- InChI
- InChI=1S/C4H2O3/c5-3-1-2-4(6)7-3/h1-2H
- InChI Key
- FPYJFEHAWHCUMM-UHFFFAOYSA-N
- Formula
- C4H2O3
- SMILES
- O=C1C=CC(=O)O1
- Molecular Weight1
- 98.06
- CAS
- 108-31-6
- Other Names
-
- (Z)-butenedioic acid anhydride
- 2,5-Furanedione
- 2,5-furandione
- Anhydrid kyseliny maleinove
- Dihydro-2,5-dioxofuran
- M 188
- Maleic acid anhydride
- Maleic anhydride, briquettes
- Maleinanhydrid
- NSC 137651
- Rcra waste number U147
- Toxilic anhydride
- UN 2215
- cis-butenedioic anhydride
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,solid : Solid phase heat capacity (J/mol×K).
- EA : Electron affinity (eV).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°solid : Solid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔsubH° : Enthalpy of sublimation at standard conditions (kJ/mol).
- ΔsubH : Enthalpy of sublimation at a given temperature (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).
- Inp : Non-polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (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°solid | [-1390.30; -1389.50] | kJ/mol |
|
| ΔcH°solid | -1389.50 ± 0.67 | kJ/mol | NIST |
| ΔcH°solid | -1390.30 ± 0.71 | kJ/mol | NIST |
| EA | [1.40; 1.44] | eV |
|
| EA | 1.44 ± 0.09 | eV | NIST |
| EA | 1.44 ± 0.05 | eV | NIST |
| EA | 1.40 ± 0.20 | eV | NIST |
| ΔfG° | -274.28 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -394.69 | kJ/mol | Joback Calculated Property |
| ΔfH°solid | [-470.41; -469.60] | kJ/mol |
|
| ΔfH°solid | -470.41 ± 0.71 | kJ/mol | NIST |
| ΔfH°solid | -469.60 ± 0.30 | kJ/mol | NIST |
| ΔfusH° | 7.20 | kJ/mol | Joback Calculated Property |
| ΔsubH° | 70.00 | kJ/mol | NIST |
| ΔvapH° | 38.36 | kJ/mol | Joback Calculated Property |
| IE | [11.07; 11.45] | eV |
|
| IE | 11.07 | eV | NIST |
| IE | 11.11 ± 0.05 | eV | NIST |
| IE | 11.10 | eV | NIST |
| IE | 11.45 | eV | NIST |
| log10WS | 0.12 | Crippen Calculated Property | |
| logPoct/wat | -0.374 | Crippen Calculated Property | |
| McVol | 61.070 | ml/mol | McGowan Calculated Property |
| Pc | 5990.66 | kPa | Joback Calculated Property |
| Inp | [790.00; 833.00] |
|
|
| Inp | 827.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 833.00 | NIST | |
| Inp | 791.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 833.00 | NIST | |
| Tboil | 473.20 | K | NIST |
| Tc | 719.14 | K | Joback Calculated Property |
| Tfus | [325.60; 325.95] | K |
|
| Tfus | 325.60 | K | Isobari... |
| Tfus | 325.60 | K | Isobari... |
| Tfus | 325.95 | K | Measure... |
| Tfus | 325.60 | K | Isother... |
| Tfus | 325.80 | K | Isobari... |
| Ttriple | 325.72 ± 0.02 | K | NIST |
| Vc | 0.223 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [117.47; 160.44] | J/mol×K | [472.62; 719.14] |
|
| Cp,gas | 117.47 | J/mol×K | 472.62 | Joback Calculated Property |
| Cp,gas | 125.28 | J/mol×K | 513.71 | Joback Calculated Property |
| Cp,gas | 132.91 | J/mol×K | 554.79 | Joback Calculated Property |
| Cp,gas | 140.29 | J/mol×K | 595.88 | Joback Calculated Property |
| Cp,gas | 147.37 | J/mol×K | 636.96 | Joback Calculated Property |
| Cp,gas | 154.11 | J/mol×K | 678.05 | Joback Calculated Property |
| Cp,gas | 160.44 | J/mol×K | 719.14 | Joback Calculated Property |
| Cp,solid | [67.40; 123.20] | J/mol×K | [298.15; 310.00] |
|
| Cp,solid | 67.40 | J/mol×K | 298.15 | NIST |
| Cp,solid | 119.90 | J/mol×K | 300.00 | NIST |
| Cp,solid | 123.20 | J/mol×K | 310.00 | NIST |
| ΔfusH | [12.26; 13.65] | kJ/mol | [325.00; 326.00] |
|
| ΔfusH | 12.93 | kJ/mol | 325.00 | NIST |
| ΔfusH | 13.60 | kJ/mol | 325.30 | NIST |
| ΔfusH | 12.26 | kJ/mol | 325.64 | NIST |
| ΔfusH | 12.26 | kJ/mol | 325.70 | NIST |
| ΔfusH | 12.26 | kJ/mol | 325.70 | NIST |
| ΔfusH | 13.55 | kJ/mol | 325.72 | NIST |
| ΔfusH | 13.65 | kJ/mol | 326.00 | NIST |
| ΔsubH | [68.80; 85.40] | kJ/mol | [258.00; 317.00] |
|
| ΔsubH | 68.80 | kJ/mol | 258.00 | NIST |
| ΔsubH | 71.50 ± 5.00 | kJ/mol | 316.50 | NIST |
| ΔsubH | 85.40 | kJ/mol | 317.00 | NIST |
| ΔvapH | [49.10; 56.70] | kJ/mol | [325.80; 405.50] |
|
| ΔvapH | 54.80 | kJ/mol | 325.80 | NIST |
| ΔvapH | 54.80 | kJ/mol | 338.00 | NIST |
| ΔvapH | 56.70 | kJ/mol | 396.00 | NIST |
| ΔvapH | 49.10 | kJ/mol | 405.50 | NIST |
| ΔfusS | [37.60; 41.80] | J/mol×K | [325.00; 325.72] |
|
| ΔfusS | 39.80 | J/mol×K | 325.00 | NIST |
| ΔfusS | 41.80 | J/mol×K | 325.30 | NIST |
| ΔfusS | 37.60 | J/mol×K | 325.64 | NIST |
| ΔfusS | 41.60 | J/mol×K | 325.72 | NIST |
Similar Compounds
Find more compounds similar to Maleic anhydride.
Mixtures
- Maleic anhydride + 1,2-Cyclohexanedicarboxylic acid, diisobutyl ester
- Dimethyl phthalate + Maleic anhydride
- Decanedioic acid, dibutyl ester + Maleic anhydride
- Maleic anhydride + Formamide, N,N-dimethyl-
- Maleic anhydride + Methyl Alcohol
- Maleic anhydride + Acetic acid
- Acetonitrile + Maleic anhydride
- Maleic anhydride + Acetone
- Maleic anhydride + Ethyl Acetate
- Maleic anhydride + Isopropyl Alcohol
- Maleic anhydride + 1-Butanol
- Dibutyl phthalate + Maleic anhydride
- Diethyl Phthalate + Maleic anhydride
Sources
- Crippen Method
- Crippen Method
- Isobaric vapor liquid equilibria of the binary system maleic anhydride and di-isobutyl hexahydrophthalate at 2.67, 5.33 and 8.00 kPa
- Isobaric vapor-liquid equilibria of the binary system maleic anhydride and dimethyl phthalate at 2.67, 5.33 and 8.00 kPa
- Isobaric vapor liquid equilibria of the binary system: Maleic anhydride + di-n-butylsebacate at 2.67, 5.33 and 8.00 kPa
- Measurement and correlation of the solubility of maleic anhydride in different organic solvents
- Isothermal (vapor + liquid) equilibria of maleic anhydride + di-isobutyl hexahydrophthalate and maleic anhydride + di-n-butyl phthalate systems at T= (413.2, 433.2 and 453.2) K
- Isobaric (vapor + liquid) equilibria of the binary system maleic anhydride and diethyl phthalate at p = (2.67, 5.33, and 8.00) kPa
- Joback Method
- McGowan Method
- NIST Webbook
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