- InChI
- InChI=1S/C4H4O3/c5-3-1-2-4(6)7-3/h1-2H2
- InChI Key
- RINCXYDBBGOEEQ-UHFFFAOYSA-N
- Formula
- C4H4O3
- SMILES
- O=C1CCC(=O)O1
- Molecular Weight1
- 100.07
- CAS
- 108-30-5
- Other Names
-
- 2,5(3H,4H)-Furandione
- 2,5-Diketotetrahydrofuran
- 2,5-Dioxotetrahydrofuran
- 2,5-Furandione, dihydro-
- Bernsteinsaure-anhydrid
- Butanedioic anhydride
- Dihydro-2,5-diketotetrahydrofuran
- Dihydro-2,5-furandione
- NCI-C55696
- NSC 8518
- Rikacid SA
- Succinic acid anhydride
- Succinyl anhydride
- Succinyl oxide
- Tetrahydro-2,5-dioxofuran
- Tetrahydro-2,5-furandione
- butanedioic acid, anhydride
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- 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).
- 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).
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pvap : Vapor pressure (kPa).
- Inp : Non-polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- 1: Molecular weight from the IUPAC atomic weights tables.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°solid | [-1543.90; -1537.10] | kJ/mol |
|
| ΔcH°solid | -1537.10 ± 0.40 | kJ/mol | NIST |
| ΔcH°solid | -1543.90 ± 0.63 | kJ/mol | NIST |
| ΔfH°gas | -527.90 ± 1.70 | kJ/mol | NIST |
| ΔfH°solid | -608.60 ± 0.70 | kJ/mol | NIST |
| ΔfusH° | 7.06 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [80.70; 80.70] | kJ/mol |
|
| ΔsubH° | 80.70 ± 1.60 | kJ/mol | NIST |
| ΔsubH° | 80.70 ± 1.60 | kJ/mol | NIST |
| ΔsubH° | 80.70 | kJ/mol | NIST |
| ΔvapH° | 49.82 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [10.80; 10.84] | eV |
|
| IE | 10.84 | eV | NIST |
| IE | 10.84 | eV | NIST |
| IE | 10.84 | eV | NIST |
| IE | 10.80 | eV | NIST |
| logPoct/wat | -0.150 | Crippen Calculated Property | |
| McVol | 65.370 | ml/mol | McGowan Calculated Property |
| Inp | 1022.00 | NIST | |
| Tboil | 534.20 | K | NIST |
| Tfus | [392.00; 393.17] | K |
|
| Tfus | 393.17 | K | Measurement and correlation of solubility of succinic anhydride in pure solvents and binary solvent mixtures |
| Tfus | 392.60 ± 1.00 | K | NIST |
| Tfus | 393.15 ± 1.50 | K | NIST |
| Tfus | 392.00 ± 1.00 | K | NIST |
Cheméo can also estimate Critical Temperature, Critical Pressure, Critical Volume, Standard Gibbs free energy of formation, Acentric Factor, Log10 of Water solubility in mol/l for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔsubH | [80.50; 82.20] | kJ/mol | [300.50; 309.00] |
|
| ΔsubH | 82.20 | kJ/mol | 300.50 | NIST |
| ΔsubH | 80.50 ± 1.60 | kJ/mol | 309.00 | NIST |
| ΔvapH | 57.30 | kJ/mol | 467.50 | NIST |
| Pvap | [20.00; 40.00] | kPa | [475.01; 499.14] |
|
| Pvap | 20.00 | kPa | 475.01 | Isobaric Vapor Liquid Equilibrium for Binary System of -Butyrolactone + Succinic Anhydride at 20.0, 30.0, and 40.0 kPa |
| Pvap | 30.00 | kPa | 488.81 | Isobaric Vapor Liquid Equilibrium for Binary System of -Butyrolactone + Succinic Anhydride at 20.0, 30.0, and 40.0 kPa |
| Pvap | 40.00 | kPa | 499.14 | Isobaric Vapor Liquid Equilibrium for Binary System of -Butyrolactone + Succinic Anhydride at 20.0, 30.0, and 40.0 kPa |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [87.34; 206.01] | 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 | 4.91000e+00 | |||
| Coefficient B | 3.38100e-01 | |||
| Coefficient C | -1.30800e-04 | |||
| Coefficient D | -6.20000e-09 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 87.34 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 107.88 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 126.62 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 143.56 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 158.66 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 171.91 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 183.29 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 192.78 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 200.36 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 206.01 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.87; 6722.70] | kPa | [393.00; 811.00] |
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 | 1.01282e+02 | |||
| Coefficient B | -1.15330e+04 | |||
| Coefficient C | -1.22030e+01 | |||
| Coefficient D | 5.30723e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 393.00 | |||
| Temperature range, max. | 811.00 | |||
| Pvap | 0.87 | kPa | 393.00 | Calculated Property |
| Pvap | 6.06 | kPa | 439.44 | Calculated Property |
| Pvap | 27.44 | kPa | 485.89 | Calculated Property |
| Pvap | 91.81 | kPa | 532.33 | Calculated Property |
| Pvap | 247.48 | kPa | 578.78 | Calculated Property |
| Pvap | 570.44 | kPa | 625.22 | Calculated Property |
| Pvap | 1172.85 | kPa | 671.67 | Calculated Property |
| Pvap | 2218.02 | kPa | 718.11 | Calculated Property |
| Pvap | 3946.85 | kPa | 764.56 | Calculated Property |
| Pvap | 6722.70 | kPa | 811.00 | Calculated Property |
| Pvap | [0.14; 94.32] | kPa | [365.00; 534.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.30147e+01 | |||
| Coefficient B | -3.30162e+03 | |||
| Coefficient C | -1.44107e+02 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 365.00 | |||
| Temperature range, max. | 534.00 | |||
| Pvap | 0.14 | kPa | 365.00 | Calculated Property |
| Pvap | 0.47 | kPa | 383.78 | Calculated Property |
| Pvap | 1.27 | kPa | 402.56 | Calculated Property |
| Pvap | 3.02 | kPa | 421.33 | Calculated Property |
| Pvap | 6.43 | kPa | 440.11 | Calculated Property |
| Pvap | 12.50 | kPa | 458.89 | Calculated Property |
| Pvap | 22.57 | kPa | 477.67 | Calculated Property |
| Pvap | 38.25 | kPa | 496.44 | Calculated Property |
| Pvap | 61.45 | kPa | 515.22 | Calculated Property |
| Pvap | 94.32 | kPa | 534.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Succinic anhydride.
Mixtures
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Cheméo Relay (1.0, beta) Beta: served but experimental, data-limited and below our cross-validation release bar; the Joback value is recommended where available.
- Crippen Method
- Crippen Method
- Measurement and correlation of solubility of succinic anhydride in pure solvents and binary solvent mixtures
- Isobaric Vapor Liquid Equilibrium for Binary System of -Butyrolactone + Succinic Anhydride at 20.0, 30.0, and 40.0 kPa
- Joback Method
- McGowan Method
- NIST Webbook
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
These property values are available through the Cheméo API. A free account gives you an access key.