | 940.00 | NIST | |
| I | [1496.00; 1530.00] |
|
|
| I | 1496.00 | NIST | |
| I | 1530.00 | NIST | |
| Tboil | [458.15; 458.90] | K |
|
| Tboil | 458.90 | K | NIST |
| Tboil | 458.80 ± 0.30 | K | NIST |
| Tboil | 458.80 ± 0.25 | K | NIST |
| Tboil | 458.15 ± 0.30 | K | NIST |
| Tboil | 458.85 ± 1.50 | K | NIST |
| Tc | 618.00 ± 2.00 | K | NIST |
| Tfus | [232.35; 232.55] | K |
|
| Tfus | 232.35 ± 0.50 | K | NIST |
| Tfus | 232.55 ± 0.40 | K | NIST |
| Vc | 0.419 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [236.42; 287.43] | J/mol×K | [489.26; 677.07] |
|
| Cp,gas | 236.42 | J/mol×K | 489.26 | Joback Calculated Property |
| Cp,gas | 245.69 | J/mol×K | 520.56 | Joback Calculated Property |
| Cp,gas | 254.67 | J/mol×K | 551.86 | Joback Calculated Property |
| Cp,gas | 263.35 | J/mol×K | 583.16 | Joback Calculated Property |
| Cp,gas | 271.71 | J/mol×K | 614.46 | Joback Calculated Property |
| Cp,gas | 279.74 | J/mol×K | 645.76 | Joback Calculated Property |
| Cp,gas | 287.43 | J/mol×K | 677.07 | Joback Calculated Property |
| Cp,liquid | 260.70 | J/mol×K | 298.00 | NIST |
| η | [0.0013670; 0.0016230] | Pa×s | [303.15; 313.15] |
|
| η | 0.0016230 | Pa×s | 303.15 | Densiti... |
| η | 0.0014800 | Pa×s | 308.15 | Densiti... |
| η | 0.0013670 | Pa×s | 313.15 | Densiti... |
| ΔvapH | [53.90; 62.30] | kJ/mol | [389.50; 400.00] |
|
| ΔvapH | 62.30 | kJ/mol | 389.50 | NIST |
| ΔvapH | 53.90 | kJ/mol | 400.00 | NIST |
| Pvap | [0.02; 0.63] | kPa | [283.60; 333.50] |
|
| Pvap | 0.02 | kPa | 283.60 | Vapor P... |
| Pvap | 0.03 | kPa | 288.50 | Vapor P... |
| Pvap | 0.04 | kPa | 293.40 | Vapor P... |
| Pvap | 0.06 | kPa | 298.30 | Vapor P... |
| Pvap | 0.08 | kPa | 303.30 | Vapor P... |
| Pvap | 0.13 | kPa | 308.40 | Vapor P... |
| Pvap | 0.15 | kPa | 311.30 | Vapor P... |
| Pvap | 0.17 | kPa | 313.50 | Vapor P... |
| Pvap | 0.21 | kPa | 316.40 | Vapor P... |
| Pvap | 0.24 | kPa | 318.30 | Vapor P... |
| Pvap | 0.30 | kPa | 321.40 | Vapor P... |
| Pvap | 0.38 | kPa | 325.40 | Vapor P... |
| Pvap | 0.48 | kPa | 329.50 | Vapor P... |
| Pvap | 0.63 | kPa | 333.50 | Vapor P... |
| n0 | [1.40340; 1.40840] | [298.15; 308.15] |
|
|
| n0 | 1.40840 | 298.15 | Density... | |
| n0 | 1.40840 | 298.15 | Density... | |
| n0 | 1.40600 | 303.15 | Density... | |
| n0 | 1.40610 | 303.15 | Density... | |
| n0 | 1.40340 | 308.15 | Density... | |
| n0 | 1.40390 | 308.15 | Density... | |
| ρl | [1001.60; 1095.94] | kg/m3 | [278.15; 358.15] |
|
| ρl | 1095.94 | kg/m3 | 278.15 | Excess ... |
| ρl | 1084.24 | kg/m3 | 288.14 | Excess ... |
| ρl | 1072.53 | kg/m3 | 298.15 | Excess ... |
| ρl | 1054.92 | kg/m3 | 313.15 | Excess ... |
| ρl | 1037.26 | kg/m3 | 328.15 | Excess ... |
| ρl | 1025.42 | kg/m3 | 338.15 | Excess ... |
| ρl | 1013.53 | kg/m3 | 348.15 | Excess ... |
| ρl | 1001.60 | kg/m3 | 358.15 | Excess ... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 370.20 | K | 2.70 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.68] | kPa | [354.76; 482.88] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.62354e+01 | |||
| Coefficient B | -4.44264e+03 | |||
| Coefficient C | -7.61870e+01 | |||
| Temperature range, min. | 354.76 | |||
| Temperature range, max. | 482.88 | |||
| Pvap | 1.33 | kPa | 354.76 | Calculated Property |
| Pvap | 2.89 | kPa | 369.00 | Calculated Property |
| Pvap | 5.85 | kPa | 383.23 | Calculated Property |
| Pvap | 11.11 | kPa | 397.47 | Calculated Property |
| Pvap | 19.97 | kPa | 411.70 | Calculated Property |
| Pvap | 34.23 | kPa | 425.94 | Calculated Property |
| Pvap | 56.26 | kPa | 440.17 | Calculated Property |
| Pvap | 89.06 | kPa | 454.41 | Calculated Property |
| Pvap | 136.37 | kPa | 468.64 | Calculated Property |
| Pvap | 202.68 | kPa | 482.88 | Calculated Property |
| Pvap | [5.54e-05; 3123.96] | kPa | [232.55; 646.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.25933e+02 | |||
| Coefficient B | -1.13116e+04 | |||
| Coefficient C | -1.60682e+01 | |||
| Coefficient D | 8.62399e-06 | |||
| Temperature range, min. | 232.55 | |||
| Temperature range, max. | 646.00 | |||
| Pvap | 5.54e-05 | kPa | 232.55 | Calculated Property |
| Pvap | 0.01 | kPa | 278.49 | Calculated Property |
| Pvap | 0.39 | kPa | 324.43 | Calculated Property |
| Pvap | 4.66 | kPa | 370.37 | Calculated Property |
| Pvap | 28.26 | kPa | 416.31 | Calculated Property |
| Pvap | 110.82 | kPa | 462.24 | Calculated Property |
| Pvap | 324.43 | kPa | 508.18 | Calculated Property |
| Pvap | 778.75 | kPa | 554.12 | Calculated Property |
| Pvap | 1632.69 | kPa | 600.06 | Calculated Property |
| Pvap | 3123.96 | kPa | 646.00 | Calculated Property |
Similar Compounds
![2-[2-(2-Ethoxyethoxy)ethoxy]ethyl acetate.](data:image/png;base64,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)
Find more compounds similar to Ethanedioic acid, diethyl ester.
Mixtures
- Ethanedioic acid, diethyl ester + Methyl Alcohol
- Ethanedioic acid, diethyl ester + Ethanol
- Ethanedioic acid, diethyl ester + 1-Propanol
- Ethanedioic acid, diethyl ester + Isopropyl Alcohol
- Ethanedioic acid, diethyl ester + 1,4-Dioxane
- Ethanedioic acid, diethyl ester + Anisole
- Ethanedioic acid, diethyl ester + Acetophenone
- Ethanedioic acid, diethyl ester + Cyclopentanone
- Ethanedioic acid, diethyl ester + Cyclohexanone
- Ethanedioic acid, diethyl ester + 3-Pentanone
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Excess molar enthalpies of {diethyl oxalate + (methanol, + ethanol, + 1-propanol, and + 2-propanol)} at T = (288.2, 298.2, 313.2, and 328.2) K and p = 101.3 kPa
- Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethyl Acetoacetate, + Diethyl Oxalate, + Diethyl Phthalate, or + Dioctyl Phthalate at 298.15, 303.15, and 308.15 K
- Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of Anisole with 2-Chloroethanol, 1,4-Dioxane, Tetrachloroethylene, Tetrachloroethane, DMF, DMSO, and Diethyl Oxalate at (298.15, 303.15, and 308.15) K
- Critical Point and Vapor Pressure Measurements for 17 Compounds by a Low Residence Time Flow Method
- Vapor Pressures and Enthalpies of Vaporization of a Series of the Symmetric Linear n-Alkyl Esters of Dicarboxylic Acids
- Densities, Viscosities, and Refractive Indices of Binary Mixtures of Diethyl Oxalate with Some Ketones at (303.15, 308.15, and 313.15) K
- Joback Method
- KDB
- 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.