- 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).
- 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).
- 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).
- 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 |
|---|---|---|---|
| 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 |
| ΔfG° | -304.24 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -527.90 ± 1.70 | kJ/mol | NIST |
| ΔfH°solid | -608.60 ± 0.70 | kJ/mol | NIST |
| ΔfusH° | 5.98 | 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° | 38.07 | kJ/mol | Joback 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 |
| log10WS | -0.03 | Crippen Calculated Property | |
| logPoct/wat | -0.150 | Crippen Calculated Property | |
| McVol | 65.370 | ml/mol | McGowan Calculated Property |
| Pc | 5670.27 | kPa | Joback Calculated Property |
| Inp | 1022.00 | NIST | |
| Tboil | 534.20 | K | NIST |
| Tc | 717.29 | K | Joback Calculated Property |
| Tfus | [392.00; 393.17] | K |
|
| Tfus | 393.17 | K | Measure... |
| Tfus | 392.60 ± 1.00 | K | NIST |
| Tfus | 393.15 ± 1.50 | K | NIST |
| Tfus | 392.00 ± 1.00 | K | NIST |
| Vc | 0.236 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [133.07; 184.46] | J/mol×K | [473.46; 717.29] |
|
| Cp,gas | 133.07 | J/mol×K | 473.46 | Joback Calculated Property |
| Cp,gas | 142.43 | J/mol×K | 514.10 | Joback Calculated Property |
| Cp,gas | 151.55 | J/mol×K | 554.74 | Joback Calculated Property |
| Cp,gas | 160.37 | J/mol×K | 595.37 | Joback Calculated Property |
| Cp,gas | 168.82 | J/mol×K | 636.01 | Joback Calculated Property |
| Cp,gas | 176.87 | J/mol×K | 676.65 | Joback Calculated Property |
| Cp,gas | 184.46 | J/mol×K | 717.29 | Joback Calculated Property |
| 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 | Isobari... |
| Pvap | 30.00 | kPa | 488.81 | Isobari... |
| Pvap | 40.00 | kPa | 499.14 | Isobari... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.87; 6722.70] | kPa | [393.00; 811.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.01282e+02 | |||
| Coefficient B | -1.15330e+04 | |||
| Coefficient C | -1.22030e+01 | |||
| Coefficient D | 5.30723e-06 | |||
| 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 |
Similar Compounds
Find more compounds similar to Succinic anhydride.
Mixtures
Sources
- KDB Vapor Pressure Data
- 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
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