- 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.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
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] |
|
| 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] |
|
| 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] |
|
| 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] |
|
| 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] |
|
| 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 | |||
| 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 | |||
| 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
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.