- InChI
- InChI=1S/C12H24O2/c1-2-3-4-5-6-7-8-9-10-11-12(13)14/h2-11H2,1H3,(H,13,14)
- InChI Key
- POULHZVOKOAJMA-UHFFFAOYSA-N
- Formula
- C12H24O2
- SMILES
- CCCCCCCCCCCC(=O)O
- Molecular Weight1
- 200.32
- CAS
- 143-07-7
- Other Names
-
- 1-Undecanecarboxylic acid
- ABL
- Acide Laurique
- Aliphat no. 4
- C-1297
- Dodecanoic (Lauric) acid
- Dodecoic acid
- Dodecylic acid
- Duodecylic acid
- Emery 650
- Emery 651
- Hydrofol acid 1255
- Hydrofol acid 1295
- Hystrene 9512
- Lauric acid
- Lauric acid (dodecanoic acid)
- Laurostearic acid
- Lunac L 70
- N-LAURIC ACID
- Neo-fat 12
- Neo-fat 12-43
- Ninol aa62 extra
- Philacid 1200
- Prifrac 2920
- Undecane-1-carboxylic acid
- Univol U-314
- Vulvic acid
- Wecoline 1295
- dodecanoic acid (lauric acid)
- n-Dodecanoic acid
- 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).
- 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).
- 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).
- Tboil : Boiling point at given pressure (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 |
|---|---|---|---|
| ΔcH°liquid | -7377.00 ± 0.90 | kJ/mol | NIST |
| ΔcH°solid | -7423.70 ± 7.50 | kJ/mol | NIST |
| ΔfG° | -215.58 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -555.82 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 35.60 | kJ/mol | Solid-L... |
| ΔsubH° | [117.20; 147.00] | kJ/mol |
|
| ΔsubH° | 147.00 ± 4.00 | kJ/mol | NIST |
| ΔsubH° | 127.90 | kJ/mol | NIST |
| ΔsubH° | 133.00 ± 2.00 | kJ/mol | NIST |
| ΔsubH° | 117.20 ± 2.90 | kJ/mol | NIST |
| ΔvapH° | 65.73 | kJ/mol | Joback Calculated Property |
| log10WS | -4.62 | Aq. Sol... | |
| logPoct/wat | 3.992 | Crippen Calculated Property | |
| McVol | 187.380 | ml/mol | McGowan Calculated Property |
| Pc | 1867.79 ± 85.00 | kPa | NIST |
| Inp | [263.20; 1604.00] |
|
|
| Inp | 1576.00 | NIST | |
| Inp | 1567.00 | NIST | |
| Inp | 1568.00 | NIST | |
| Inp | 1602.00 | NIST | |
| Inp | 1547.00 | NIST | |
| Inp | 1554.00 | NIST | |
| Inp | 1562.00 | NIST | |
| Inp | 1570.00 | NIST | |
| Inp | 1556.00 | NIST | |
| Inp | 1566.60 | NIST | |
| Inp | 1576.00 | NIST | |
| Inp | 1568.00 | NIST | |
| Inp | 1571.00 | NIST | |
| Inp | 1577.00 | NIST | |
| Inp | 1554.00 | NIST | |
| Inp | 1580.00 | NIST | |
| Inp | 1575.00 | NIST | |
| Inp | 1578.00 | NIST | |
| Inp | 1568.00 | NIST | |
| Inp | 1568.00 | NIST | |
| Inp | 1568.00 | NIST | |
| Inp | 1559.00 | NIST | |
| Inp | 1550.00 | NIST | |
| Inp | 1578.00 | NIST | |
| Inp | 1566.00 | NIST | |
| Inp | 1573.00 | NIST | |
| Inp | 1563.00 | NIST | |
| Inp | 1568.00 | NIST | |
| Inp | 1558.00 | NIST | |
| Inp | 1567.00 | NIST | |
| Inp | 1562.00 | NIST | |
| Inp | 1561.00 | NIST | |
| Inp | 1561.00 | NIST | |
| Inp | 1566.00 | NIST | |
| Inp | 1568.00 | NIST | |
| Inp | 1543.00 | NIST | |
| Inp | 1559.00 | NIST | |
| Inp | 1548.00 | NIST | |
| Inp | 1577.00 | NIST | |
| Inp | 1567.00 | NIST | |
| Inp | 1545.00 | NIST | |
| Inp | 1556.00 | NIST | |
| Inp | 1545.00 | NIST | |
| Inp | 1545.00 | NIST | |
| Inp | 1529.00 | NIST | |
| Inp | 1565.00 | NIST | |
| Inp | 1566.00 | NIST | |
| Inp | 1556.00 | NIST | |
| Inp | 1564.00 | NIST | |
| Inp | 1554.00 | NIST | |
| Inp | 1565.00 | NIST | |
| Inp | 1557.00 | NIST | |
| Inp | 1561.00 | NIST | |
| Inp | 1570.00 | NIST | |
| Inp | 1567.00 | NIST | |
| Inp | 1547.00 | NIST | |
| Inp | 1565.00 | NIST | |
| Inp | 1541.00 | NIST | |
| Inp | 1565.00 | NIST | |
| Inp | 1573.00 | NIST | |
| Inp | 1569.00 | NIST | |
| Inp | 1564.00 | NIST | |
| Inp | 1562.00 | NIST | |
| Inp | 1568.00 | NIST | |
| Inp | 1568.00 | NIST | |
| Inp | 1574.00 | NIST | |
| Inp | 1566.00 | NIST | |
| Inp | 1573.00 | NIST | |
| Inp | 1604.00 | NIST | |
| Inp | 1549.00 | NIST | |
| Inp | 1568.00 | NIST | |
| Inp | 1568.00 | NIST | |
| Inp | 1569.00 | NIST | |
| Inp | 1566.00 | NIST | |
| Inp | 1571.30 | NIST | |
| Inp | 1558.00 | NIST | |
| Inp | 1581.00 | NIST | |
| Inp | 1566.00 | NIST | |
| Inp | 1568.00 | NIST | |
| Inp | 1568.00 | NIST | |
| Inp | 1568.00 | NIST | |
| Inp | 1569.00 | NIST | |
| Inp | 1572.00 | NIST | |
| Inp | 1568.00 | NIST | |
| Inp | 1565.00 | NIST | |
| Inp | 1592.00 | NIST | |
| Inp | 1592.00 | NIST | |
| Inp | 1567.00 | NIST | |
| Inp | 1580.00 | NIST | |
| Inp | 1570.00 | NIST | |
| Inp | 1566.00 | NIST | |
| Inp | 1569.00 | NIST | |
| Inp | 1550.00 | NIST | |
| Inp | 1553.00 | NIST | |
| Inp | 1591.00 | NIST | |
| Inp | 1546.00 | NIST | |
| Inp | 1546.00 | NIST | |
| Inp | 1566.00 | NIST | |
| Inp | 1552.00 | NIST | |
| Inp | 1561.00 | NIST | |
| Inp | 1562.00 | NIST | |
| Inp | 1587.00 | NIST | |
| Inp | 1563.00 | NIST | |
| Inp | 1565.00 | NIST | |
| Inp | 1564.00 | NIST | |
| Inp | 1569.00 | NIST | |
| Inp | 1566.00 | NIST | |
| Inp | 1566.00 | NIST | |
| Inp | 1556.00 | NIST | |
| Inp | 1564.00 | NIST | |
| Inp | 1566.00 | NIST | |
| Inp | 1570.00 | NIST | |
| Inp | 1560.00 | NIST | |
| Inp | 1568.00 | NIST | |
| Inp | 1582.00 | NIST | |
| Inp | 1580.00 | NIST | |
| Inp | 1567.00 | NIST | |
| Inp | 1553.00 | NIST | |
| Inp | 1551.00 | NIST | |
| Inp | 1557.00 | NIST | |
| Inp | 1556.00 | NIST | |
| Inp | 1559.00 | NIST | |
| Inp | 1556.00 | NIST | |
| Inp | 1567.00 | NIST | |
| Inp | 1574.00 | NIST | |
| Inp | 1567.00 | NIST | |
| Inp | 1589.00 | NIST | |
| Inp | 1572.00 | NIST | |
| Inp | 1568.00 | NIST | |
| Inp | 1600.00 | NIST | |
| Inp | 1559.00 | NIST | |
| Inp | 1567.00 | NIST | |
| Inp | 1573.00 | NIST | |
| Inp | 1580.00 | NIST | |
| Inp | 1572.00 | NIST | |
| Inp | 1558.00 | NIST | |
| Inp | 1543.00 | NIST | |
| Inp | 1587.00 | NIST | |
| Inp | 1587.00 | NIST | |
| Inp | 1600.00 | NIST | |
| Inp | Outlier 264.58 | NIST | |
| Inp | Outlier 272.70 | NIST | |
| Inp | Outlier 263.20 | NIST | |
| Inp | 1567.00 | NIST | |
| Inp | 1587.00 | NIST | |
| Inp | 1566.00 | NIST | |
| Inp | 1570.00 | NIST | |
| Inp | 1559.00 | NIST | |
| Inp | 1589.00 | NIST | |
| Inp | 1543.00 | NIST | |
| Inp | 1529.00 | NIST | |
| Inp | 1554.00 | NIST | |
| Inp | 1573.00 | NIST | |
| Inp | 1568.00 | NIST | |
| Inp | 1549.00 | NIST | |
| Inp | 1571.30 | NIST | |
| Inp | 1565.00 | NIST | |
| Inp | 1591.00 | NIST | |
| Inp | 1561.00 | NIST | |
| Inp | 1571.00 | NIST | |
| Inp | 1578.00 | NIST | |
| Inp | 1550.00 | NIST | |
| Inp | 1548.00 | NIST | |
| Inp | 1562.00 | NIST | |
| I | [2446.00; 2538.00] |
|
|
| I | 2502.00 | NIST | |
| I | 2508.00 | NIST | |
| I | 2474.00 | NIST | |
| I | 2523.00 | NIST | |
| I | 2475.00 | NIST | |
| I | 2486.00 | NIST | |
| I | 2485.00 | NIST | |
| I | 2505.00 | NIST | |
| I | 2482.00 | NIST | |
| I | 2471.00 | NIST | |
| I | 2471.00 | NIST | |
| I | 2448.00 | NIST | |
| I | 2448.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2515.00 | NIST | |
| I | 2516.00 | NIST | |
| I | 2529.00 | NIST | |
| I | 2515.00 | NIST | |
| I | 2516.00 | NIST | |
| I | 2447.00 | NIST | |
| I | 2479.00 | NIST | |
| I | 2517.00 | NIST | |
| I | 2451.00 | NIST | |
| I | 2449.00 | NIST | |
| I | 2469.00 | NIST | |
| I | 2449.00 | NIST | |
| I | 2486.00 | NIST | |
| I | 2499.00 | NIST | |
| I | 2531.00 | NIST | |
| I | 2487.00 | NIST | |
| I | 2451.00 | NIST | |
| I | 2474.00 | NIST | |
| I | 2504.00 | NIST | |
| I | 2482.00 | NIST | |
| I | 2504.00 | NIST | |
| I | 2499.00 | NIST | |
| I | 2467.00 | NIST | |
| I | 2493.00 | NIST | |
| I | 2507.00 | NIST | |
| I | 2482.00 | NIST | |
| I | 2502.00 | NIST | |
| I | 2465.00 | NIST | |
| I | 2495.00 | NIST | |
| I | 2487.00 | NIST | |
| I | 2487.00 | NIST | |
| I | 2496.00 | NIST | |
| I | 2498.00 | NIST | |
| I | 2494.00 | NIST | |
| I | 2517.00 | NIST | |
| I | 2502.00 | NIST | |
| I | 2490.00 | NIST | |
| I | 2466.00 | NIST | |
| I | 2466.00 | NIST | |
| I | 2479.00 | NIST | |
| I | Outlier 2538.00 | NIST | |
| I | 2490.00 | NIST | |
| I | 2470.00 | NIST | |
| I | 2489.00 | NIST | |
| I | 2472.00 | NIST | |
| I | 2465.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2478.00 | NIST | |
| I | 2482.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2488.00 | NIST | |
| I | 2477.00 | NIST | |
| I | 2456.00 | NIST | |
| I | 2466.00 | NIST | |
| I | 2524.00 | NIST | |
| I | 2465.00 | NIST | |
| I | 2500.00 | NIST | |
| I | 2479.00 | NIST | |
| I | Outlier 2446.00 | NIST | |
| I | 2500.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2490.00 | NIST | |
| I | 2488.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2467.00 | NIST | |
| I | 2457.00 | NIST | |
| I | 2458.00 | NIST | |
| I | 2517.00 | NIST | |
| I | 2517.00 | NIST | |
| I | 2517.00 | NIST | |
| I | 2514.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2467.00 | NIST | |
| I | 2525.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2499.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2499.00 | NIST | |
| I | 2473.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2472.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2471.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2463.00 | NIST | |
| I | 2451.00 | NIST | |
| I | 2449.00 | NIST | |
| I | 2531.00 | NIST | |
| I | 2451.00 | NIST | |
| I | 2499.00 | NIST | |
| I | 2502.00 | NIST | |
| I | 2496.00 | NIST | |
| I | 2490.00 | NIST | |
| I | 2503.00 | NIST | |
| I | 2466.00 | NIST | |
| I | Outlier 2446.00 | NIST | |
| I | 2474.00 | NIST | |
| I | 2505.00 | NIST | |
| I | 2448.00 | NIST | |
| I | 2515.00 | NIST | |
| Tboil | 571.00 ± 3.00 | K | NIST |
| Tc | 743.43 ± 3.00 | K | NIST |
| Tfus | [315.85; 318.50] | K |
|
| Tfus | 317.00 | K | Aq. Sol... |
| Tfus | 316.18 | K | High pr... |
| Tfus | 317.48 | K | Measure... |
| Tfus | 318.50 | K | Solid-l... |
| Tfus | 318.07 | K | The sol... |
| Tfus | 315.95 | K | Thermal... |
| Tfus | 315.85 | K | Improvi... |
| Tfus | 316.75 | K | Predict... |
| Tfus | 317.40 | K | Solid L... |
| Tfus | 316.94 | K | Solid-L... |
| Tfus | 317.70 | K | Study o... |
| Ttriple | [316.98; 320.35] | K |
|
| Ttriple | 320.35 | K | Fabrica... |
| Ttriple | 317.71 | K | Solubil... |
| Ttriple | 316.98 ± 0.02 | K | NIST |
| Vc | 0.733 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [502.78; 576.84] | J/mol×K | [620.01; 786.00] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 500 520 540 560 580 650 700 750 | ||||
| Cp,gas | 502.78 | J/mol×K | 620.01 | Joback Calculated Property |
| Cp,gas | 516.54 | J/mol×K | 647.67 | Joback Calculated Property |
| Cp,gas | 529.70 | J/mol×K | 675.34 | Joback Calculated Property |
| Cp,gas | 542.30 | J/mol×K | 703.00 | Joback Calculated Property |
| Cp,gas | 554.35 | J/mol×K | 730.67 | Joback Calculated Property |
| Cp,gas | 565.85 | J/mol×K | 758.33 | Joback Calculated Property |
| Cp,gas | 576.84 | J/mol×K | 786.00 | Joback Calculated Property |
| Cp,solid | [381.00; 428.90] | J/mol×K | [279.00; 301.00] |
|
| Cp,solid | 381.00 | J/mol×K | 279.00 | NIST |
| Cp,solid | 404.28 | J/mol×K | 298.15 | NIST |
| Cp,solid | 428.90 | J/mol×K | 301.00 | NIST |
| η | [0.0000730; 0.0076488] | Pa×s | [335.75; 620.01] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 6.00e-3 7.00e-3 8.00e-3 400 500 600 | ||||
| η | 0.0076488 | Pa×s | 335.75 | Joback Calculated Property |
| η | 0.0021816 | Pa×s | 383.13 | Joback Calculated Property |
| η | 0.0008201 | Pa×s | 430.50 | Joback Calculated Property |
| η | 0.0003743 | Pa×s | 477.88 | Joback Calculated Property |
| η | 0.0001968 | Pa×s | 525.26 | Joback Calculated Property |
| η | 0.0001151 | Pa×s | 572.63 | Joback Calculated Property |
| η | 0.0000730 | Pa×s | 620.01 | Joback Calculated Property |
| ΔfusH | [34.70; 44.94] | kJ/mol | [316.60; 327.00] |
|
|
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 34 36 38 40 42 44 320 325 | ||||
| ΔfusH | 36.10 | kJ/mol | 316.60 | NIST |
| ΔfusH | 36.65 | kJ/mol | 316.90 | NIST |
| ΔfusH | 36.65 | kJ/mol | 316.90 | NIST |
| ΔfusH | 36.65 | kJ/mol | 316.90 | NIST |
| ΔfusH | 34.70 | kJ/mol | 317.90 | NIST |
| ΔfusH | 44.94 | kJ/mol | 327.00 | NIST |
| ΔsubH | [117.20; 140.20] | kJ/mol | [295.70; 305.00] |
|
| ΔsubH | 140.00 ± 3.00 | kJ/mol | 295.70 | NIST |
| ΔsubH | 132.60 | kJ/mol | 300.50 | NIST |
| ΔsubH | 117.20 ± 2.90 | kJ/mol | 303.00 | NIST |
| ΔsubH | 140.20 ± 3.30 | kJ/mol | 305.00 | NIST |
| ΔvapH | [81.30; 95.80] | kJ/mol | [331.00; 483.00] |
|
| ΔvapH | 95.80 | kJ/mol | 331.00 | NIST |
| ΔvapH | 81.30 | kJ/mol | 437.00 | NIST |
| ΔvapH | 88.80 | kJ/mol | 483.00 | NIST |
| Pvap | [1.33; 9.33] | kPa | [444.60; 490.50] |
|
|
T(K) Vapor pressure (kPa) 2 4 6 8 10 460 480 | ||||
| Pvap | 1.33 | kPa | 444.60 | Vapor p... |
| Pvap | 2.67 | kPa | 458.90 | Vapor p... |
| Pvap | 4.00 | kPa | 468.50 | Vapor p... |
| Pvap | 5.33 | kPa | 475.00 | Vapor p... |
| Pvap | 6.67 | kPa | 479.60 | Vapor p... |
| Pvap | 8.00 | kPa | 484.80 | Vapor p... |
| Pvap | 9.33 | kPa | 490.50 | Vapor p... |
| ρl | [762.00; 872.40] | kg/m3 | [322.10; 467.20] |
|
|
T(K) Liquid Density (kg/m3) 760 780 800 820 840 860 880 350 400 450 | ||||
| ρl | 872.40 | kg/m3 | 322.10 | Density... |
| ρl | 864.60 | kg/m3 | 332.10 | Density... |
| ρl | 849.90 | kg/m3 | 352.10 | Density... |
| ρl | 838.90 | kg/m3 | 368.20 | Density... |
| ρl | 824.10 | kg/m3 | 388.40 | Density... |
| ρl | 809.30 | kg/m3 | 408.10 | Density... |
| ρl | 794.40 | kg/m3 | 428.10 | Density... |
| ρl | 783.50 | kg/m3 | 442.20 | Density... |
| ρl | 770.20 | kg/m3 | 457.20 | Density... |
| ρl | 762.00 | kg/m3 | 467.20 | Density... |
| ΔfusS | [115.70; 137.00] | J/mol×K | [316.90; 327.00] |
|
| ΔfusS | 115.70 | J/mol×K | 316.90 | NIST |
| ΔfusS | 137.00 | J/mol×K | 327.00 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | 465.77 | K | 3.42 | Vapor-l... |
| Tboilr | 498.20 | K | 13.30 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [439.64; 602.09] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.58098e+01 | |||
| Coefficient B | -5.26917e+03 | |||
| Coefficient C | -1.00180e+02 | |||
| Temperature range, min. | 439.64 | |||
| Temperature range, max. | 602.09 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 600 | ||||
| Pvap | 1.33 | kPa | 439.64 | Calculated Property |
| Pvap | 2.92 | kPa | 457.69 | Calculated Property |
| Pvap | 5.93 | kPa | 475.74 | Calculated Property |
| Pvap | 11.28 | kPa | 493.79 | Calculated Property |
| Pvap | 20.29 | kPa | 511.84 | Calculated Property |
| Pvap | 34.73 | kPa | 529.89 | Calculated Property |
| Pvap | 56.94 | kPa | 547.94 | Calculated Property |
| Pvap | 89.83 | kPa | 565.99 | Calculated Property |
| Pvap | 137.00 | kPa | 584.04 | Calculated Property |
| Pvap | 202.67 | kPa | 602.09 | Calculated Property |
| Pvap | [4.13e-05; 1831.09] | kPa | [317.15; 734.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 2.90782e+02 | |||
| Coefficient B | -2.44556e+04 | |||
| Coefficient C | -3.91170e+01 | |||
| Coefficient D | 1.51519e-05 | |||
| Temperature range, min. | 317.15 | |||
| Temperature range, max. | 734.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 400 500 600 700 | ||||
| Pvap | 4.13e-05 | kPa | 317.15 | Calculated Property |
| Pvap | 5.96e-03 | kPa | 363.47 | Calculated Property |
| Pvap | 0.19 | kPa | 409.78 | Calculated Property |
| Pvap | 2.25 | kPa | 456.10 | Calculated Property |
| Pvap | 14.08 | kPa | 502.42 | Calculated Property |
| Pvap | 56.92 | kPa | 548.73 | Calculated Property |
| Pvap | 171.34 | kPa | 595.05 | Calculated Property |
| Pvap | 422.94 | kPa | 641.37 | Calculated Property |
| Pvap | 916.51 | kPa | 687.68 | Calculated Property |
| Pvap | 1831.09 | kPa | 734.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Dodecanoic acid.
Mixtures
- Dodecanoic acid + Tetradecanoic acid
- Dodecanoic acid + Tetramethylammonium chloride
- Dodecanoic acid + Tripalmitin
- Dodecanoic acid + Octadecanoic acid
- Dodecanoic acid + Hexadecane
- 1-Dodecanol + Dodecanoic acid
- Carbon dioxide + Dodecanoic acid
- Isopropyl Alcohol + Dodecanoic acid
- 1-Propanol + Dodecanoic acid
- Dodecanoic acid + Ethanol
- Dodecanoic acid + n-Decanoic acid
- Dodecanoic acid + n-Hexadecanoic acid
- Lidocaine + Dodecanoic acid
- Carbon dioxide + Dodecanoic acid + Methyl Alcohol
- n-Hexane + Dodecanoic acid
- Dodecanoic acid + Heptane
- Dodecanoic acid + Pentane, 2,2,4-trimethyl-
- 1-Hexene + Dodecanoic acid
- Toluene + Dodecanoic acid
- Dodecanoic acid + Cyclohexane
Find more mixtures with Dodecanoic acid.
Sources
- KDB Vapor Pressure Data
- 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
- Vapor-liquid equilibria of monoacylglicerol + monoacylglicerol or alcohol or fatty acid at subatmospheric pressures
- Thermodynamic properties of hydrophobic deep eutectic solvents and solubility of water and HMF in them: Measurements and PC-SAFT modeling
- Solid-liquid phase equilibrium diagrams of binary mixtures containing fatty acids, fatty alcohol compounds and tripalmitin using differential scanning calorimetry
- Phase behavior of (CO2 + methanol + lauric acid) system
- Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
- 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
- Thermal conductivity enhancement of lauric acid phase change nanocomposite in solid and liquid state with single-walled carbon nanohorn inclusions
- Improving thermal properties of shape-stabilized phase change materials containing lauric acid and mesocellular foam silica by assessing thermodynamic properties of the non-melting layer
- Prediction of the properties of eutectic fatty acid phase change materials
- Fabrication of shape-stable composite phase change materials based on lauric acid and graphene/graphene oxide complex aerogels for enhancement of thermal energy storage and electrical conduction
- 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
- Twenty Years of Experimental Determinations of Thermophysical Properties with High Accuracy: Thermodynamics Laboratory, ESIQIE-IPN, Mexico
- Solubility Measurement of Lauric, Palmitic, and Stearic Acids in Ethanol, n-Propanol, and 2-Propanol Using Differential Scanning Calorimetry
- Apparent Molar Volumes and Viscosities of Lauric, Palmitic, and Stearic Acids in 2-Butanol at (20, 30, 40, and 60) C
- Solid-Liquid Equilibrium of Binary Fatty Acid Mixtures
- Phase Equilibria of Long-Chain Carboxylic Acids in Supercritical Propane
- Study of the Effect of Pressure on Melting Behavior of Saturated Fatty Acids in Liquid or Supercritical Carbon Dioxide
- Determination and Correlation of Solubilities of Lauric Acid in Eight Alcohols
- Solubilities of Dodecanoic and Tetradecanoic Acids in Supercritical CO2 with and without Entrainers
- Solubilities of Lauric Acid in n-Hexane, Acetone, Propanol, 2-Propanol, 1-Bromopropane, and Trichloroethylene from (279.0 to 315.3) K
- Joback Method
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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