- InChI
- InChI=1S/C10H20O2/c1-2-3-4-5-6-7-8-9-10(11)12/h2-9H2,1H3,(H,11,12)
- InChI Key
- GHVNFZFCNZKVNT-UHFFFAOYSA-N
- Formula
- C10H20O2
- SMILES
- CCCCCCCCCC(=O)O
- Molecular Weight1
- 172.26
- CAS
- 334-48-5
- Other Names
-
- 1-Decanoic acid
- 1-Nonanecarboxylic acid
- Capric acid
- Caprinic acid
- Caprynic acid
- Decanoic acid
- Decanoic acid (capric acid)
- Decoic acid
- Decylic acid
- Emery 659
- Hexacid 1095
- NSC 5025
- Nonane-1-carboxylic acid
- Prifrac 296
- n-Capric acid
- n-Decoic acid
- n-Decylic acid
- neo-Fat 10
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid 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 | 0.8292 | Relay (1.0) Calculated Property | |
| ΔcH°liquid | -6079.30 ± 0.90 | kJ/mol | NIST |
| ΔfG° | -232.42 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -624.20 ± 5.10 | kJ/mol | NIST |
| ΔfusH° | 28.00 | kJ/mol | Solid-Liquid Equilibrium of Binary Systems Containing Fatty Acids and Fatty Alcohols Using Differential Scanning Calorimetry |
| ΔsubH° | [118.80; 130.00] | kJ/mol |
|
| ΔsubH° | 130.00 ± 5.00 | kJ/mol | NIST |
| ΔsubH° | 119.00 ± 2.00 | kJ/mol | NIST |
| ΔsubH° | 118.80 ± 2.20 | kJ/mol | NIST |
| ΔvapH° | 88.50 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.97 | eV | Relay (1.0) Calculated Property |
| log10WS | -3.44 | Aq. Solubility Prediction | |
| logPoct/wat | 3.212 | Crippen Calculated Property | |
| McVol | 159.200 | ml/mol | McGowan Calculated Property |
| Pc | [2100.00; 2230.00] | kPa |
|
| Pc | 2230.00 | kPa | KDB |
| Pc | 2100.00 ± 400.00 | kPa | NIST |
| Pc | 2161.74 ± 90.00 | kPa | NIST |
| Ptriple | 9.73e-05 ± 2.67e-05 | kPa | NIST |
| Inp | [231.60; 1404.00] |
|
|
| Inp | 1384.00 | NIST | |
| Inp | 1355.00 | NIST | |
| Inp | 1335.00 | NIST | |
| Inp | 1365.00 | NIST | |
| Inp | 1387.00 | NIST | |
| Inp | 1380.00 | NIST | |
| Inp | 1373.00 | NIST | |
| Inp | 1402.00 | NIST | |
| Inp | 1380.00 | NIST | |
| Inp | 1373.00 | NIST | |
| Inp | 1368.20 | NIST | |
| Inp | 1344.00 | NIST | |
| Inp | 1377.00 | NIST | |
| Inp | 1371.00 | NIST | |
| Inp | 1382.00 | NIST | |
| Inp | 1380.00 | NIST | |
| Inp | 1400.00 | NIST | |
| Inp | 1381.00 | NIST | |
| Inp | 1372.00 | NIST | |
| Inp | 1350.00 | NIST | |
| Inp | 1387.00 | NIST | |
| Inp | 1353.00 | NIST | |
| Inp | 1380.00 | NIST | |
| Inp | 1359.00 | NIST | |
| Inp | 1378.00 | NIST | |
| Inp | 1370.00 | NIST | |
| Inp | 1360.00 | NIST | |
| Inp | 1404.00 | NIST | |
| Inp | 1374.00 | NIST | |
| Inp | 1360.00 | NIST | |
| Inp | 1360.00 | NIST | |
| Inp | 1369.00 | NIST | |
| Inp | 1376.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1386.00 | NIST | |
| Inp | 1354.00 | NIST | |
| Inp | 1374.00 | NIST | |
| Inp | 1374.00 | NIST | |
| Inp | 1373.00 | NIST | |
| Inp | 1336.00 | NIST | |
| Inp | 1367.00 | NIST | |
| Inp | 1368.00 | NIST | |
| Inp | 1373.00 | NIST | |
| Inp | 1347.00 | NIST | |
| Inp | 1356.00 | NIST | |
| Inp | 1370.00 | NIST | |
| Inp | 1370.00 | NIST | |
| Inp | 1373.00 | NIST | |
| Inp | 1370.00 | NIST | |
| Inp | 1362.00 | NIST | |
| Inp | 1374.00 | NIST | |
| Inp | 1380.00 | NIST | |
| Inp | 1354.00 | NIST | |
| Inp | 1369.00 | NIST | |
| Inp | 1383.00 | NIST | |
| Inp | 1358.00 | NIST | |
| Inp | 1380.00 | NIST | |
| Inp | 1352.00 | NIST | |
| Inp | 1373.00 | NIST | |
| Inp | 1362.00 | NIST | |
| Inp | 1372.00 | NIST | |
| Inp | 1385.00 | NIST | |
| Inp | 1357.00 | NIST | |
| Inp | 1357.00 | NIST | |
| Inp | 1396.00 | NIST | |
| Inp | 1385.00 | NIST | |
| Inp | 1380.00 | NIST | |
| Inp | 1356.00 | NIST | |
| Inp | 1376.00 | NIST | |
| Inp | 1376.00 | NIST | |
| Inp | 1373.00 | NIST | |
| Inp | 1379.00 | NIST | |
| Inp | 1362.00 | NIST | |
| Inp | 1368.00 | NIST | |
| Inp | 1363.00 | NIST | |
| Inp | 1372.00 | NIST | |
| Inp | 1363.00 | NIST | |
| Inp | 1371.00 | NIST | |
| Inp | 1371.00 | NIST | |
| Inp | 1379.00 | NIST | |
| Inp | 1350.00 | NIST | |
| Inp | 1393.00 | NIST | |
| Inp | 1357.00 | NIST | |
| Inp | 1376.00 | NIST | |
| Inp | 1373.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1353.00 | NIST | |
| Inp | 1358.00 | NIST | |
| Inp | 1364.00 | NIST | |
| Inp | 1366.00 | NIST | |
| Inp | 1360.00 | NIST | |
| Inp | 1367.00 | NIST | |
| Inp | 1360.00 | NIST | |
| Inp | 1348.00 | NIST | |
| Inp | 1371.00 | NIST | |
| Inp | 1397.00 | NIST | |
| Inp | 1380.00 | NIST | |
| Inp | 1363.00 | NIST | |
| Inp | 1366.00 | NIST | |
| Inp | 1378.00 | NIST | |
| Inp | 1376.00 | NIST | |
| Inp | 1349.00 | NIST | |
| Inp | 1384.00 | NIST | |
| Inp | 1367.00 | NIST | |
| Inp | 1368.00 | NIST | |
| Inp | 1369.00 | NIST | |
| Inp | 1369.00 | NIST | |
| Inp | 1370.00 | NIST | |
| Inp | 1372.00 | NIST | |
| Inp | 1373.00 | NIST | |
| Inp | 1373.00 | NIST | |
| Inp | 1373.00 | NIST | |
| Inp | 1373.00 | NIST | |
| Inp | 1373.00 | NIST | |
| Inp | 1373.00 | NIST | |
| Inp | 1373.00 | NIST | |
| Inp | 1363.00 | NIST | |
| Inp | 1394.00 | NIST | |
| Inp | 1367.00 | NIST | |
| Inp | 1357.00 | NIST | |
| Inp | 1364.00 | NIST | |
| Inp | 1364.00 | NIST | |
| Inp | 1400.00 | NIST | |
| Inp | 1366.00 | NIST | |
| Inp | 1366.00 | NIST | |
| Inp | 1386.00 | NIST | |
| Inp | 1390.00 | NIST | |
| Inp | 1386.00 | NIST | |
| Inp | 1348.00 | NIST | |
| Inp | 1349.00 | NIST | |
| Inp | 1364.00 | NIST | |
| Inp | 1400.00 | NIST | |
| Inp | 1399.00 | NIST | |
| Inp | Outlier 234.82 | NIST | |
| Inp | Outlier 231.60 | NIST | |
| Inp | 1373.00 | NIST | |
| Inp | 1347.00 | NIST | |
| Inp | 1370.00 | NIST | |
| Inp | 1369.00 | NIST | |
| Inp | 1357.00 | NIST | |
| Inp | 1376.00 | NIST | |
| Inp | 1368.00 | NIST | |
| Inp | 1371.00 | NIST | |
| Inp | 1364.00 | NIST | |
| Inp | 1348.00 | NIST | |
| Inp | 1366.00 | NIST | |
| Inp | 1367.00 | NIST | |
| Inp | 1372.00 | NIST | |
| Inp | Outlier 234.82 | NIST | |
| I | [2227.00; 2320.00] |
|
|
| I | 2279.00 | NIST | |
| I | 2288.00 | NIST | |
| I | 2281.00 | NIST | |
| I | 2281.00 | NIST | |
| I | 2265.00 | NIST | |
| I | 2270.00 | NIST | |
| I | 2314.00 | NIST | |
| I | 2270.00 | NIST | |
| I | 2246.00 | NIST | |
| I | 2275.00 | NIST | |
| I | 2303.00 | NIST | |
| I | 2276.00 | NIST | |
| I | 2316.00 | NIST | |
| I | Outlier 2227.00 | NIST | |
| I | 2250.00 | NIST | |
| I | 2270.00 | NIST | |
| I | 2294.00 | NIST | |
| I | Outlier 2231.00 | NIST | |
| I | 2271.00 | NIST | |
| I | 2250.00 | NIST | |
| I | 2250.00 | NIST | |
| I | 2261.00 | NIST | |
| I | 2242.00 | NIST | |
| I | 2262.00 | NIST | |
| I | 2298.00 | NIST | |
| I | 2252.00 | NIST | |
| I | 2242.00 | NIST | |
| I | 2288.00 | NIST | |
| I | Outlier 2227.00 | NIST | |
| I | 2280.00 | NIST | |
| I | 2284.00 | NIST | |
| I | Outlier 2318.00 | NIST | |
| I | 2235.00 | NIST | |
| I | 2268.00 | NIST | |
| I | 2280.00 | NIST | |
| I | 2284.00 | NIST | |
| I | 2284.00 | NIST | |
| I | 2246.00 | NIST | |
| I | 2271.00 | NIST | |
| I | 2275.00 | NIST | |
| I | 2300.00 | NIST | |
| I | 2269.00 | NIST | |
| I | 2238.00 | NIST | |
| I | 2258.00 | NIST | |
| I | 2258.00 | NIST | |
| I | 2244.00 | NIST | |
| I | 2263.00 | NIST | |
| I | 2264.00 | NIST | |
| I | 2276.00 | NIST | |
| I | 2261.00 | NIST | |
| I | 2264.00 | NIST | |
| I | 2253.00 | NIST | |
| I | 2276.00 | NIST | |
| I | 2288.00 | NIST | |
| I | 2251.00 | NIST | |
| I | 2269.00 | NIST | |
| I | 2290.00 | NIST | |
| I | 2258.00 | NIST | |
| I | 2276.00 | NIST | |
| I | 2274.00 | NIST | |
| I | 2251.00 | NIST | |
| I | 2282.00 | NIST | |
| I | 2282.00 | NIST | |
| I | 2282.00 | NIST | |
| I | 2272.00 | NIST | |
| I | 2289.00 | NIST | |
| I | 2280.00 | NIST | |
| I | 2287.00 | NIST | |
| I | 2256.00 | NIST | |
| I | 2268.00 | NIST | |
| I | 2308.00 | NIST | |
| I | 2275.00 | NIST | |
| I | 2282.00 | NIST | |
| I | 2282.00 | NIST | |
| I | 2307.00 | NIST | |
| I | 2286.00 | NIST | |
| I | 2272.00 | NIST | |
| I | 2278.00 | NIST | |
| I | Outlier 2320.00 | NIST | |
| I | 2258.00 | NIST | |
| I | 2270.00 | NIST | |
| I | 2278.00 | NIST | |
| I | 2279.00 | NIST | |
| I | 2270.00 | NIST | |
| I | 2295.00 | NIST | |
| I | 2256.00 | NIST | |
| I | 2296.00 | NIST | |
| I | 2260.00 | NIST | |
| I | 2270.00 | NIST | |
| I | 2270.00 | NIST | |
| I | 2266.00 | NIST | |
| I | 2270.00 | NIST | |
| I | 2244.00 | NIST | |
| I | 2285.00 | NIST | |
| I | 2280.00 | NIST | |
| I | 2276.00 | NIST | |
| I | 2275.00 | NIST | |
| I | 2244.00 | NIST | |
| I | 2300.00 | NIST | |
| I | 2300.00 | NIST | |
| I | 2300.00 | NIST | |
| I | 2300.00 | NIST | |
| I | Outlier 2229.00 | NIST | |
| I | 2278.00 | NIST | |
| I | 2296.00 | NIST | |
| I | 2276.00 | NIST | |
| I | 2273.00 | NIST | |
| I | 2283.00 | NIST | |
| I | 2287.00 | NIST | |
| I | 2237.00 | NIST | |
| I | 2261.00 | NIST | |
| I | 2243.00 | NIST | |
| I | 2285.00 | NIST | |
| I | 2298.00 | NIST | |
| I | 2278.00 | NIST | |
| I | 2266.00 | NIST | |
| I | 2269.00 | NIST | |
| I | 2263.00 | NIST | |
| I | 2264.00 | NIST | |
| I | 2298.00 | NIST | |
| I | 2271.00 | NIST | |
| I | 2298.00 | NIST | |
| I | 2313.00 | NIST | |
| I | 2300.00 | NIST | |
| I | 2283.00 | NIST | |
| I | 2273.00 | NIST | |
| I | 2274.00 | NIST | |
| I | 2264.00 | NIST | |
| I | 2296.00 | NIST | |
| I | 2262.00 | NIST | |
| I | 2296.00 | NIST | |
| I | 2296.00 | NIST | |
| I | 2240.00 | NIST | |
| I | 2300.00 | NIST | |
| I | 2298.00 | NIST | |
| I | 2266.00 | NIST | |
| I | 2255.00 | NIST | |
| I | 2298.00 | NIST | |
| I | 2286.00 | NIST | |
| I | 2254.00 | NIST | |
| I | 2298.00 | NIST | |
| I | 2298.00 | NIST | |
| I | Outlier 2227.00 | NIST | |
| I | 2298.00 | NIST | |
| I | 2300.00 | NIST | |
| I | 2298.00 | NIST | |
| I | 2300.00 | NIST | |
| I | 2296.00 | NIST | |
| I | 2261.00 | NIST | |
| I | 2273.00 | NIST | |
| I | 2300.00 | NIST | |
| I | 2300.00 | NIST | |
| I | 2300.00 | NIST | |
| I | 2298.00 | NIST | |
| I | 2300.00 | NIST | |
| I | 2242.00 | NIST | |
| I | 2300.00 | NIST | |
| I | 2300.00 | NIST | |
| I | 2276.00 | NIST | |
| I | 2266.00 | NIST | |
| I | 2270.00 | NIST | |
| I | 2300.00 | NIST | |
| I | 2300.00 | NIST | |
| I | 2300.00 | NIST | |
| I | 2296.00 | NIST | |
| I | 2245.00 | NIST | |
| I | 2264.00 | NIST | |
| I | 2278.00 | NIST | |
| I | 2238.00 | NIST | |
| I | 2238.00 | NIST | |
| I | 2290.00 | NIST | |
| I | 2263.00 | NIST | |
| I | 2253.00 | NIST | |
| I | 2251.00 | NIST | |
| I | 2274.00 | NIST | |
| I | 2272.00 | NIST | |
| I | 2268.00 | NIST | |
| I | 2307.00 | NIST | |
| I | 2258.00 | NIST | |
| I | 2295.00 | NIST | |
| I | 2270.00 | NIST | |
| I | 2280.00 | NIST | |
| I | 2300.00 | NIST | |
| I | 2296.00 | NIST | |
| I | 2237.00 | NIST | |
| I | 2279.00 | NIST | |
| Tboil | [435.65; 544.15] | K |
|
| Tboil | 541.90 | K | KDB |
| Tboil | 543.20 | K | NIST |
| Tboil | 541.00 ± 2.00 | K | NIST |
| Tboil | 542.15 ± 3.00 | K | NIST |
| Tboil | 541.95 ± 1.00 | K | NIST |
| Tboil | Outlier 435.65 ± 3.00 | K | NIST |
| Tboil | 535.65 ± 5.00 | K | NIST |
| Tboil | 540.15 ± 4.00 | K | NIST |
| Tboil | 544.15 ± 3.00 | K | NIST |
| Tboil | 541.65 ± 3.00 | K | NIST |
| Tboil | 542.15 ± 4.00 | K | NIST |
| Tc | [720.53; 726.00] | K |
|
| Tc | 726.00 | K | KDB |
| Tc | 726.00 ± 4.00 | K | NIST |
| Tc | 720.53 ± 3.00 | K | NIST |
| Tfus | [300.10; 305.46] | K |
|
| Tfus | 304.53 | K | Aq. Solubility Prediction |
| Tfus | 305.14 | K | KDB |
| Tfus | 304.75 | K | Measurement and PC-SAFT modeling of solid-liquid equilibrium of deep eutectic solvents of quaternary ammonium chlorides and carboxylic acids |
| Tfus | 305.22 | K | Solid-liquid phase equilibrium diagrams of binary mixtures containing fatty acids, fatty alcohol compounds and tripalmitin using differential scanning calorimetry |
| Tfus | 305.46 | K | The solid liquid phase diagrams of binary mixtures of even saturated fatty acids differing by six carbon atoms |
| Tfus | 305.15 | K | Prediction of the properties of eutectic fatty acid phase change materials |
| Tfus | 304.42 | K | Solid-Liquid Equilibrium of Binary Fatty Acid Mixtures |
| Tfus | 304.70 ± 0.05 | K | NIST |
| Tfus | 304.00 ± 1.60 | K | NIST |
| Tfus | 303.90 ± 1.00 | K | NIST |
| Tfus | 305.00 ± 3.00 | K | NIST |
| Tfus | 303.40 ± 0.50 | K | NIST |
| Tfus | 304.00 ± 2.00 | K | NIST |
| Tfus | 303.65 ± 2.00 | K | NIST |
| Tfus | 302.90 ± 1.50 | K | NIST |
| Tfus | 304.40 ± 0.20 | K | NIST |
| Tfus | 304.15 ± 2.00 | K | NIST |
| Tfus | Outlier 300.10 ± 1.00 | K | NIST |
| Tfus | 304.60 ± 2.00 | K | NIST |
| Ttriple | [303.95; 304.55] | K |
|
| Ttriple | 304.55 ± 0.02 | K | NIST |
| Ttriple | 303.95 ± 0.50 | K | NIST |
| Vc | 0.608 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [402.78; 469.86] | J/mol×K | [574.25; 741.22] |
|
| Cp,gas | 402.78 | J/mol×K | 574.25 | Joback Calculated Property |
| Cp,gas | 415.22 | J/mol×K | 602.08 | Joback Calculated Property |
| Cp,gas | 427.13 | J/mol×K | 629.91 | Joback Calculated Property |
| Cp,gas | 438.54 | J/mol×K | 657.73 | Joback Calculated Property |
| Cp,gas | 449.45 | J/mol×K | 685.56 | Joback Calculated Property |
| Cp,gas | 459.89 | J/mol×K | 713.39 | Joback Calculated Property |
| Cp,gas | 469.86 | J/mol×K | 741.22 | Joback Calculated Property |
| Cp,solid | [361.10; 475.59] | J/mol×K | [285.00; 298.15] |
|
| Cp,solid | 361.10 | J/mol×K | 285.00 | NIST |
| Cp,solid | 475.59 | J/mol×K | 298.15 | NIST |
| η | [0.0001044; 0.0111394] | Pa×s | [313.21; 574.25] |
|
| η | 0.0111394 | Pa×s | 313.21 | Joback Calculated Property |
| η | 0.0031819 | Pa×s | 356.72 | Joback Calculated Property |
| η | 0.0011935 | Pa×s | 400.22 | Joback Calculated Property |
| η | 0.0005426 | Pa×s | 443.73 | Joback Calculated Property |
| η | 0.0002839 | Pa×s | 487.24 | Joback Calculated Property |
| η | 0.0001652 | Pa×s | 530.74 | Joback Calculated Property |
| η | 0.0001044 | Pa×s | 574.25 | Joback Calculated Property |
| ΔfusH | [27.82; 29.22] | kJ/mol | [300.10; 304.50] |
|
| ΔfusH | 29.22 | kJ/mol | 300.10 | NIST |
| ΔfusH | 28.30 | kJ/mol | 303.80 | NIST |
| ΔfusH | 27.99 | kJ/mol | 304.40 | NIST |
| ΔfusH | 27.82 | kJ/mol | 304.50 | NIST |
| ΔfusH | 27.99 | kJ/mol | 304.50 | NIST |
| ΔsubH | [117.00; 117.10] | kJ/mol | [289.80; 295.50] |
|
| ΔsubH | 117.00 ± 2.00 | kJ/mol | 289.80 | NIST |
| ΔsubH | 117.10 ± 1.70 | kJ/mol | 295.50 | NIST |
| ΔvapH | [71.40; 88.60] | kJ/mol | [314.00; 470.50] |
|
| ΔvapH | 88.60 | kJ/mol | 314.00 | NIST |
| ΔvapH | 71.40 | kJ/mol | 418.00 | NIST |
| ΔvapH | 76.40 | kJ/mol | 470.50 | NIST |
| ρl | [761.90; 878.00] | kg/m3 | [322.10; 472.20] |
|
| ρl | 878.00 | kg/m3 | 322.10 | Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K |
| ρl | 871.00 | kg/m3 | 332.10 | Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K |
| ρl | 855.30 | kg/m3 | 352.10 | Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K |
| ρl | 843.10 | kg/m3 | 368.30 | Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K |
| ρl | 827.30 | kg/m3 | 388.30 | Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K |
| ρl | 812.20 | kg/m3 | 408.20 | Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K |
| ρl | 797.20 | kg/m3 | 427.20 | Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K |
| ρl | 796.40 | kg/m3 | 428.20 | Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K |
| ρl | 784.90 | kg/m3 | 442.20 | Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K |
| ρl | 772.90 | kg/m3 | 457.20 | Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K |
| ρl | 761.90 | kg/m3 | 472.20 | Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K |
| ΔfusS | [92.00; 97.40] | J/mol×K | [300.10; 304.40] |
|
| ΔfusS | 97.40 | J/mol×K | 300.10 | NIST |
| ΔfusS | 92.00 | J/mol×K | 304.40 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 422.20 | K | 1.50 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [426.58; 554.19] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.62028e+01 | |||
| Coefficient B | -4.40263e+03 | |||
| Coefficient C | -1.49953e+02 | |||
| Temperature range, min. | 426.58 | |||
| Temperature range, max. | 554.19 | |||
| Pvap | 1.33 | kPa | 426.58 | Calculated Property |
| Pvap | 2.90 | kPa | 440.76 | Calculated Property |
| Pvap | 5.85 | kPa | 454.94 | Calculated Property |
| Pvap | 11.12 | kPa | 469.12 | Calculated Property |
| Pvap | 19.99 | kPa | 483.30 | Calculated Property |
| Pvap | 34.26 | kPa | 497.47 | Calculated Property |
| Pvap | 56.30 | kPa | 511.65 | Calculated Property |
| Pvap | 89.11 | kPa | 525.83 | Calculated Property |
| Pvap | 136.41 | kPa | 540.01 | Calculated Property |
| Pvap | 202.67 | kPa | 554.19 | Calculated Property |
| Pvap | [1.32e-05; 2336.98] | kPa | [304.75; 713.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 4.88007e+02 | |||
| Coefficient B | -3.39121e+04 | |||
| Coefficient C | -6.83540e+01 | |||
| Coefficient D | 3.21849e-05 | |||
| Temperature range, min. | 304.75 | |||
| Temperature range, max. | 713.00 | |||
| Pvap | 1.32e-05 | kPa | 304.75 | Calculated Property |
| Pvap | 4.78e-03 | kPa | 350.11 | Calculated Property |
| Pvap | 0.23 | kPa | 395.47 | Calculated Property |
| Pvap | 3.16 | kPa | 440.83 | Calculated Property |
| Pvap | 19.81 | kPa | 486.19 | Calculated Property |
| Pvap | 75.73 | kPa | 531.56 | Calculated Property |
| Pvap | 213.62 | kPa | 576.92 | Calculated Property |
| Pvap | 505.84 | kPa | 622.28 | Calculated Property |
| Pvap | 1099.51 | kPa | 667.64 | Calculated Property |
| Pvap | 2336.98 | kPa | 713.00 | Calculated Property |
Similar Compounds
Find more compounds similar to n-Decanoic acid.
Mixtures
- n-Decanoic acid + Tetramethylammonium chloride
- Tripalmitin + n-Decanoic acid
- n-Decanoic acid + n-Hexadecanoic acid
- 1-Dodecanol + n-Decanoic acid
- Dodecanoic acid + n-Decanoic acid
- n-Decanoic acid + Tetradecanoic acid
- Octadecanoic acid + n-Decanoic acid
- n-Decanoic acid + Methyl Alcohol
- Ethanol + n-Decanoic acid
- n-Decanoic acid + Acetone
- n-Hexane + n-Decanoic acid
- n-Decanoic acid + Cyclohexane
- Toluene + n-Decanoic acid
- n-Decanoic acid + Thymol
- Lidocaine + n-Decanoic acid
- 5-Hydroxymethylfurfural + n-Decanoic acid + Thymol
- Lidocaine + n-Decanoic acid + Water
- n-Decanoic acid + Thymol + Water
- n-Decanoic acid + Heptane
- n-Decanoic acid + Pentane, 2,2,4-trimethyl-
Find more mixtures with n-Decanoic acid.
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Crippen Method
- Measurements of activity coefficients at infinite dilution in vegetable oils and capric acid using the dilutor technique
- Measurement and PC-SAFT modeling of solid-liquid equilibrium of deep eutectic solvents of quaternary ammonium chlorides and carboxylic acids
- 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
- 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
- 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
- Thermophysical Properties and Solubility of Different Sugar-Derived Molecules in Deep Eutectic Solvents
- Carbon Dioxide Solubilities in Decanoic Acid-Based Hydrophobic Deep Eutectic Solvents
- Solid-Liquid Equilibrium of Binary Systems Containing Fatty Acids and Fatty Alcohols Using Differential Scanning Calorimetry
- Fixed-Path Length Laser-Induced Sound Pinging: A Streamlined Method for Sound Speed Determination in Arbitrary Liquids
- Solid-Liquid Equilibrium of Binary Fatty Acid Mixtures
- Phase Equilibria of Long-Chain Carboxylic Acids in Supercritical Propane
- Viscosities of Fatty Mixtures: Experimental Data and Prediction
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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