- 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
- 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).
- 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.
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 | -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-L... |
| 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° | 61.28 | kJ/mol | Joback Calculated Property |
| log10WS | -3.44 | Aq. Sol... | |
| 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. Sol... |
| Tfus | 305.14 | K | KDB |
| Tfus | 304.75 | K | Measure... |
| Tfus | 305.22 | K | Solid-l... |
| Tfus | 305.46 | K | The sol... |
| Tfus | 305.15 | K | Predict... |
| Tfus | 304.42 | K | Solid-L... |
| 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 | 0.621 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [402.78; 469.86] | J/mol×K | [574.25; 741.22] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 400 410 420 430 440 450 460 470 600 650 700 | ||||
| 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] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 2.00e-3 4.00e-3 6.00e-3 8.00e-3 0.01 0.01 400 500 | ||||
| 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] |
|
|
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 27.8 28 28.2 28.4 28.6 28.8 29 29.2 300 302 304 | ||||
| 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] |
|
|
T(K) Liquid Density (kg/m3) 760 780 800 820 840 860 880 350 400 450 | ||||
| ρl | 878.00 | kg/m3 | 322.10 | Density... |
| ρl | 871.00 | kg/m3 | 332.10 | Density... |
| ρl | 855.30 | kg/m3 | 352.10 | Density... |
| ρl | 843.10 | kg/m3 | 368.30 | Density... |
| ρl | 827.30 | kg/m3 | 388.30 | Density... |
| ρl | 812.20 | kg/m3 | 408.20 | Density... |
| ρl | 797.20 | kg/m3 | 427.20 | Density... |
| ρl | 796.40 | kg/m3 | 428.20 | Density... |
| ρl | 784.90 | kg/m3 | 442.20 | Density... |
| ρl | 772.90 | kg/m3 | 457.20 | Density... |
| ρl | 761.90 | kg/m3 | 472.20 | Density... |
| 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 Yaw...
|
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 | ||||
| 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 Vap...
|
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 400 600 | ||||
| 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
- 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
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.