- InChI
- InChI=1S/C10H18O4/c1-3-7-13-9(11)5-6-10(12)14-8-4-2/h3-8H2,1-2H3
- InChI Key
- SZHZCPHKDJWHNG-UHFFFAOYSA-N
- Formula
- C10H18O4
- SMILES
- CCCOC(=O)CCC(=O)OCCC
- Molecular Weight1
- 202.25
- CAS
- 925-15-5
- Other Names
-
- Di-n-propyl succinate
- Dipropyl butanedioate
- Dipropyl succinate
- Dipropylester kyseliny jantarove
- Succinic acid, dipropyl ester
- 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).
- ΔvapH : Enthalpy of vaporization at a given temperature (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).
- Inp : Non-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° | -434.52 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -739.33 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 27.23 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 56.17 | kJ/mol | Joback Calculated Property |
| log10WS | -1.73 | Crippen Calculated Property | |
| logPoct/wat | 1.673 | Crippen Calculated Property | |
| McVol | 166.640 | ml/mol | McGowan Calculated Property |
| Pc | 2298.11 | kPa | Joback Calculated Property |
| Inp | [1336.00; 1357.00] |
|
|
| Inp | 1357.00 | NIST | |
| Inp | 1338.00 | NIST | |
| Inp | 1339.00 | NIST | |
| Inp | 1336.00 | NIST | |
| Inp | 1338.00 | NIST | |
| Inp | 1357.00 | NIST | |
| Inp | 1336.00 | NIST | |
| Inp | 1336.00 | NIST | |
| Inp | 1357.00 | NIST | |
| Inp | 1338.00 | NIST | |
| Tboil | [521.00; 524.00] | K |
|
| Tboil | 524.00 ± 1.00 | K | NIST |
| Tboil | 521.00 ± 1.50 | K | NIST |
| Tc | 760.87 | K | Joback Calculated Property |
| Tfus | 346.78 | K | Joback Calculated Property |
| Vc | 0.643 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [415.69; 486.74] | J/mol×K | [580.78; 760.87] |
|
| Cp,gas | 415.69 | J/mol×K | 580.78 | Joback Calculated Property |
| Cp,gas | 428.88 | J/mol×K | 610.80 | Joback Calculated Property |
| Cp,gas | 441.54 | J/mol×K | 640.81 | Joback Calculated Property |
| Cp,gas | 453.66 | J/mol×K | 670.83 | Joback Calculated Property |
| Cp,gas | 465.23 | J/mol×K | 700.84 | Joback Calculated Property |
| Cp,gas | 476.26 | J/mol×K | 730.86 | Joback Calculated Property |
| Cp,gas | 486.74 | J/mol×K | 760.87 | Joback Calculated Property |
| η | [0.0001892; 0.0019074] | Pa×s | [346.78; 580.78] |
|
| η | 0.0019074 | Pa×s | 346.78 | Joback Calculated Property |
| η | 0.0010682 | Pa×s | 385.78 | Joback Calculated Property |
| η | 0.0006655 | Pa×s | 424.78 | Joback Calculated Property |
| η | 0.0004489 | Pa×s | 463.78 | Joback Calculated Property |
| η | 0.0003219 | Pa×s | 502.78 | Joback Calculated Property |
| η | 0.0002421 | Pa×s | 541.78 | Joback Calculated Property |
| η | 0.0001892 | Pa×s | 580.78 | Joback Calculated Property |
| ΔvapH | 59.40 | kJ/mol | 437.00 | NIST |
| Pvap | [4.87e-03; 0.07] | kPa | [308.30; 343.50] |
|
| Pvap | 4.87e-03 | kPa | 308.30 | Vapor P... |
| Pvap | 6.85e-03 | kPa | 312.40 | Vapor P... |
| Pvap | 9.36e-03 | kPa | 316.40 | Vapor P... |
| Pvap | 0.01 | kPa | 318.50 | Vapor P... |
| Pvap | 0.01 | kPa | 321.50 | Vapor P... |
| Pvap | 0.02 | kPa | 323.50 | Vapor P... |
| Pvap | 0.02 | kPa | 326.40 | Vapor P... |
| Pvap | 0.03 | kPa | 328.60 | Vapor P... |
| Pvap | 0.03 | kPa | 331.30 | Vapor P... |
| Pvap | 0.04 | kPa | 333.40 | Vapor P... |
| Pvap | 0.04 | kPa | 336.50 | Vapor P... |
| Pvap | 0.05 | kPa | 338.50 | Vapor P... |
| Pvap | 0.06 | kPa | 341.50 | Vapor P... |
| Pvap | 0.07 | kPa | 343.50 | Vapor P... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [394.78; 553.60] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.68825e+01 | |||
| Coefficient B | -6.07022e+03 | |||
| Coefficient C | -2.89960e+01 | |||
| Temperature range, min. | 394.78 | |||
| Temperature range, max. | 553.60 | |||
| Pvap | 1.33 | kPa | 394.78 | Calculated Property |
| Pvap | 2.86 | kPa | 412.43 | Calculated Property |
| Pvap | 5.74 | kPa | 430.07 | Calculated Property |
| Pvap | 10.87 | kPa | 447.72 | Calculated Property |
| Pvap | 19.53 | kPa | 465.37 | Calculated Property |
| Pvap | 33.53 | kPa | 483.01 | Calculated Property |
| Pvap | 55.30 | kPa | 500.66 | Calculated Property |
| Pvap | 87.96 | kPa | 518.31 | Calculated Property |
| Pvap | 135.46 | kPa | 535.95 | Calculated Property |
| Pvap | 202.65 | kPa | 553.60 | Calculated Property |
Similar Compounds
Find more compounds similar to Butanedioic acid, dipropyl ester.
Sources
- Crippen Method
- Crippen Method
- Vapor Pressures and Enthalpies of Vaporization of a Series of the Symmetric Linear n-Alkyl Esters of Dicarboxylic Acids
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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