- InChI
- InChI=1S/C10H18O4/c11-9(12)7-5-3-1-2-4-6-8-10(13)14/h1-8H2,(H,11,12)(H,13,14)
- InChI Key
- CXMXRPHRNRROMY-UHFFFAOYSA-N
- Formula
- C10H18O4
- SMILES
- O=C(O)CCCCCCCCC(=O)O
- Molecular Weight1
- 202.25
- CAS
- 111-20-6
- Other Names
-
- 1,10-Decanedioic acid
- 1,8-Octanedicarboxylic acid
- Decanedicarboxylic acid
- NSC 19492
- Sebacic acid
- Seracic acid
- USAF HC-1
- n-Decanedioic 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).
- 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).
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- 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 | -5425.00 ± 2.10 | kJ/mol | NIST |
| ΔfG° | -498.16 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -779.35 | kJ/mol | Joback Calculated Property |
| ΔfusH° | [0.40; 46.11] | kJ/mol |
|
| ΔfusH° | 0.40 | kJ/mol | Vaporiz... |
| ΔfusH° | 46.11 | kJ/mol | Thermal... |
| ΔfusH° | 44.90 | kJ/mol | Measure... |
| ΔsubH° | 161.00 ± 3.00 | kJ/mol | NIST |
| ΔvapH° | 124.80 | kJ/mol | NIST |
| log10WS | -2.21 | Crippen Calculated Property | |
| logPoct/wat | 2.276 | Crippen Calculated Property | |
| McVol | 166.640 | ml/mol | McGowan Calculated Property |
| Pc | 2500.00 | kPa | Critica... |
| Tboil | 720.30 | K | Joback Calculated Property |
| Tc | 894.41 | K | Joback Calculated Property |
| Tfus | [404.00; 407.00] | K |
|
| Tfus | 404.00 ± 0.40 | K | NIST |
| Tfus | 405.00 ± 1.50 | K | NIST |
| Tfus | 404.00 ± 0.50 | K | NIST |
| Tfus | 407.00 ± 2.00 | K | NIST |
| Tfus | 406.90 ± 1.00 | K | NIST |
| Vc | 0.645 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [473.58; 526.27] | J/mol×K | [720.30; 894.41] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 470 480 490 500 510 520 530 750 800 850 | ||||
| Cp,gas | 473.58 | J/mol×K | 720.30 | Joback Calculated Property |
| Cp,gas | 483.56 | J/mol×K | 749.32 | Joback Calculated Property |
| Cp,gas | 493.05 | J/mol×K | 778.34 | Joback Calculated Property |
| Cp,gas | 502.04 | J/mol×K | 807.35 | Joback Calculated Property |
| Cp,gas | 510.57 | J/mol×K | 836.37 | Joback Calculated Property |
| Cp,gas | 518.64 | J/mol×K | 865.39 | Joback Calculated Property |
| Cp,gas | 526.27 | J/mol×K | 894.41 | Joback Calculated Property |
| η | [0.0000151; 0.0023069] | Pa×s | [423.96; 720.30] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 500 600 700 | ||||
| η | 0.0023069 | Pa×s | 423.96 | Joback Calculated Property |
| η | 0.0006441 | Pa×s | 473.35 | Joback Calculated Property |
| η | 0.0002289 | Pa×s | 522.74 | Joback Calculated Property |
| η | 0.0000972 | Pa×s | 572.13 | Joback Calculated Property |
| η | 0.0000473 | Pa×s | 621.52 | Joback Calculated Property |
| η | 0.0000256 | Pa×s | 670.91 | Joback Calculated Property |
| η | 0.0000151 | Pa×s | 720.30 | Joback Calculated Property |
| ΔfusH | [40.80; 46.90] | kJ/mol | [403.90; 405.70] |
|
|
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 41 42 43 44 45 46 47 404 404.5 405 405.5 | ||||
| ΔfusH | 46.60 | kJ/mol | 403.90 | NIST |
| ΔfusH | 40.81 | kJ/mol | 404.00 | NIST |
| ΔfusH | 40.80 | kJ/mol | 404.00 | NIST |
| ΔfusH | 40.80 | kJ/mol | 404.00 | NIST |
| ΔfusH | 45.30 | kJ/mol | 405.60 | NIST |
| ΔfusH | 46.90 | kJ/mol | 405.70 | NIST |
| ΔsubH | [146.50; 181.00] | kJ/mol | [311.00; 389.00] |
|
| ΔsubH | 146.50 | kJ/mol | 311.00 | NIST |
| ΔsubH | 181.00 ± 8.00 | kJ/mol | 369.00 | NIST |
| ΔsubH | 160.70 ± 2.50 | kJ/mol | 389.00 | NIST |
| ΔvapH | 85.90 | kJ/mol | 540.50 | NIST |
| ΔfusS | 101.00 | J/mol×K | 404.00 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [546.20; 568.20] | K | [6.70; 13.30] |
|
| Tboilr | 546.20 | K | 6.70 | NIST |
| Tboilr | 568.20 | K | 13.30 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [507.74; 679.47] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.69408e+01 | |||
| Coefficient B | -6.61985e+03 | |||
| Coefficient C | -1.10231e+02 | |||
| Temperature range, min. | 507.74 | |||
| Temperature range, max. | 679.47 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 550 600 650 | ||||
| Pvap | 1.33 | kPa | 507.74 | Calculated Property |
| Pvap | 2.86 | kPa | 526.82 | Calculated Property |
| Pvap | 5.73 | kPa | 545.90 | Calculated Property |
| Pvap | 10.85 | kPa | 564.98 | Calculated Property |
| Pvap | 19.49 | kPa | 584.06 | Calculated Property |
| Pvap | 33.47 | kPa | 603.15 | Calculated Property |
| Pvap | 55.22 | kPa | 622.23 | Calculated Property |
| Pvap | 87.87 | kPa | 641.31 | Calculated Property |
| Pvap | 135.39 | kPa | 660.39 | Calculated Property |
| Pvap | 202.65 | kPa | 679.47 | Calculated Property |
Similar Compounds
Find more compounds similar to Decanedioic acid.
Mixtures
- 1,2-Ethanediol + Decanedioic acid
- Ethanol + Decanedioic acid + Cyclohexane
- Ethanol + Decanedioic acid + Heptane
- 1,2-Ethanediol + Decanedioic acid + Water
- Ethanol + Decanedioic acid
- Acetic acid + Decanedioic acid
- Acetone + Decanedioic acid
- Decanedioic acid + Ethyl Acetate
- Decanedioic acid + Water
- Ethanol + Decanedioic acid + Water
- 1-Propanol + Decanedioic acid
- 1-Propanol + Decanedioic acid + Water
- 1-Butanol + Decanedioic acid
- Decanedioic acid + 1-Pentanol
- Decanedioic acid + 1-Hexanol
- Isopropyl Alcohol + Decanedioic acid
- Isopropyl Alcohol + Decanedioic acid + Water
Sources
- Crippen Method
- Crippen Method
- Solubility of decanedioic acid in binary solvent mixtures
- Vaporization, fusion and sublimation enthalpies of the dicarboxylic acids from C4 to C14 and C16
- An odd-even effect on solubility of dicarboxylic acids in organic solvents
- Thermal analysis of phase change materials in the temperature range 120.150 .C
- 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?
- Critical Temperatures and Pressures of Straight-Chain Saturated Dicarboxylic Acids (C4 to C14)
- Solubility of Sebacic Acid in Binary Water + Ethanol Solvent Mixtures
- Solubility of Sebacic Acid in Binary Mixtures Containing Alcohols
- Measurement and Correlation of Solubilities of Decanedioic Acid in C4-C6 Alcohol Solvents
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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