- InChI
- InChI=1S/C6H10O4/c1-4(7)9-6(3)10-5(2)8/h6H,1-3H3
- InChI Key
- ACKALUBLCWJVNB-UHFFFAOYSA-N
- Formula
- C6H10O4
- SMILES
- CC(=O)OC(C)OC(C)=O
- Molecular Weight1
- 146.14
- CAS
- 542-10-9
- Other Names
-
- 1,1'-Diacetoxy-ethane
- 1,1-Diacetoxyethane
- 1,1-ETHANEDIOL
- DIACETATE
- Ethylidene acetate
- Ethylidene diacetate
- ethylidene diethanoate
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- 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).
- 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 | 0.4746 | Relay (1.0) Calculated Property | |
| ΔcH°liquid | -2918.70 ± 1.00 | kJ/mol | NIST |
| ΔfH°gas | -812.60 ± 1.10 | kJ/mol | NIST |
| ΔfH°liquid | -871.50 ± 1.00 | kJ/mol | NIST |
| ΔfusH° | 16.51 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [58.90; 59.00] | kJ/mol |
|
| ΔvapH° | 59.00 ± 1.00 | kJ/mol | NIST |
| ΔvapH° | 58.90 | kJ/mol | NIST |
| IE | 10.04 | eV | Relay (1.0) Calculated Property |
| log10WS | -0.73 | Relay (1.0) Calculated Property | |
| logPoct/wat | 0.459 | Crippen Calculated Property | |
| McVol | 110.280 | ml/mol | McGowan Calculated Property |
| Pc | 2970.00 | kPa | Critical Point and Vapor Pressure Measurements for 17 Compounds by a Low Residence Time Flow Method |
| Inp | [786.00; 789.00] |
|
|
| Inp | 789.00 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | 789.00 | NIST | |
| Tboil | 405.95 | K | Relay (1.0) Calculated Property |
| Tc | 588.29 | K | Relay (1.0) Calculated Property |
| Tfus | 292.05 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Vc | 0.435 | 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 |
|---|---|---|---|---|
| ΔvapH | 49.70 | kJ/mol | 390.50 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 339.20 | K | 1.30 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [165.12; 345.63] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 4.65700e+01 | |||
| Coefficient B | 4.70160e-01 | |||
| Coefficient C | -1.16600e-04 | |||
| Coefficient D | -5.45000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 165.12 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 195.90 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 224.39 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 250.44 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 273.86 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 294.49 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 312.15 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 326.68 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 337.90 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 345.63 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0017934; 0.0002409] | Pa×s | [292.05; 446.83] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.21194e+01 | |||
| Coefficient B | 1.69266e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 292.05 | |||
| Temperature range, max. | 446.83 | |||
| η | 0.0017934 | Pa×s | 292.05 | Calculated Property |
| η | 0.0012993 | Pa×s | 309.25 | Calculated Property |
| η | 0.0009738 | Pa×s | 326.44 | Calculated Property |
| η | 0.0007513 | Pa×s | 343.64 | Calculated Property |
| η | 0.0005941 | Pa×s | 360.84 | Calculated Property |
| η | 0.0004799 | Pa×s | 378.04 | Calculated Property |
| η | 0.0003950 | Pa×s | 395.23 | Calculated Property |
| η | 0.0003304 | Pa×s | 412.43 | Calculated Property |
| η | 0.0002803 | Pa×s | 429.63 | Calculated Property |
| η | 0.0002409 | Pa×s | 446.83 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [337.55; 468.47] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.40900e+01 | |||
| Coefficient B | -3.15761e+03 | |||
| Coefficient C | -1.08775e+02 | |||
| Temperature range, min. | 337.55 | |||
| Temperature range, max. | 468.47 | |||
| Pvap | 1.33 | kPa | 337.55 | Calculated Property |
| Pvap | 3.04 | kPa | 352.10 | Calculated Property |
| Pvap | 6.33 | kPa | 366.64 | Calculated Property |
| Pvap | 12.17 | kPa | 381.19 | Calculated Property |
| Pvap | 21.90 | kPa | 395.74 | Calculated Property |
| Pvap | 37.24 | kPa | 410.28 | Calculated Property |
| Pvap | 60.30 | kPa | 424.83 | Calculated Property |
| Pvap | 93.59 | kPa | 439.38 | Calculated Property |
| Pvap | 139.97 | kPa | 453.92 | Calculated Property |
| Pvap | 202.63 | kPa | 468.47 | Calculated Property |
| Pvap | [0.04; 3249.39] | kPa | [292.00; 635.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 3.44052e+02 | |||
| Coefficient B | -2.10841e+04 | |||
| Coefficient C | -4.89250e+01 | |||
| Coefficient D | 3.21924e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 292.00 | |||
| Temperature range, max. | 635.00 | |||
| Pvap | 0.04 | kPa | 292.00 | Calculated Property |
| Pvap | 0.95 | kPa | 330.11 | Calculated Property |
| Pvap | 7.97 | kPa | 368.22 | Calculated Property |
| Pvap | 35.80 | kPa | 406.33 | Calculated Property |
| Pvap | 108.31 | kPa | 444.44 | Calculated Property |
| Pvap | 255.65 | kPa | 482.56 | Calculated Property |
| Pvap | 520.00 | kPa | 520.67 | Calculated Property |
| Pvap | 976.45 | kPa | 558.78 | Calculated Property |
| Pvap | 1777.53 | kPa | 596.89 | Calculated Property |
| Pvap | 3249.39 | kPa | 635.00 | Calculated Property |
Similar Compounds
![2-[2-(2-Ethoxyethoxy)ethoxy]ethyl acetate.](data:image/png;base64,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)
![2-[2-[2-[2-(2-Acetyloxyethoxy)ethoxy]ethoxy]ethoxy]ethyl acetate.](data:image/png;base64,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)
![2-[2-[2-[2-[2-[2-[2-(2-Acetyloxyethoxy)ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethoxy]ethyl acetate.](data:image/png;base64,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)
Find more compounds similar to 1,1-Ethanediol, diacetate.
Sources
- KDB Vapor Pressure Data
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Critical Point and Vapor Pressure Measurements for 17 Compounds by a Low Residence Time Flow Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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