- InChI
- InChI=1S/C12H20O4/c1-3-5-9-15-11(13)7-8-12(14)16-10-6-4-2/h7-8H,3-6,9-10H2,1-2H3/b8-7-
- InChI Key
- JBSLOWBPDRZSMB-FPLPWBNLSA-N
- Formula
- C12H20O4
- SMILES
- CCCCOC(=O)C=CC(=O)OCCCC
- Molecular Weight1
- 228.28
- CAS
- 105-76-0
- Other Names
-
- 2-Butenedioic acid (2Z)-, 1,4-dibutyl ester
- 2-Butenedioic acid (2Z)-, dibutyl ester
- 2-Butenedioic acid, dibutyl ester, cis-
- Bibutyl maleate
- Bisomer DBM
- Butyl maleate
- DBM
- Dibutyl (2z)-2-butenedioate
- Dibutyl maleate
- Dibutylester kyseliny maleinove
- Maleic acid, dibutyl ester
- Octomer DBM
- PX-504
- RC Comonomer DBM
- Staflex DBM
- cis-butenedioic acid, dibutyl ester
- di-n-Butyl maleate
- dibutyl cis-butendioate
- dibutyl maleinate
- 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).
- ρl : Liquid Density (kg/m3).
- 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° | -337.46 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -663.39 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 32.61 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 60.58 | kJ/mol | Joback Calculated Property |
| log10WS | -2.42 | Crippen Calculated Property | |
| logPoct/wat | 2.229 | Crippen Calculated Property | |
| McVol | 190.520 | ml/mol | McGowan Calculated Property |
| Pc | 2018.13 | kPa | Joback Calculated Property |
| Inp | [1505.00; 1505.00] |
|
|
| Inp | 1505.00 | NIST | |
| Inp | 1505.00 | NIST | |
| Inp | 1505.00 | NIST | |
| Inp | 1505.00 | NIST | |
| Tboil | [553.40; 554.20] | K |
|
| Tboil | 554.20 | K | NIST |
| Tboil | 553.40 ± 0.50 | K | NIST |
| Tc | 814.25 | K | Joback Calculated Property |
| Tfus | 364.24 | K | Joback Calculated Property |
| Vc | 0.736 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [495.03; 569.75] | J/mol×K | [630.70; 814.25] |
|
| Cp,gas | 495.03 | J/mol×K | 630.70 | Joback Calculated Property |
| Cp,gas | 509.10 | J/mol×K | 661.29 | Joback Calculated Property |
| Cp,gas | 522.51 | J/mol×K | 691.88 | Joback Calculated Property |
| Cp,gas | 535.27 | J/mol×K | 722.48 | Joback Calculated Property |
| Cp,gas | 547.40 | J/mol×K | 753.07 | Joback Calculated Property |
| Cp,gas | 558.89 | J/mol×K | 783.66 | Joback Calculated Property |
| Cp,gas | 569.75 | J/mol×K | 814.25 | Joback Calculated Property |
| η | [0.0001303; 0.0015837] | Pa×s | [364.24; 630.70] |
|
| η | 0.0015837 | Pa×s | 364.24 | Joback Calculated Property |
| η | 0.0008330 | Pa×s | 408.65 | Joback Calculated Property |
| η | 0.0004970 | Pa×s | 453.06 | Joback Calculated Property |
| η | 0.0003252 | Pa×s | 497.47 | Joback Calculated Property |
| η | 0.0002281 | Pa×s | 541.88 | Joback Calculated Property |
| η | 0.0001688 | Pa×s | 586.29 | Joback Calculated Property |
| η | 0.0001303 | Pa×s | 630.70 | Joback Calculated Property |
| ΔvapH | 41.10 | kJ/mol | 402.50 | NIST |
| ρl | 990.10 | kg/m3 | 293.15 | Correla... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [411.56; 586.19] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.78368e+01 | |||
| Coefficient B | -7.64066e+03 | |||
| Coefficient C | 2.38300e+01 | |||
| Temperature range, min. | 411.56 | |||
| Temperature range, max. | 586.19 | |||
| Pvap | 1.33 | kPa | 411.56 | Calculated Property |
| Pvap | 2.82 | kPa | 430.96 | Calculated Property |
| Pvap | 5.61 | kPa | 450.37 | Calculated Property |
| Pvap | 10.56 | kPa | 469.77 | Calculated Property |
| Pvap | 18.97 | kPa | 489.17 | Calculated Property |
| Pvap | 32.64 | kPa | 508.58 | Calculated Property |
| Pvap | 54.07 | kPa | 527.98 | Calculated Property |
| Pvap | 86.54 | kPa | 547.38 | Calculated Property |
| Pvap | 134.29 | kPa | 566.79 | Calculated Property |
| Pvap | 202.66 | kPa | 586.19 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Butenedioic acid (Z)-, dibutyl ester.
Mixtures
- Propanoic acid + Water + 2-Butenedioic acid (Z)-, dibutyl ester
- Water + 2-Butenedioic acid (Z)-, dibutyl ester
Sources
- Crippen Method
- Crippen Method
- Correlation of Experimental Liquid Liquid Equilibrium Data for Ternary Systems Using NRTL and GMDH-Type Neural Network
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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