- InChI
- InChI=1S/C14H28O2/c1-2-3-4-5-6-7-8-9-10-11-12-13-14(15)16/h2-13H2,1H3,(H,15,16)
- InChI Key
- TUNFSRHWOTWDNC-UHFFFAOYSA-N
- Formula
- C14H28O2
- SMILES
- CCCCCCCCCCCCCC(=O)O
- Molecular Weight1
- 228.37
- CAS
- 544-63-8
- Other Names
-
- 1-Tridecanecarboxylic acid
- Acide Myristique
- Crodacid
- Emery 655
- Hydrofol acid 1495
- Hystrene 9014
- Hystrene 9514
- Myristic acid (tetradecanoic acid)
- N-MYRISTIC ACID
- NSC 5028
- Neo-Fat 14
- Philacid 1400
- Prifac 2942
- Prifrac 2942
- Tetradecanoic (Myristic) acid
- Tetradecanoic acid (=Myristic acid)
- Tetradecanoic acid (myristic acid)
- Univol U 316S
- myristic acid
- n-Tetradecan-1-oic acid
- n-Tetradecanoic acid
- n-Tetradecoic acid
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,solid : Solid phase 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).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- 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).
- Ttriple : Triple Point Temperature (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 | 0.9700 | Relay (1.0) Calculated Property | |
| ΔcH°liquid | -8676.70 ± 1.40 | kJ/mol | NIST |
| ΔcH°solid | -8675.90 ± 9.60 | kJ/mol | NIST |
| ΔfG° | -276.91 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -693.07 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | [43.70; 44.75] | kJ/mol |
|
| ΔfusH° | 44.75 | kJ/mol | Solid-liquid phase equilibria of (n-octadecane with myristic, and palmitic acid) binary mixtures used as phase change materials (PCMs) |
| ΔfusH° | 43.70 | kJ/mol | Solid-Liquid Equilibrium of Binary Systems Containing Fatty Acids and Fatty Alcohols Using Differential Scanning Calorimetry |
| ΔsubH° | 169.00 ± 9.00 | kJ/mol | NIST |
| ΔvapH° | 107.40 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.95 | eV | Relay (1.0) Calculated Property |
| log10WS | -5.33 | Aq. Solubility Prediction | |
| logPoct/wat | 4.772 | Crippen Calculated Property | |
| McVol | 215.560 | ml/mol | McGowan Calculated Property |
| Pc | 1644.20 ± 85.00 | kPa | NIST |
| Ptriple | 2.13e-05 ± 1.07e-05 | kPa | NIST |
| Inp | [288.93; 1800.00] |
|
|
| Inp | 1763.00 | NIST | |
| Inp | 1767.00 | NIST | |
| Inp | 1738.00 | NIST | |
| Inp | 1778.00 | NIST | |
| Inp | 1735.00 | NIST | |
| Inp | 1784.00 | NIST | |
| Inp | 1765.00 | NIST | |
| Inp | 1740.00 | NIST | |
| Inp | 1750.00 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1763.00 | NIST | |
| Inp | 1763.00 | NIST | |
| Inp | 1761.00 | NIST | |
| Inp | 1768.00 | NIST | |
| Inp | 1769.00 | NIST | |
| Inp | 1775.00 | NIST | |
| Inp | 1748.00 | NIST | |
| Inp | 1780.00 | NIST | |
| Inp | 1770.00 | NIST | |
| Inp | 1767.10 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1772.00 | NIST | |
| Inp | 1765.00 | NIST | |
| Inp | 1787.00 | NIST | |
| Inp | 1787.00 | NIST | |
| Inp | 1769.70 | NIST | |
| Inp | 1770.00 | NIST | |
| Inp | 1748.00 | NIST | |
| Inp | 1748.00 | NIST | |
| Inp | 1768.00 | NIST | |
| Inp | 1776.00 | NIST | |
| Inp | 1780.00 | NIST | |
| Inp | 1798.00 | NIST | |
| Inp | 1770.00 | NIST | |
| Inp | 1771.00 | NIST | |
| Inp | 1771.00 | NIST | |
| Inp | 1770.00 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1772.00 | NIST | |
| Inp | 1767.00 | NIST | |
| Inp | 1759.00 | NIST | |
| Inp | 1752.00 | NIST | |
| Inp | 1771.00 | NIST | |
| Inp | 1777.00 | NIST | |
| Inp | 1767.00 | NIST | |
| Inp | 1771.00 | NIST | |
| Inp | 1752.00 | NIST | |
| Inp | 1743.00 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1743.00 | NIST | |
| Inp | 1743.00 | NIST | |
| Inp | 1769.00 | NIST | |
| Inp | 1772.71 | NIST | |
| Inp | 1774.64 | NIST | |
| Inp | 1769.00 | NIST | |
| Inp | 1751.00 | NIST | |
| Inp | 1731.00 | NIST | |
| Inp | 1737.00 | NIST | |
| Inp | 1740.00 | NIST | |
| Inp | 1737.27 | NIST | |
| Inp | 1763.00 | NIST | |
| Inp | 1779.00 | NIST | |
| Inp | 1758.20 | NIST | |
| Inp | 1767.00 | NIST | |
| Inp | 1770.00 | NIST | |
| Inp | 1752.10 | NIST | |
| Inp | 1756.00 | NIST | |
| Inp | 1739.00 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1747.00 | NIST | |
| Inp | 1747.00 | NIST | |
| Inp | 1761.00 | NIST | |
| Inp | 1751.00 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1763.00 | NIST | |
| Inp | 1766.00 | NIST | |
| Inp | 1744.00 | NIST | |
| Inp | 1774.00 | NIST | |
| Inp | 1767.00 | NIST | |
| Inp | 1761.00 | NIST | |
| Inp | 1765.00 | NIST | |
| Inp | 1763.00 | NIST | |
| Inp | 1763.00 | NIST | |
| Inp | 1746.00 | NIST | |
| Inp | 1761.00 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1747.00 | NIST | |
| Inp | 1763.00 | NIST | |
| Inp | 1780.00 | NIST | |
| Inp | 1765.00 | NIST | |
| Inp | 1771.00 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1748.00 | NIST | |
| Inp | 1742.00 | NIST | |
| Inp | 1742.00 | NIST | |
| Inp | 1741.00 | NIST | |
| Inp | 1771.00 | NIST | |
| Inp | 1765.00 | NIST | |
| Inp | 1769.00 | NIST | |
| Inp | 1782.00 | NIST | |
| Inp | 1769.00 | NIST | |
| Inp | 1769.00 | NIST | |
| Inp | 1771.00 | NIST | |
| Inp | 1750.00 | NIST | |
| Inp | 1765.00 | NIST | |
| Inp | 1764.00 | NIST | |
| Inp | 1769.00 | NIST | |
| Inp | 1765.00 | NIST | |
| Inp | 1768.00 | NIST | |
| Inp | 1757.00 | NIST | |
| Inp | 1782.00 | NIST | |
| Inp | 1769.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1769.00 | NIST | |
| Inp | 1770.00 | NIST | |
| Inp | 1771.00 | NIST | |
| Inp | 1768.00 | NIST | |
| Inp | 1773.00 | NIST | |
| Inp | 1795.00 | NIST | |
| Inp | 1777.00 | NIST | |
| Inp | 1780.00 | NIST | |
| Inp | 1770.00 | NIST | |
| Inp | 1765.00 | NIST | |
| Inp | 1776.00 | NIST | |
| Inp | 1783.00 | NIST | |
| Inp | 1741.00 | NIST | |
| Inp | 1768.00 | NIST | |
| Inp | 1755.00 | NIST | |
| Inp | 1751.00 | NIST | |
| Inp | 1783.00 | NIST | |
| Inp | 1786.00 | NIST | |
| Inp | 1747.00 | NIST | |
| Inp | 1770.00 | NIST | |
| Inp | 1764.00 | NIST | |
| Inp | 1748.00 | NIST | |
| Inp | 1748.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1773.00 | NIST | |
| Inp | 1769.00 | NIST | |
| Inp | 1776.00 | NIST | |
| Inp | 1756.00 | NIST | |
| Inp | 1763.00 | NIST | |
| Inp | 1765.00 | NIST | |
| Inp | 1763.00 | NIST | |
| Inp | 1772.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1758.00 | NIST | |
| Inp | 1751.00 | NIST | |
| Inp | 1761.00 | NIST | |
| Inp | 1767.00 | NIST | |
| Inp | 1765.00 | NIST | |
| Inp | 1769.00 | NIST | |
| Inp | 1756.00 | NIST | |
| Inp | 1768.00 | NIST | |
| Inp | 1772.00 | NIST | |
| Inp | 1769.00 | NIST | |
| Inp | 1738.00 | NIST | |
| Inp | 1768.00 | NIST | |
| Inp | 1777.00 | NIST | |
| Inp | 1780.00 | NIST | |
| Inp | 1755.00 | NIST | |
| Inp | 1743.00 | NIST | |
| Inp | 1757.00 | NIST | |
| Inp | 1759.00 | NIST | |
| Inp | 1717.00 | NIST | |
| Inp | 1750.00 | NIST | |
| Inp | 1731.00 | NIST | |
| Inp | 1758.00 | NIST | |
| Inp | 1768.00 | NIST | |
| Inp | 1758.00 | NIST | |
| Inp | 1778.00 | NIST | |
| Inp | 1770.00 | NIST | |
| Inp | 1768.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1800.00 | NIST | |
| Inp | 1761.00 | NIST | |
| Inp | 1777.00 | NIST | |
| Inp | 1768.00 | NIST | |
| Inp | 1750.00 | NIST | |
| Inp | 1780.00 | NIST | |
| Inp | 1774.00 | NIST | |
| Inp | 1748.00 | NIST | |
| Inp | 1767.00 | NIST | |
| Inp | 1745.00 | NIST | |
| Inp | 1758.00 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1749.00 | NIST | |
| Inp | 1750.00 | NIST | |
| Inp | 1786.00 | NIST | |
| Inp | 1754.00 | NIST | |
| Inp | Outlier 293.98 | NIST | |
| Inp | Outlier 303.00 | NIST | |
| Inp | Outlier 291.80 | NIST | |
| Inp | Outlier 288.93 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1769.00 | NIST | |
| Inp | 1763.00 | NIST | |
| Inp | 1761.00 | NIST | |
| Inp | 1768.00 | NIST | |
| Inp | 1777.00 | NIST | |
| Inp | 1759.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1750.00 | NIST | |
| Inp | 1745.00 | NIST | |
| Inp | 1786.00 | NIST | |
| Inp | 1784.00 | NIST | |
| Inp | 1758.20 | NIST | |
| Inp | 1739.00 | NIST | |
| Inp | Outlier 293.98 | NIST | |
| I | [2648.00; 2734.00] |
|
|
| I | 2681.00 | NIST | |
| I | 2715.00 | NIST | |
| I | 2687.00 | NIST | |
| I | 2679.00 | NIST | |
| I | 2694.00 | NIST | |
| I | 2694.00 | NIST | |
| I | 2716.00 | NIST | |
| I | 2712.00 | NIST | |
| I | 2714.00 | NIST | |
| I | 2734.00 | NIST | |
| I | 2680.00 | NIST | |
| I | 2712.00 | NIST | |
| I | 2714.00 | NIST | |
| I | 2656.00 | NIST | |
| I | 2656.00 | NIST | |
| I | 2679.00 | NIST | |
| I | 2724.00 | NIST | |
| I | 2733.00 | NIST | |
| I | 2660.00 | NIST | |
| I | 2698.00 | NIST | |
| I | 2692.00 | NIST | |
| I | 2692.00 | NIST | |
| I | 2692.00 | NIST | |
| I | 2675.00 | NIST | |
| I | 2692.00 | NIST | |
| I | 2674.00 | NIST | |
| I | 2684.00 | NIST | |
| I | 2651.00 | NIST | |
| I | Outlier 2649.00 | NIST | |
| I | 2703.00 | NIST | |
| I | 2685.00 | NIST | |
| I | 2693.00 | NIST | |
| I | 2693.00 | NIST | |
| I | 2708.00 | NIST | |
| I | 2710.00 | NIST | |
| I | 2715.00 | NIST | |
| I | 2715.00 | NIST | |
| I | 2733.00 | NIST | |
| I | 2706.00 | NIST | |
| I | 2704.00 | NIST | |
| I | 2674.00 | NIST | |
| I | Outlier 2648.00 | NIST | |
| I | 2682.00 | NIST | |
| I | 2717.00 | NIST | |
| I | 2713.00 | NIST | |
| I | 2713.00 | NIST | |
| I | 2713.00 | NIST | |
| I | 2713.00 | NIST | |
| I | 2672.00 | NIST | |
| I | 2695.00 | NIST | |
| I | 2713.00 | NIST | |
| I | 2684.00 | NIST | |
| I | 2691.00 | NIST | |
| I | 2670.00 | NIST | |
| I | 2670.00 | NIST | |
| I | 2702.00 | NIST | |
| I | 2692.00 | NIST | |
| I | 2695.00 | NIST | |
| I | 2679.00 | NIST | |
| I | 2713.00 | NIST | |
| I | 2722.00 | NIST | |
| I | 2672.00 | NIST | |
| I | 2701.00 | NIST | |
| I | 2724.00 | NIST | |
| I | 2689.00 | NIST | |
| I | 2713.00 | NIST | |
| I | 2670.00 | NIST | |
| I | 2670.00 | NIST | |
| I | 2670.00 | NIST | |
| I | 2670.00 | NIST | |
| I | 2670.00 | NIST | |
| I | 2670.00 | NIST | |
| I | 2713.00 | NIST | |
| I | 2670.00 | NIST | |
| I | 2713.00 | NIST | |
| I | 2670.00 | NIST | |
| I | 2670.00 | NIST | |
| I | 2660.00 | NIST | |
| I | 2670.00 | NIST | |
| I | 2713.00 | NIST | |
| I | 2713.00 | NIST | |
| I | 2719.00 | NIST | |
| I | 2713.00 | NIST | |
| I | 2670.00 | NIST | |
| I | 2713.00 | NIST | |
| I | 2713.00 | NIST | |
| I | 2713.00 | NIST | |
| I | 2713.00 | NIST | |
| I | 2713.00 | NIST | |
| I | 2713.00 | NIST | |
| I | 2682.00 | NIST | |
| I | 2660.00 | NIST | |
| I | 2670.00 | NIST | |
| I | 2679.00 | NIST | |
| I | 2724.00 | NIST | |
| I | 2713.00 | NIST | |
| I | 2681.00 | NIST | |
| I | 2694.00 | NIST | |
| I | 2680.00 | NIST | |
| I | 2651.00 | NIST | |
| I | 2693.00 | NIST | |
| I | 2733.00 | NIST | |
| I | 2682.00 | NIST | |
| I | 2691.00 | NIST | |
| Tboil | 574.66 | K | Relay (1.0) Calculated Property |
| Tc | 765.19 ± 3.00 | K | NIST |
| Tfus | [326.15; 329.05] | K |
|
| Tfus | 327.50 | K | High pressure solid liquid equilibria of fatty acids |
| Tfus | 327.03 | K | Measurement and PC-SAFT modeling of solid-liquid equilibrium of deep eutectic solvents of quaternary ammonium chlorides and carboxylic acids |
| Tfus | 329.05 | K | Solid-liquid phase equilibrium diagrams of binary mixtures containing fatty acids, fatty alcohol compounds and tripalmitin using differential scanning calorimetry |
| Tfus | 328.88 | K | The solid liquid phase diagrams of binary mixtures of even saturated fatty acids differing by six carbon atoms |
| Tfus | 326.15 | K | Preparation of paraffin and fatty acid phase changing nanoemulsions for heat transfer |
| Tfus | 327.85 | K | Prediction of the properties of eutectic fatty acid phase change materials |
| Tfus | 327.60 | K | Solid Liquid Equilibria in the Binary Systems of Saturated Fatty Acids or Triglycerides (C12 to C18) + Hexadecane |
| Tfus | 327.48 | K | Solid-Liquid Equilibrium of Binary Fatty Acid Mixtures |
| Tfus | 327.50 | K | Study of the Effect of Pressure on Melting Behavior of Saturated Fatty Acids in Liquid or Supercritical Carbon Dioxide |
| Tfus | 327.82 | K | Aq. Solubility Prediction |
| Tfus | 327.05 ± 0.35 | K | NIST |
| Tfus | 327.40 ± 0.05 | K | NIST |
| Tfus | 327.10 ± 1.00 | K | NIST |
| Tfus | 328.70 ± 1.50 | K | NIST |
| Tfus | 327.00 ± 3.00 | K | NIST |
| Tfus | 327.00 ± 3.00 | K | NIST |
| Ttriple | [327.05; 327.32] | K |
|
| Ttriple | 327.32 ± 0.02 | K | NIST |
| Ttriple | 327.05 ± 0.50 | K | NIST |
| Ttriple | 327.32 ± 0.02 | K | NIST |
| Vc | 0.842 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [611.33; 695.50] | J/mol×K | [665.43; 841.89] |
|
| Cp,gas | 611.33 | J/mol×K | 665.43 | Joback Calculated Property |
| Cp,gas | 627.11 | J/mol×K | 694.84 | Joback Calculated Property |
| Cp,gas | 642.16 | J/mol×K | 724.25 | Joback Calculated Property |
| Cp,gas | 656.49 | J/mol×K | 753.66 | Joback Calculated Property |
| Cp,gas | 670.14 | J/mol×K | 783.07 | Joback Calculated Property |
| Cp,gas | 683.14 | J/mol×K | 812.48 | Joback Calculated Property |
| Cp,gas | 695.50 | J/mol×K | 841.89 | Joback Calculated Property |
| Cp,solid | [432.01; 523.00] | J/mol×K | [298.00; 298.15] |
|
| Cp,solid | 523.00 | J/mol×K | 298.00 | NIST |
| Cp,solid | 432.01 | J/mol×K | 298.15 | NIST |
| η | [0.0001430; 0.0013858] | Pa×s | [408.14; 665.43] |
|
| η | 0.0013858 | Pa×s | 408.14 | Joback Calculated Property |
| η | 0.0007927 | Pa×s | 451.02 | Joback Calculated Property |
| η | 0.0004997 | Pa×s | 493.90 | Joback Calculated Property |
| η | 0.0003390 | Pa×s | 536.79 | Joback Calculated Property |
| η | 0.0002436 | Pa×s | 579.67 | Joback Calculated Property |
| η | 0.0001832 | Pa×s | 622.55 | Joback Calculated Property |
| η | 0.0001430 | Pa×s | 665.43 | Joback Calculated Property |
| ΔfusH | [36.28; 45.75] | kJ/mol | [317.00; 327.00] |
|
| ΔfusH | 36.28 | kJ/mol | 317.00 | NIST |
| ΔfusH | 45.75 | kJ/mol | 326.20 | NIST |
| ΔfusH | 45.00 | kJ/mol | 326.50 | NIST |
| ΔfusH | 40.10 | kJ/mol | 326.60 | NIST |
| ΔfusH | 45.10 | kJ/mol | 327.00 | NIST |
| ΔfusH | 45.10 | kJ/mol | 327.00 | NIST |
| ΔsubH | [139.70; 140.00] | kJ/mol | [311.85; 318.50] |
|
| ΔsubH | 140.00 ± 4.00 | kJ/mol | 311.85 | NIST |
| ΔsubH | 139.70 ± 3.80 | kJ/mol | 318.50 | NIST |
| ΔvapH | [88.90; 111.20] | kJ/mol | [298.00; 511.00] |
|
| ΔvapH | 111.20 | kJ/mol | 298.00 | Vapor Pressures and Vaporization, Sublimation, and Fusion Enthalpies of Some Fatty Acids |
| ΔvapH | 104.10 ± 2.00 | kJ/mol | 348.50 | NIST |
| ΔvapH | 100.40 | kJ/mol | 421.00 | NIST |
| ΔvapH | 88.90 | kJ/mol | 455.00 | NIST |
| ΔvapH | 91.60 | kJ/mol | 511.00 | NIST |
| Pvap | [1.33; 9.33] | kPa | [464.60; 512.60] |
|
| Pvap | 1.33 | kPa | 464.60 | Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique |
| Pvap | 2.67 | kPa | 480.80 | Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique |
| Pvap | 4.00 | kPa | 489.50 | Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique |
| Pvap | 5.33 | kPa | 497.20 | Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique |
| Pvap | 6.67 | kPa | 503.10 | Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique |
| Pvap | 8.00 | kPa | 508.20 | Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique |
| Pvap | 9.33 | kPa | 512.60 | Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique |
| ρl | [758.00; 861.30] | kg/m3 | [332.10; 473.20] |
|
| ρl | 861.30 | kg/m3 | 332.10 | Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K |
| ρl | 846.90 | kg/m3 | 352.10 | Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K |
| ρl | 835.60 | kg/m3 | 368.20 | Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K |
| ρl | 821.40 | kg/m3 | 388.20 | Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K |
| ρl | 806.70 | kg/m3 | 408.20 | Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K |
| ρl | 791.70 | kg/m3 | 427.90 | Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K |
| ρl | 780.90 | kg/m3 | 443.20 | Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K |
| ρl | 769.30 | kg/m3 | 458.20 | Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K |
| ρl | 758.00 | kg/m3 | 473.20 | Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K |
| ΔfusS | 114.00 | J/mol×K | 317.00 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 523.20 | K | 13.30 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [461.48; 631.79] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.57451e+01 | |||
| Coefficient B | -5.46750e+03 | |||
| Coefficient C | -1.07769e+02 | |||
| Temperature range, min. | 461.48 | |||
| Temperature range, max. | 631.79 | |||
| Pvap | 1.33 | kPa | 461.48 | Calculated Property |
| Pvap | 2.92 | kPa | 480.40 | Calculated Property |
| Pvap | 5.94 | kPa | 499.33 | Calculated Property |
| Pvap | 11.31 | kPa | 518.25 | Calculated Property |
| Pvap | 20.34 | kPa | 537.17 | Calculated Property |
| Pvap | 34.81 | kPa | 556.10 | Calculated Property |
| Pvap | 57.04 | kPa | 575.02 | Calculated Property |
| Pvap | 89.94 | kPa | 593.94 | Calculated Property |
| Pvap | 137.07 | kPa | 612.87 | Calculated Property |
| Pvap | 202.63 | kPa | 631.79 | Calculated Property |
| Pvap | [4.19e-05; 1535.46] | kPa | [327.55; 756.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 2.20853e+02 | |||
| Coefficient B | -2.15189e+04 | |||
| Coefficient C | -2.86975e+01 | |||
| Coefficient D | 9.02023e-06 | |||
| Temperature range, min. | 327.55 | |||
| Temperature range, max. | 756.00 | |||
| Pvap | 4.19e-05 | kPa | 327.55 | Calculated Property |
| Pvap | 4.81e-03 | kPa | 375.16 | Calculated Property |
| Pvap | 0.14 | kPa | 422.76 | Calculated Property |
| Pvap | 1.66 | kPa | 470.37 | Calculated Property |
| Pvap | 10.72 | kPa | 517.97 | Calculated Property |
| Pvap | 45.19 | kPa | 565.58 | Calculated Property |
| Pvap | 141.42 | kPa | 613.18 | Calculated Property |
| Pvap | 358.30 | kPa | 660.79 | Calculated Property |
| Pvap | 781.64 | kPa | 708.39 | Calculated Property |
| Pvap | 1535.46 | kPa | 756.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Tetradecanoic acid.
Mixtures
- TETRAMETHYLAMMONIUM CHLORIDE + Tetradecanoic acid
- Triolein + Tetradecanoic acid + 1-Hexanol
- Triolein + 1-Butanol + Tetradecanoic acid
- 1-Propanol + Triolein + Tetradecanoic acid
- Triolein + 2-Propanol + Tetradecanoic acid
- Tetradecanoic acid + n-Hexadecanoic acid
- Octadecanoic acid + Tetradecanoic acid
- Tetradecanoic acid + Octadecane
- Dodecanoic acid + Tetradecanoic acid
- Tetradecanoic acid + Octanoic acid
- Tripalmitin + Tetradecanoic acid
- Trichloromethane + Tetradecanoic acid
- Trichloroethylene + Tetradecanoic acid
- Benzene, chloro- + Tetradecanoic acid
- Tetradecanoic acid + Ethane, 1,2-dichloro-
- Tetradecanoic acid + Benzene, (chloromethyl)-
- Tetradecanoic acid + Ethyl Acetate
- Tetradecanoic acid + Acetone
- Tetradecanoic acid + Anisole
- n-Hexane + Tetradecanoic acid
Find more mixtures with Tetradecanoic acid.
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Crippen Method
- High pressure solid liquid equilibria of fatty acids
- Measurement and PC-SAFT modeling of solid-liquid equilibrium of deep eutectic solvents of quaternary ammonium chlorides and carboxylic acids
- Solid-liquid phase equilibrium diagrams of binary mixtures containing fatty acids, fatty alcohol compounds and tripalmitin using differential scanning calorimetry
- Experimental determination of the (vapor + liquid) equilibrium data of binary mixtures of fatty acids by differential scanning calorimetry
- Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
- Solid-liquid phase equilibria of (n-octadecane with myristic, and palmitic acid) binary mixtures used as phase change materials (PCMs)
- Physical properties of systems of interest to the edible oil industry: Viscosities and densities of model systems formed by (triacylglycerol + fatty acid + solvent)
- The solid liquid phase diagrams of binary mixtures of even saturated fatty acids differing by six carbon atoms
- Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique
- Preparation of paraffin and fatty acid phase changing nanoemulsions for heat transfer
- Prediction of the properties of eutectic fatty acid phase change materials
- Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K
- Solid Liquid Equilibria in the Binary Systems of Saturated Fatty Acids or Triglycerides (C12 to C18) + Hexadecane
- Solid-Liquid Equilibrium of Binary Systems Containing Fatty Acids and Fatty Alcohols Using Differential Scanning Calorimetry
- Solid-Liquid Equilibrium of Binary Fatty Acid Mixtures
- Solubilities of Fatty Acids and Triglycerides in 1-Bromopropane
- Vapor Pressures and Vaporization, Sublimation, and Fusion Enthalpies of Some Fatty Acids
- Study of the Effect of Pressure on Melting Behavior of Saturated Fatty Acids in Liquid or Supercritical Carbon Dioxide
- Solubilities of Dodecanoic and Tetradecanoic Acids in Supercritical CO2 with and without Entrainers
- Joback Method
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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