- 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.
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 |
| 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] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 130 140 150 160 170 180 500 600 700 | ||||
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 7000 400 600 800 | ||||
| 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
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.