- InChI
- InChI=1S/C10H18O2/c1-2-3-4-5-6-9-7-8-10(11)12-9/h9H,2-8H2,1H3
- InChI Key
- IFYYFLINQYPWGJ-UHFFFAOYSA-N
- Formula
- C10H18O2
- SMILES
- CCCCCCC1CCC(=O)O1
- Molecular Weight1
- 170.25
- CAS
- 706-14-9
- Other Names
-
- (.+/-.)-«gamma»-Decanolactone
- .gamma.-decalactone
- 4-Decalactone
- 4-Hexyl-4-butanolide
- 4-Hexyl-«gamma»-butyrolactone
- 4-Hydroxydecanoic acid lactone
- 4-Hydroxydecanoic acid, «gamma»-lactone
- 4-decanolide
- 4-hydroxydecanoic acid .gamma.-lactone
- 5-Hexyldihydro-2(3H)-furanone
- 5-Hexyltetrahydro-2-furanone
- Decan-4-olide
- Decanoic acid, 4-hydroxy-, «gamma»-lactone
- Decanoic acid, «gamma»-lactone
- Decanolactone
- Decanolide-1,4
- Hydroxydecanoic acid «gamma»-lactone
- NSC 24248
- NSC 26510
- «gamma»-Decalactone
- «gamma»-Decanolactone
- «gamma»-Decanolide
- «gamma»-Hexyl-«gamma»-butyrolactone
- «gamma»-Hexylbutyrolactone
- «gamma»-n-Decalactone
- «gamma»-n-Hexyl-«gamma»-butyrolactone
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (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).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (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 |
|---|---|---|---|
| ΔfG° | -138.84 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -496.00 ± 3.00 | kJ/mol | NIST |
| ΔfH°liquid | -559.00 ± 2.00 | kJ/mol | NIST |
| ΔfusH° | 23.08 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [63.00; 75.60] | kJ/mol |
|
| ΔvapH° | 75.60 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 63.00 ± 1.00 | kJ/mol | NIST |
| ΔvapH° | 63.00 | kJ/mol | NIST |
| log10WS | -2.88 | Crippen Calculated Property | |
| logPoct/wat | 2.662 | Crippen Calculated Property | |
| McVol | 148.340 | ml/mol | McGowan Calculated Property |
| Pc | 2571.50 | kPa | Joback Calculated Property |
| Inp | [1414.60; 1504.00] |
|
|
| Inp | 1431.40 | NIST | |
| Inp | 1463.00 | NIST | |
| Inp | 1428.00 | NIST | |
| Inp | 1419.00 | NIST | |
| Inp | 1423.00 | NIST | |
| Inp | 1428.00 | NIST | |
| Inp | 1422.00 | NIST | |
| Inp | 1424.00 | NIST | |
| Inp | 1422.00 | NIST | |
| Inp | 1425.00 | NIST | |
| Inp | 1418.00 | NIST | |
| Inp | 1465.00 | NIST | |
| Inp | 1490.00 | NIST | |
| Inp | 1485.00 | NIST | |
| Inp | 1486.00 | NIST | |
| Inp | 1470.00 | NIST | |
| Inp | 1494.00 | NIST | |
| Inp | 1468.00 | NIST | |
| Inp | 1472.00 | NIST | |
| Inp | 1414.60 | NIST | |
| Inp | 1472.00 | NIST | |
| Inp | 1463.00 | NIST | |
| Inp | 1431.00 | NIST | |
| Inp | 1478.00 | NIST | |
| Inp | Outlier 1503.00 | NIST | |
| Inp | Outlier 1504.00 | NIST | |
| Inp | 1476.00 | NIST | |
| Inp | 1474.00 | NIST | |
| Inp | 1472.60 | NIST | |
| Inp | 1470.00 | NIST | |
| Inp | 1462.00 | NIST | |
| Inp | 1465.00 | NIST | |
| Inp | 1472.00 | NIST | |
| Inp | 1470.00 | NIST | |
| Inp | 1467.00 | NIST | |
| Inp | 1450.00 | NIST | |
| Inp | 1472.00 | NIST | |
| Inp | 1470.00 | NIST | |
| Inp | 1472.00 | NIST | |
| Inp | 1472.00 | NIST | |
| Inp | 1468.00 | NIST | |
| Inp | 1448.00 | NIST | |
| Inp | 1467.00 | NIST | |
| Inp | 1467.00 | NIST | |
| Inp | 1416.00 | NIST | |
| Inp | 1423.00 | NIST | |
| Inp | 1475.00 | NIST | |
| Inp | 1466.00 | NIST | |
| Inp | 1418.00 | NIST | |
| Inp | 1418.00 | NIST | |
| Inp | 1476.00 | NIST | |
| Inp | 1487.00 | NIST | |
| Inp | 1429.00 | NIST | |
| Inp | 1429.00 | NIST | |
| Inp | 1422.00 | NIST | |
| Inp | 1435.00 | NIST | |
| Inp | 1470.00 | NIST | |
| Inp | 1477.00 | NIST | |
| Inp | 1430.00 | NIST | |
| Inp | 1428.00 | NIST | |
| Inp | 1462.00 | NIST | |
| Inp | 1470.00 | NIST | |
| Inp | 1454.00 | NIST | |
| Inp | 1475.00 | NIST | |
| Inp | 1437.00 | NIST | |
| Inp | 1437.00 | NIST | |
| Inp | 1439.00 | NIST | |
| Inp | 1437.00 | NIST | |
| Inp | 1429.00 | NIST | |
| Inp | 1445.00 | NIST | |
| Inp | 1470.00 | NIST | |
| Inp | 1470.00 | NIST | |
| Inp | 1418.00 | NIST | |
| Inp | 1465.00 | NIST | |
| Inp | 1494.00 | NIST | |
| Inp | 1463.00 | NIST | |
| Inp | 1476.00 | NIST | |
| Inp | 1435.00 | NIST | |
| Inp | 1462.00 | NIST | |
| Inp | 1437.00 | NIST | |
| Inp | 1470.00 | NIST | |
| Inp | 1431.40 | NIST | |
| I | [2090.00; 2185.00] |
|
|
| I | 2101.00 | NIST | |
| I | 2098.00 | NIST | |
| I | 2113.00 | NIST | |
| I | 2151.00 | NIST | |
| I | 2153.00 | NIST | |
| I | 2096.00 | NIST | |
| I | 2144.00 | NIST | |
| I | 2136.00 | NIST | |
| I | 2136.00 | NIST | |
| I | 2144.00 | NIST | |
| I | 2126.00 | NIST | |
| I | 2149.00 | NIST | |
| I | 2103.00 | NIST | |
| I | 2139.00 | NIST | |
| I | 2142.00 | NIST | |
| I | 2137.00 | NIST | |
| I | 2138.00 | NIST | |
| I | 2143.00 | NIST | |
| I | 2131.00 | NIST | |
| I | 2136.00 | NIST | |
| I | 2136.00 | NIST | |
| I | 2136.00 | NIST | |
| I | 2153.00 | NIST | |
| I | 2116.00 | NIST | |
| I | 2185.00 | NIST | |
| I | 2151.00 | NIST | |
| I | 2158.00 | NIST | |
| I | 2127.00 | NIST | |
| I | 2135.00 | NIST | |
| I | 2138.00 | NIST | |
| I | 2110.00 | NIST | |
| I | 2179.00 | NIST | |
| I | 2140.00 | NIST | |
| I | 2106.00 | NIST | |
| I | 2149.00 | NIST | |
| I | 2140.00 | NIST | |
| I | 2140.00 | NIST | |
| I | 2138.00 | NIST | |
| I | 2183.00 | NIST | |
| I | 2131.00 | NIST | |
| I | 2110.00 | NIST | |
| I | 2141.00 | NIST | |
| I | 2175.00 | NIST | |
| I | 2177.00 | NIST | |
| I | 2185.00 | NIST | |
| I | 2144.00 | NIST | |
| I | 2178.00 | NIST | |
| I | 2152.00 | NIST | |
| I | 2132.00 | NIST | |
| I | 2165.00 | NIST | |
| I | 2145.00 | NIST | |
| I | 2126.00 | NIST | |
| I | 2165.00 | NIST | |
| I | 2160.00 | NIST | |
| I | 2152.00 | NIST | |
| I | 2125.00 | NIST | |
| I | 2127.00 | NIST | |
| I | 2164.00 | NIST | |
| I | 2162.00 | NIST | |
| I | 2130.00 | NIST | |
| I | 2165.00 | NIST | |
| I | 2130.00 | NIST | |
| I | 2178.00 | NIST | |
| I | 2109.00 | NIST | |
| I | 2109.00 | NIST | |
| I | 2123.00 | NIST | |
| I | 2170.00 | NIST | |
| I | 2142.00 | NIST | |
| I | 2129.00 | NIST | |
| I | 2131.00 | NIST | |
| I | 2138.00 | NIST | |
| I | 2145.00 | NIST | |
| I | 2094.00 | NIST | |
| I | 2139.00 | NIST | |
| I | 2141.00 | NIST | |
| I | 2100.00 | NIST | |
| I | 2137.00 | NIST | |
| I | 2131.00 | NIST | |
| I | 2103.00 | NIST | |
| I | 2141.00 | NIST | |
| I | 2183.00 | NIST | |
| I | 2100.00 | NIST | |
| I | 2137.00 | NIST | |
| I | 2131.00 | NIST | |
| I | 2101.00 | NIST | |
| I | 2101.00 | NIST | |
| I | 2173.00 | NIST | |
| I | 2130.00 | NIST | |
| I | Outlier 2090.00 | NIST | |
| I | 2125.00 | NIST | |
| I | 2155.00 | NIST | |
| I | 2155.00 | NIST | |
| I | 2183.00 | NIST | |
| I | 2177.00 | NIST | |
| I | 2132.00 | NIST | |
| I | 2160.00 | NIST | |
| I | 2162.00 | NIST | |
| I | 2109.00 | NIST | |
| I | 2129.00 | NIST | |
| I | 2144.00 | NIST | |
| I | 2149.00 | NIST | |
| I | 2138.00 | NIST | |
| I | 2136.00 | NIST | |
| I | 2158.00 | NIST | |
| I | 2100.00 | NIST | |
| I | 2101.00 | NIST | |
| I | 2155.00 | NIST | |
| Tboil | 538.25 | K | Joback Calculated Property |
| Tc | 742.73 | K | Joback Calculated Property |
| Tfus | 308.15 | K | Joback Calculated Property |
| Vc | 0.565 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [370.23; 461.59] | J/mol×K | [538.25; 742.73] |
|
| Cp,gas | 370.23 | J/mol×K | 538.25 | Joback Calculated Property |
| Cp,gas | 387.45 | J/mol×K | 572.33 | Joback Calculated Property |
| Cp,gas | 403.86 | J/mol×K | 606.41 | Joback Calculated Property |
| Cp,gas | 419.47 | J/mol×K | 640.49 | Joback Calculated Property |
| Cp,gas | 434.30 | J/mol×K | 674.57 | Joback Calculated Property |
| Cp,gas | 448.34 | J/mol×K | 708.65 | Joback Calculated Property |
| Cp,gas | 461.59 | J/mol×K | 742.73 | Joback Calculated Property |
| ΔvapH | 75.00 | kJ/mol | 298.15 | Vapor p... |
| Pvap | [3.50e-04; 0.07] | kPa | [298.40; 365.00] |
|
| Pvap | 3.50e-04 | kPa | 298.40 | Vapour ... |
| Pvap | 5.60e-04 | kPa | 303.30 | Vapour ... |
| Pvap | 8.80e-04 | kPa | 308.20 | Vapour ... |
| Pvap | 1.46e-03 | kPa | 313.10 | Vapour ... |
| Pvap | 1.44e-03 | kPa | 313.40 | Vapour ... |
| Pvap | 2.14e-03 | kPa | 318.20 | Vapour ... |
| Pvap | 2.33e-03 | kPa | 318.20 | Vapour ... |
| Pvap | 3.39e-03 | kPa | 322.90 | Vapour ... |
| Pvap | 3.45e-03 | kPa | 323.20 | Vapour ... |
| Pvap | 5.32e-03 | kPa | 328.10 | Vapour ... |
| Pvap | 5.23e-03 | kPa | 328.20 | Vapour ... |
| Pvap | 7.65e-03 | kPa | 333.00 | Vapour ... |
| Pvap | 7.91e-03 | kPa | 333.20 | Vapour ... |
| Pvap | 0.01 | kPa | 338.10 | Vapour ... |
| Pvap | 0.01 | kPa | 338.70 | Vapour ... |
| Pvap | 0.02 | kPa | 343.20 | Vapour ... |
| Pvap | 0.02 | kPa | 343.90 | Vapour ... |
| Pvap | 0.02 | kPa | 348.20 | Vapour ... |
| Pvap | 0.03 | kPa | 349.40 | Vapour ... |
| Pvap | 0.03 | kPa | 353.30 | Vapour ... |
| Pvap | 0.04 | kPa | 354.80 | Vapour ... |
| Pvap | 0.05 | kPa | 360.30 | Vapour ... |
| Pvap | 0.07 | kPa | 365.00 | Vapour ... |
Similar Compounds
Find more compounds similar to 2(3H)-Furanone, 5-hexyldihydro-.
Sources
- Crippen Method
- Crippen Method
- Vapour pressures and enthalpies of vapourization of a series of the c-lactones
- Vapor pressures and enthalpies of vaporization of a series of .gamma. and .delta.-lactones by correlation gas chromatography
- Joback Method
- McGowan Method
- NIST Webbook
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that the value is more than 2 standard deviations away from the
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