- 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
- Seracic acid
- USAF HC-1
- n-decanedioic acid
- sebacic acid
- ω : Acentric Factor.
- 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).
- 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).
- 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 |
|---|---|---|---|
| ω | 0.9950 | Relay (1.0) Calculated Property | |
| ΔcH°solid | -5425.00 ± 2.10 | kJ/mol | NIST |
| ΔfG° | -654.50 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -925.76 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | [0.40; 46.11] | kJ/mol |
|
| ΔfusH° | 0.40 | kJ/mol | Vaporization, fusion and sublimation enthalpies of the dicarboxylic acids from C4 to C14 and C16 |
| ΔfusH° | 46.11 | kJ/mol | Thermal analysis of phase change materials in the temperature range 120.150 .C |
| ΔfusH° | 44.90 | kJ/mol | 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? |
| ΔsubH° | 161.00 ± 3.00 | kJ/mol | NIST |
| ΔvapH° | 124.80 | kJ/mol | NIST |
| IE | 9.80 | eV | Relay (1.0) Calculated Property |
| log10WS | -2.37 | Relay (1.0) Calculated Property | |
| logPoct/wat | 2.276 | Crippen Calculated Property | |
| McVol | 166.640 | ml/mol | McGowan Calculated Property |
| Pc | 2500.00 | kPa | Critical Temperatures and Pressures of Straight-Chain Saturated Dicarboxylic Acids (C4 to C14) |
| Tboil | 559.88 | K | Relay (1.0) Calculated Property |
| Tc | 781.95 | K | Relay (1.0) 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 | 0.644 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔfusH | [40.80; 46.90] | kJ/mol | [403.90; 405.70] |
|
| 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 |
| 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 |
|---|---|---|---|---|
| Cp,gas | [244.86; 556.80] | 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 | 2.99800e+00 | |||
| Coefficient B | 1.05540e+00 | |||
| Coefficient C | -6.65400e-04 | |||
| Coefficient D | 1.63800e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 244.86 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 300.35 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 349.42 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 392.59 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 430.38 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 463.31 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 491.90 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 516.67 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 538.13 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 556.80 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0031566; 0.0002532] | Pa×s | [405.38; 640.02] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.26405e+01 | |||
| Coefficient B | 2.78992e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 405.38 | |||
| Temperature range, max. | 640.02 | |||
| η | 0.0031566 | Pa×s | 405.38 | Calculated Property |
| η | 0.0020826 | Pa×s | 431.45 | Calculated Property |
| η | 0.0014407 | Pa×s | 457.52 | Calculated Property |
| η | 0.0010371 | Pa×s | 483.59 | Calculated Property |
| η | 0.0007721 | Pa×s | 509.66 | Calculated Property |
| η | 0.0005915 | Pa×s | 535.73 | Calculated Property |
| η | 0.0004645 | Pa×s | 561.81 | Calculated Property |
| η | 0.0003727 | Pa×s | 587.88 | Calculated Property |
| η | 0.0003047 | Pa×s | 613.95 | Calculated Property |
| η | 0.0002532 | Pa×s | 640.02 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [507.74; 679.47] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| 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 | |||
| 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 |
| Pvap | [0.14; 96.39] | kPa | [456.00; 625.40] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 2.99022e+01 | |||
| Coefficient B | -2.08650e+04 | |||
| Coefficient C | 1.98202e+02 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 456.00 | |||
| Temperature range, max. | 625.40 | |||
| Pvap | 0.14 | kPa | 456.00 | Calculated Property |
| Pvap | 0.33 | kPa | 474.82 | Calculated Property |
| Pvap | 0.77 | kPa | 493.64 | Calculated Property |
| Pvap | 1.72 | kPa | 512.47 | Calculated Property |
| Pvap | 3.67 | kPa | 531.29 | Calculated Property |
| Pvap | 7.53 | kPa | 550.11 | Calculated Property |
| Pvap | 14.93 | kPa | 568.93 | Calculated Property |
| Pvap | 28.65 | kPa | 587.76 | Calculated Property |
| Pvap | 53.30 | kPa | 606.58 | Calculated Property |
| Pvap | 96.39 | kPa | 625.40 | Calculated Property |
Similar Compounds
Find more compounds similar to Decanedioic acid.
Mixtures
- Ethanol + Decanedioic acid
- Acetic acid + Decanedioic acid
- Acetone + Decanedioic acid
- Decanedioic acid + Ethyl Acetate
- 1,2-Ethanediol + Decanedioic acid
- Ethanol + Decanedioic acid + Cyclohexane
- Ethanol + Decanedioic acid + Heptane
- 1,2-Ethanediol + Decanedioic acid + Water
- 1-Butanol + Decanedioic acid
- Decanedioic acid + 1-Pentanol
- Decanedioic acid + 1-Hexanol
- 2-Propanol + Decanedioic acid
- 2-Propanol + Decanedioic acid + Water
- Decanedioic acid + Water
- Ethanol + Decanedioic acid + Water
- 1-Propanol + Decanedioic acid
- 1-Propanol + Decanedioic acid + Water
Sources
- Cheméo Relay (1.0)
- 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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