- InChI
- InChI=1S/C6H10O4/c1-2-10-6(9)4-3-5(7)8/h2-4H2,1H3,(H,7,8)
- InChI Key
- LOLKAJARZKDJTD-UHFFFAOYSA-N
- Formula
- C6H10O4
- SMILES
- CCOC(=O)CCC(=O)O
- Molecular Weight1
- 146.14
- CAS
- 1070-34-4
- Other Names
-
- 4-ethoxy-4-oxobutanoic acid
- Butanedioic acid, 1-ethyl ester
- Butanedioic acid, monoethyl ester
- Monoethyl butanedioate
- Succinic acid monoethyl ester
- monoethyl succinate
- 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).
- 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).
- 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° | -500.02 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -676.78 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 19.77 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 61.53 | kJ/mol | Joback Calculated Property |
| log10WS | -0.30 | Crippen Calculated Property | |
| logPoct/wat | 0.414 | Crippen Calculated Property | |
| McVol | 110.280 | ml/mol | McGowan Calculated Property |
| Pc | 3940.66 | kPa | Joback Calculated Property |
| I | [2350.00; 2395.00] |
|
|
| I | 2367.00 | NIST | |
| I | 2395.00 | NIST | |
| I | 2368.00 | NIST | |
| I | 2350.00 | NIST | |
| Tboil | 559.02 | K | Joback Calculated Property |
| Tc | 738.59 | K | Joback Calculated Property |
| Tfus | 340.29 | K | Joback Calculated Property |
| Vc | 0.420 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [257.90; 301.97] | J/mol×K | [559.02; 738.59] |
|
| Cp,gas | 257.90 | J/mol×K | 559.02 | Joback Calculated Property |
| Cp,gas | 266.10 | J/mol×K | 588.95 | Joback Calculated Property |
| Cp,gas | 273.95 | J/mol×K | 618.88 | Joback Calculated Property |
| Cp,gas | 281.47 | J/mol×K | 648.80 | Joback Calculated Property |
| Cp,gas | 288.64 | J/mol×K | 678.73 | Joback Calculated Property |
| Cp,gas | 295.48 | J/mol×K | 708.66 | Joback Calculated Property |
| Cp,gas | 301.97 | J/mol×K | 738.59 | Joback Calculated Property |
| η | [0.0001317; 0.0052745] | Pa×s | [340.29; 559.02] |
|
| η | 0.0052745 | Pa×s | 340.29 | Joback Calculated Property |
| η | 0.0021175 | Pa×s | 376.75 | Joback Calculated Property |
| η | 0.0009987 | Pa×s | 413.20 | Joback Calculated Property |
| η | 0.0005320 | Pa×s | 449.65 | Joback Calculated Property |
| η | 0.0003115 | Pa×s | 486.11 | Joback Calculated Property |
| η | 0.0001965 | Pa×s | 522.56 | Joback Calculated Property |
| η | 0.0001317 | Pa×s | 559.02 | Joback Calculated Property |
| Pvap | [1.59; 25.70] | kPa | [417.70; 471.90] |
|
| Pvap | 1.59 | kPa | 417.70 | Phase e... |
| Pvap | 2.09 | kPa | 421.20 | Phase e... |
| Pvap | 2.59 | kPa | 425.10 | Phase e... |
| Pvap | 3.09 | kPa | 428.50 | Phase e... |
| Pvap | 3.60 | kPa | 433.00 | Phase e... |
| Pvap | 4.10 | kPa | 435.60 | Phase e... |
| Pvap | 4.60 | kPa | 436.70 | Phase e... |
| Pvap | 5.10 | kPa | 439.80 | Phase e... |
| Pvap | 5.61 | kPa | 440.30 | Phase e... |
| Pvap | 6.11 | kPa | 443.00 | Phase e... |
| Pvap | 6.61 | kPa | 444.30 | Phase e... |
| Pvap | 7.11 | kPa | 445.90 | Phase e... |
| Pvap | 7.61 | kPa | 447.60 | Phase e... |
| Pvap | 8.12 | kPa | 449.10 | Phase e... |
| Pvap | 8.62 | kPa | 450.50 | Phase e... |
| Pvap | 9.12 | kPa | 452.10 | Phase e... |
| Pvap | 9.62 | kPa | 453.20 | Phase e... |
| Pvap | 10.13 | kPa | 454.70 | Phase e... |
| Pvap | 10.63 | kPa | 455.70 | Phase e... |
| Pvap | 11.13 | kPa | 456.50 | Phase e... |
| Pvap | 11.63 | kPa | 457.20 | Phase e... |
| Pvap | 12.14 | kPa | 458.20 | Phase e... |
| Pvap | 12.64 | kPa | 458.40 | Phase e... |
| Pvap | 13.14 | kPa | 459.80 | Phase e... |
| Pvap | 13.64 | kPa | 460.10 | Phase e... |
| Pvap | 14.14 | kPa | 460.30 | Phase e... |
| Pvap | 14.65 | kPa | 461.10 | Phase e... |
| Pvap | 15.15 | kPa | 462.00 | Phase e... |
| Pvap | 15.65 | kPa | 463.30 | Phase e... |
| Pvap | 16.15 | kPa | 463.80 | Phase e... |
| Pvap | 16.66 | kPa | 464.20 | Phase e... |
| Pvap | 17.16 | kPa | 464.50 | Phase e... |
| Pvap | 17.66 | kPa | 465.20 | Phase e... |
| Pvap | 18.16 | kPa | 465.80 | Phase e... |
| Pvap | 18.67 | kPa | 466.70 | Phase e... |
| Pvap | 19.17 | kPa | 467.30 | Phase e... |
| Pvap | 19.67 | kPa | 467.80 | Phase e... |
| Pvap | 20.17 | kPa | 468.30 | Phase e... |
| Pvap | 20.67 | kPa | 468.80 | Phase e... |
| Pvap | 21.18 | kPa | 469.50 | Phase e... |
| Pvap | 21.68 | kPa | 469.70 | Phase e... |
| Pvap | 22.18 | kPa | 469.80 | Phase e... |
| Pvap | 22.68 | kPa | 470.10 | Phase e... |
| Pvap | 23.19 | kPa | 470.30 | Phase e... |
| Pvap | 23.69 | kPa | 470.40 | Phase e... |
| Pvap | 24.19 | kPa | 470.50 | Phase e... |
| Pvap | 24.69 | kPa | 471.10 | Phase e... |
| Pvap | 25.20 | kPa | 471.40 | Phase e... |
| Pvap | 25.70 | kPa | 471.90 | Phase e... |
Similar Compounds
Find more compounds similar to Ethyl hydrogen succinate.
Mixtures
- Ethyl Acetate + Ethyl hydrogen succinate
- Acetic acid + Ethyl hydrogen succinate
- Ethyl hydrogen succinate + Water
- Ethanol + Ethyl hydrogen succinate
Sources
- Crippen Method
- Crippen Method
- Phase equilibria in binary mixtures with monoethyl succinate
- Joback Method
- McGowan Method
- NIST Webbook
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