- InChI
- InChI=1S/C5H8O4/c6-4(7)2-1-3-5(8)9/h1-3H2,(H,6,7)(H,8,9)
- InChI Key
- JFCQEDHGNNZCLN-UHFFFAOYSA-N
- Formula
- C5H8O4
- SMILES
- O=C(O)CCCC(=O)O
- Molecular Weight1
- 132.11
- CAS
- 110-94-1
- Other Names
-
- 1,3-Propanedicarboxylic acid
- 1,5-Pentanedioic acid
- Glutaric acid
- Pentandioic acid
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- 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).
- 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).
- 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).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (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 | [-2151.60; -2150.35] | kJ/mol |
|
| ΔcH°solid | -2150.35 ± 0.75 | kJ/mol | NIST |
| ΔcH°solid | -2150.90 ± 1.20 | kJ/mol | NIST |
| ΔcH°solid | -2151.60 ± 0.50 | kJ/mol | NIST |
| ΔfG° | -540.26 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -676.15 | kJ/mol | Joback Calculated Property |
| ΔfH°solid | [-960.50; -960.00] | kJ/mol |
|
| ΔfH°solid | -960.50 ± 1.10 | kJ/mol | NIST |
| ΔfH°solid | -960.00 ± 1.20 | kJ/mol | NIST |
| ΔfusH° | [2.30; 21.53] | kJ/mol |
|
| ΔfusH° | 2.30 | kJ/mol | Vaporiz... |
| ΔfusH° | 21.01 | kJ/mol | Measure... |
| ΔfusH° | 21.53 | kJ/mol | Solid L... |
| ΔsubH° | 119.80 ± 1.20 | kJ/mol | NIST |
| ΔvapH° | 101.60 | kJ/mol | NIST |
| log10WS | 1.00 | Aq. Sol... | |
| logPoct/wat | 0.326 | Crippen Calculated Property | |
| McVol | 96.190 | ml/mol | McGowan Calculated Property |
| Pc | 4270.00 | kPa | Critica... |
| Tboil | 605.90 | K | Joback Calculated Property |
| Tc | 780.63 | K | Joback Calculated Property |
| Tfus | [369.80; 372.25] | K |
|
| Tfus | 370.25 | K | Aq. Sol... |
| Tfus | 371.60 | K | Determi... |
| Tfus | Outlier 372.25 | K | Solubil... |
| Tfus | 371.00 ± 0.30 | K | NIST |
| Tfus | 371.00 ± 0.30 | K | NIST |
| Tfus | 371.00 ± 0.03 | K | NIST |
| Tfus | 371.00 ± 0.40 | K | NIST |
| Tfus | 371.00 ± 0.30 | K | NIST |
| Tfus | 370.70 ± 1.00 | K | NIST |
| Tfus | 371.00 ± 0.50 | K | NIST |
| Tfus | 370.05 ± 0.50 | K | NIST |
| Tfus | 369.80 ± 0.60 | K | NIST |
| Vc | 0.365 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [232.39; 264.97] | J/mol×K | [605.90; 780.63] |
|
| Cp,gas | 232.39 | J/mol×K | 605.90 | Joback Calculated Property |
| Cp,gas | 238.55 | J/mol×K | 635.02 | Joback Calculated Property |
| Cp,gas | 244.40 | J/mol×K | 664.14 | Joback Calculated Property |
| Cp,gas | 249.96 | J/mol×K | 693.27 | Joback Calculated Property |
| Cp,gas | 255.24 | J/mol×K | 722.39 | Joback Calculated Property |
| Cp,gas | 260.24 | J/mol×K | 751.51 | Joback Calculated Property |
| Cp,gas | 264.97 | J/mol×K | 780.63 | Joback Calculated Property |
| η | [0.0000477; 0.0073782] | Pa×s | [367.61; 605.90] |
|
| η | 0.0073782 | Pa×s | 367.61 | Joback Calculated Property |
| η | 0.0021139 | Pa×s | 407.32 | Joback Calculated Property |
| η | 0.0007563 | Pa×s | 447.04 | Joback Calculated Property |
| η | 0.0003200 | Pa×s | 486.75 | Joback Calculated Property |
| η | 0.0001541 | Pa×s | 526.47 | Joback Calculated Property |
| η | 0.0000823 | Pa×s | 566.18 | Joback Calculated Property |
| η | 0.0000477 | Pa×s | 605.90 | Joback Calculated Property |
| ΔfusH | [18.80; 23.00] | kJ/mol | [363.90; 372.30] |
|
| ΔfusH | 18.80 | kJ/mol | 363.90 | NIST |
| ΔfusH | 20.70 | kJ/mol | 370.90 | NIST |
| ΔfusH | 23.00 | kJ/mol | 371.00 | NIST |
| ΔfusH | 20.90 | kJ/mol | 371.00 | NIST |
| ΔfusH | 21.30 | kJ/mol | 372.30 | NIST |
| ΔsubH | [117.00; 134.00] | kJ/mol | [284.50; 355.50] |
|
| ΔsubH | 132.30 | kJ/mol | 284.50 | NIST |
| ΔsubH | 134.00 ± 4.00 | kJ/mol | 331.00 | NIST |
| ΔsubH | 117.00 ± 1.20 | kJ/mol | 355.50 | NIST |
| ΔvapH | 98.10 | kJ/mol | 502.00 | NIST |
| Pvap | [0.17; 0.55] | kPa | [433.15; 453.15] |
|
| Pvap | 0.17 | kPa | 433.15 | Vapor-L... |
| Pvap | 0.32 | kPa | 443.15 | Vapor-L... |
| Pvap | 0.55 | kPa | 453.15 | Vapor-L... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 473.20 | K | 2.70 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [469.85; 599.42] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.86943e+01 | |||
| Coefficient B | -6.35351e+03 | |||
| Coefficient C | -1.24671e+02 | |||
| Temperature range, min. | 469.85 | |||
| Temperature range, max. | 599.42 | |||
| Pvap | 1.33 | kPa | 469.85 | Calculated Property |
| Pvap | 2.79 | kPa | 484.25 | Calculated Property |
| Pvap | 5.50 | kPa | 498.64 | Calculated Property |
| Pvap | 10.33 | kPa | 513.04 | Calculated Property |
| Pvap | 18.53 | kPa | 527.44 | Calculated Property |
| Pvap | 31.94 | kPa | 541.83 | Calculated Property |
| Pvap | 53.10 | kPa | 556.23 | Calculated Property |
| Pvap | 85.40 | kPa | 570.63 | Calculated Property |
| Pvap | 133.34 | kPa | 585.02 | Calculated Property |
| Pvap | 202.64 | kPa | 599.42 | Calculated Property |
| Pvap | [1.74e-03; 3770.18] | kPa | [370.65; 807.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.83091e+02 | |||
| Coefficient B | -2.04558e+04 | |||
| Coefficient C | -2.28089e+01 | |||
| Coefficient D | 4.85058e-06 | |||
| Temperature range, min. | 370.65 | |||
| Temperature range, max. | 807.00 | |||
| Pvap | 1.74e-03 | kPa | 370.65 | Calculated Property |
| Pvap | 0.08 | kPa | 419.13 | Calculated Property |
| Pvap | 1.20 | kPa | 467.62 | Calculated Property |
| Pvap | 9.74 | kPa | 516.10 | Calculated Property |
| Pvap | 48.74 | kPa | 564.58 | Calculated Property |
| Pvap | 172.37 | kPa | 613.07 | Calculated Property |
| Pvap | 472.82 | kPa | 661.55 | Calculated Property |
| Pvap | 1074.35 | kPa | 710.03 | Calculated Property |
| Pvap | 2121.16 | kPa | 758.52 | Calculated Property |
| Pvap | 3770.18 | kPa | 807.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Pentanedioic acid.
Mixtures
- Water + Pentanedioic acid
- Butanedioic acid + Ethyl Acetate + Pentanedioic acid
- Hexanedioic acid + Ethyl Acetate + Pentanedioic acid
- Octanedioic acid + Pentanedioic acid
- Pentanedioic acid + 2,2-Dimethylbutanedioic acid
- Butanedioic acid + Acetone + Pentanedioic acid
- Hexanedioic acid + Acetone + Pentanedioic acid
- Butanedioic acid + 1-Butanol + Pentanedioic acid
- Hexanedioic acid + 1-Butanol + Pentanedioic acid
- Pentanedioic acid, dimethyl ester + Pentanedioic acid
- Hexanedioic acid + Ethanol + Pentanedioic acid
- Ethanol + Pentanedioic acid
- Acetic acid + Pentanedioic acid
- Acetone + Pentanedioic acid
- Ethyl Acetate + Pentanedioic acid
- Butanedioic acid + Ethanol + Pentanedioic acid
- Propanoic acid + Water + Pentanedioic acid
- Propanoic acid + Pentanedioic acid
- Cyclohexanol + Pentanedioic acid
- Cyclohexanone + Pentanedioic acid
Find more mixtures with Pentanedioic acid.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Determination and correlation of solid-liquid phase equilibrium and phase diagram for multicomponent system of mixed dibasic acids. (I) Ternary system of adipic acid + glutaric acid + ethanol system
- Vaporization, fusion and sublimation enthalpies of the dicarboxylic acids from C4 to C14 and C16
- Volumetric properties of aqueous solutions of glutaric acid
- An odd-even effect on solubility of dicarboxylic acids in organic solvents
- Determination and correlation of solid-liquid phase equilibrium and phase diagram for multicomponent system of mixed dibasic acids. (III) Ternary system of succinic acid + glutaric acid + ethanol system
- Solubility of succinic acid, glutaric acid and adipic acid in propionic acid + epsilon-caprolactone + water mixtures: Experimental measurement and thermodynamic modeling
- Measurement of enthalpy curves of phase change materials via DSC and T-History: When are both methods needed to estimate the behaviour of the bulk material in applications?
- Determination and Correlation for the Solubility of Glutaric Acid in Cyclohexane + Cyclohexanol + Cyclohexanone Solvent Mixtures
- Measurement and Correlation for Solubilities of Adipic Acid, Glutaric Acid and Succinic Acid in Acetic Acid + Cyclohexanone Mixtures
- Measurement and Correlation for Solubilities of Adipic Acid, Glutaric Acid, and Succinic Acid in Dimethyl Adipate + Methanol Mixtures
- Measurement and Correlation for the Solubility of Adipic Acid and Succinic Acid in Glutaric Acid + Cyclohexanone and Glutaric Acid + Acetic Acid Mixtures
- Measurement and Correlation for Solubilities of Succinic Acid and Glutaric Acid in e-Caprolactone + Acetic Acid Mixtures and e-Caprolactone + Cyclohexanone Mixtures
- Solubility Determination and Thermodynamic Modeling of Glutaric Anhydride in Diverse Solvent Systems Consisting of Acetic Acid, Ethanoic Anhydride, and Tetrachloromethane from T = (278.45 to 324.45) K
- Determination and Thermodynamic Modeling of Solid-Liquid Phase Equilibrium for Succinic Acid in the Glutaric Acid + Adipic Acid + Ethyl Acetate Mixture and Adipic Acid in the Succinic Acid + Glutaric Acid + Ethyl Acetate Mixture
- Critical Temperatures and Pressures of Straight-Chain Saturated Dicarboxylic Acids (C4 to C14)
- Solid Liquid Equilibria for Six Binary Mixtures of Pentanedioic Acid, Octanedioic Acid, 3-Methylheptanedioic Acid, 2,2-Dimethylbutanedioic Acid, and 2,3-Dimethylbutanedioic Acid
- Solid Liquid Equilibrium and Phase Diagram for the Ternary Succinic Acid + Glutaric Acid + Water System
- Solubilities of Adipic Acid and Succinic Acid in Glutaric Acid + Acetone or n-butanol Mixture
- Ternary Phase Diagram for Systems of Succinic Acid + Urea + Water, Glutaric Acid + Urea + Water and Adipic Acid + Urea + Water at 288.15 K and 303.15 K
- Vapor-Liquid Equilibrium of Mixtures Containing Adipic Acid, Glutaric Acid, Dimethyl Adipate, Dimethyl Glutarate, Methanol, and Water
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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