- InChI
- InChI=1S/C11H22O/c1-3-4-5-6-7-8-9-10-11(2)12/h3-10H2,1-2H3
- InChI Key
- KYWIYKKSMDLRDC-UHFFFAOYSA-N
- Formula
- C11H22O
- SMILES
- CCCCCCCCCC(C)=O
- Molecular Weight1
- 170.29
- CAS
- 112-12-9
- Other Names
-
- 2-Hendecanone
- Ketone, methyl nonyl
- Methyl n-nonyl ketone
- Mgk dog & cat repellent
- Mgk dog and cat repellent
- Nonyl methyl ketone
- Undecan-2-one
- Undecanone-(2)
- methyl nonyl ketone
- ω : Acentric Factor.
- Cp,gas : Ideal gas 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).
- 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).
- Pvap : Vapor pressure (kPa).
- ρc : Critical density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (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 |
|---|---|---|---|
| ω | 0.6092 | Relay (1.0) Calculated Property | |
| ΔfG° | -87.18 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -402.04 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 27.35 | kJ/mol | Measurements, Correlations, and Mod. UNIFAC (Do) Prediction of (Solid-Liquid) Phase Equilibria Diagrams in Binary Systems (Aliphatic Ketone + an Alcohol) |
| ΔvapH° | [67.00; 69.70] | kJ/mol |
|
| ΔvapH° | 67.00 | kJ/mol | NIST |
| ΔvapH° | 69.70 ± 0.50 | kJ/mol | NIST |
| ΔvapH° | 67.00 ± 0.41 | kJ/mol | NIST |
| ΔvapH° | 67.00 ± 0.40 | kJ/mol | NIST |
| IE | 9.29 ± 0.01 | eV | NIST |
| log10WS | -3.83 | Relay (1.0) Calculated Property | |
| logPoct/wat | 3.716 | Crippen Calculated Property | |
| McVol | 167.420 | ml/mol | McGowan Calculated Property |
| Pc | 2045.61 | kPa | Joback Calculated Property |
| ρc | 245.22 ± 6.81 | kg/m3 | NIST |
| Inp | [220.32; 1315.00] |
|
|
| Inp | 1298.50 | NIST | |
| Inp | 1284.50 | NIST | |
| Inp | 1290.20 | NIST | |
| Inp | 1273.80 | NIST | |
| Inp | 1276.90 | NIST | |
| Inp | 1280.60 | NIST | |
| Inp | 1291.00 | NIST | |
| Inp | 1285.00 | NIST | |
| Inp | 1285.00 | NIST | |
| Inp | 1272.00 | NIST | |
| Inp | 1297.00 | NIST | |
| Inp | 1291.00 | NIST | |
| Inp | 1291.00 | NIST | |
| Inp | 1291.00 | NIST | |
| Inp | 1291.00 | NIST | |
| Inp | 1291.00 | NIST | |
| Inp | 1279.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1256.30 | NIST | |
| Inp | 1270.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1291.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1295.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1291.00 | NIST | |
| Inp | 1293.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1302.00 | NIST | |
| Inp | 1293.00 | NIST | |
| Inp | 1294.30 | NIST | |
| Inp | 1273.00 | NIST | |
| Inp | 1273.00 | NIST | |
| Inp | 1273.00 | NIST | |
| Inp | 1290.00 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1293.00 | NIST | |
| Inp | 1297.00 | NIST | |
| Inp | 1298.00 | NIST | |
| Inp | 1297.00 | NIST | |
| Inp | 1271.70 | NIST | |
| Inp | 1293.40 | NIST | |
| Inp | 1273.00 | NIST | |
| Inp | 1288.00 | NIST | |
| Inp | 1276.00 | NIST | |
| Inp | 1295.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1300.00 | NIST | |
| Inp | 1279.00 | NIST | |
| Inp | 1279.00 | NIST | |
| Inp | 1295.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1295.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1276.00 | NIST | |
| Inp | 1269.00 | NIST | |
| Inp | 1270.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1277.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1257.00 | NIST | |
| Inp | 1259.00 | NIST | |
| Inp | 1261.00 | NIST | |
| Inp | 1280.00 | NIST | |
| Inp | 1303.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1281.00 | NIST | |
| Inp | 1295.00 | NIST | |
| Inp | 1315.00 | NIST | |
| Inp | 1290.00 | NIST | |
| Inp | 1290.00 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1278.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1298.00 | NIST | |
| Inp | 1297.00 | NIST | |
| Inp | 1272.00 | NIST | |
| Inp | 1269.00 | NIST | |
| Inp | 1276.00 | NIST | |
| Inp | 1273.00 | NIST | |
| Inp | 1273.00 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1273.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1270.00 | NIST | |
| Inp | 1297.00 | NIST | |
| Inp | 1302.00 | NIST | |
| Inp | 1298.00 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1291.00 | NIST | |
| Inp | 1291.00 | NIST | |
| Inp | 1273.00 | NIST | |
| Inp | 1303.00 | NIST | |
| Inp | 1288.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1272.00 | NIST | |
| Inp | 1273.00 | NIST | |
| Inp | 1291.00 | NIST | |
| Inp | 1276.00 | NIST | |
| Inp | 1291.00 | NIST | |
| Inp | 1291.00 | NIST | |
| Inp | 1291.00 | NIST | |
| Inp | 1295.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1272.00 | NIST | |
| Inp | 1295.00 | NIST | |
| Inp | 1302.00 | NIST | |
| Inp | 1301.00 | NIST | |
| Inp | 1291.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1282.00 | NIST | |
| Inp | 1277.00 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1275.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1282.00 | NIST | |
| Inp | 1293.00 | NIST | |
| Inp | 1293.00 | NIST | |
| Inp | 1273.00 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1278.00 | NIST | |
| Inp | 1290.00 | NIST | |
| Inp | 1298.00 | NIST | |
| Inp | 1298.00 | NIST | |
| Inp | 1287.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1295.00 | NIST | |
| Inp | 1288.00 | NIST | |
| Inp | 1288.00 | NIST | |
| Inp | 1295.00 | NIST | |
| Inp | 1295.00 | NIST | |
| Inp | 1271.00 | NIST | |
| Inp | 1270.00 | NIST | |
| Inp | 1273.00 | NIST | |
| Inp | 1269.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1284.00 | NIST | |
| Inp | 1295.00 | NIST | |
| Inp | 1298.00 | NIST | |
| Inp | 1272.00 | NIST | |
| Inp | 1275.00 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1271.00 | NIST | |
| Inp | 1289.00 | NIST | |
| Inp | 1276.00 | NIST | |
| Inp | 1273.00 | NIST | |
| Inp | 1273.00 | NIST | |
| Inp | 1268.00 | NIST | |
| Inp | 1310.00 | NIST | |
| Inp | 1272.00 | NIST | |
| Inp | 1249.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1270.00 | NIST | |
| Inp | 1270.00 | NIST | |
| Inp | 1293.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1295.00 | NIST | |
| Inp | 1298.00 | NIST | |
| Inp | 1289.00 | NIST | |
| Inp | 1279.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1295.00 | NIST | |
| Inp | 1293.00 | NIST | |
| Inp | 1268.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1273.00 | NIST | |
| Inp | 1302.00 | NIST | |
| Inp | 1302.00 | NIST | |
| Inp | 1293.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1247.00 | NIST | |
| Inp | 1290.00 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1291.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1271.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1303.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1312.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1276.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1293.00 | NIST | |
| Inp | 1269.00 | NIST | |
| Inp | 1290.00 | NIST | |
| Inp | 1277.00 | NIST | |
| Inp | 1278.00 | NIST | |
| Inp | 1289.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1247.00 | NIST | |
| Inp | 1290.00 | NIST | |
| Inp | 1302.00 | NIST | |
| Inp | 1303.00 | NIST | |
| Inp | 1277.00 | NIST | |
| Inp | 1293.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1273.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | Outlier 220.32 | NIST | |
| Inp | 1291.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1295.00 | NIST | |
| Inp | 1302.00 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1271.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1276.00 | NIST | |
| Inp | 1277.00 | NIST | |
| Inp | 1290.00 | NIST | |
| Inp | 1279.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | Outlier 220.32 | NIST | |
| Inp | 1303.00 | NIST | |
| Inp | 1315.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Ip | [1564.00; 1628.00] |
|
|
| Ip | 1592.00 | NIST | |
| Ip | 1595.00 | NIST | |
| Ip | 1599.00 | NIST | |
| Ip | 1599.00 | NIST | |
| Ip | 1598.00 | NIST | |
| Ip | 1593.00 | NIST | |
| Ip | 1600.00 | NIST | |
| Ip | 1615.00 | NIST | |
| Ip | 1593.00 | NIST | |
| Ip | 1602.00 | NIST | |
| Ip | 1602.00 | NIST | |
| Ip | 1598.00 | NIST | |
| Ip | 1610.00 | NIST | |
| Ip | 1606.00 | NIST | |
| Ip | 1604.00 | NIST | |
| Ip | 1595.00 | NIST | |
| Ip | 1598.00 | NIST | |
| Ip | 1596.00 | NIST | |
| Ip | 1609.00 | NIST | |
| Ip | 1578.00 | NIST | |
| Ip | 1580.00 | NIST | |
| Ip | 1603.00 | NIST | |
| Ip | 1603.00 | NIST | |
| Ip | 1586.00 | NIST | |
| Ip | 1588.00 | NIST | |
| Ip | 1593.00 | NIST | |
| Ip | 1595.00 | NIST | |
| Ip | 1596.00 | NIST | |
| Ip | 1612.00 | NIST | |
| Ip | 1591.00 | NIST | |
| Ip | 1604.00 | NIST | |
| Ip | 1605.00 | NIST | |
| Ip | 1586.00 | NIST | |
| Ip | 1596.00 | NIST | |
| Ip | 1606.00 | NIST | |
| Ip | 1606.00 | NIST | |
| Ip | 1601.00 | NIST | |
| Ip | 1601.00 | NIST | |
| Ip | Outlier 1570.00 | NIST | |
| Ip | Outlier 1623.00 | NIST | |
| Ip | 1599.00 | NIST | |
| Ip | Outlier 1622.00 | NIST | |
| Ip | 1596.00 | NIST | |
| Ip | 1596.00 | NIST | |
| Ip | 1615.00 | NIST | |
| Ip | 1614.00 | NIST | |
| Ip | 1617.00 | NIST | |
| Ip | 1582.00 | NIST | |
| Ip | 1579.00 | NIST | |
| Ip | 1605.00 | NIST | |
| Ip | 1598.00 | NIST | |
| Ip | 1594.00 | NIST | |
| Ip | 1590.00 | NIST | |
| Ip | Outlier 1628.00 | NIST | |
| Ip | 1608.00 | NIST | |
| Ip | Outlier 1626.00 | NIST | |
| Ip | 1588.00 | NIST | |
| Ip | 1587.00 | NIST | |
| Ip | 1602.00 | NIST | |
| Ip | 1593.00 | NIST | |
| Ip | 1579.00 | NIST | |
| Ip | 1594.00 | NIST | |
| Ip | 1601.00 | NIST | |
| Ip | 1610.00 | NIST | |
| Ip | 1596.00 | NIST | |
| Ip | Outlier 1564.00 | NIST | |
| Ip | 1600.00 | NIST | |
| Ip | 1595.00 | NIST | |
| Ip | 1594.00 | NIST | |
| Ip | 1576.00 | NIST | |
| Ip | 1599.00 | NIST | |
| Ip | Outlier 1572.00 | NIST | |
| Ip | 1585.00 | NIST | |
| Ip | 1585.00 | NIST | |
| Ip | 1607.00 | NIST | |
| Ip | 1615.00 | NIST | |
| Ip | 1600.00 | NIST | |
| Ip | 1594.00 | NIST | |
| Ip | 1590.00 | NIST | |
| Ip | 1610.00 | NIST | |
| Ip | 1604.00 | NIST | |
| Ip | 1588.00 | NIST | |
| Ip | 1604.00 | NIST | |
| Ip | 1585.00 | NIST | |
| Ip | 1604.00 | NIST | |
| Ip | 1604.00 | NIST | |
| Ip | 1604.00 | NIST | |
| Ip | 1595.00 | NIST | |
| Ip | 1574.00 | NIST | |
| Ip | 1597.00 | NIST | |
| Ip | 1596.00 | NIST | |
| Ip | 1592.00 | NIST | |
| Ip | 1610.00 | NIST | |
| Ip | 1604.00 | NIST | |
| Ip | 1597.00 | NIST | |
| Ip | 1599.00 | NIST | |
| Ip | 1615.00 | NIST | |
| Ip | 1596.00 | NIST | |
| Ip | 1603.00 | NIST | |
| Ip | 1586.00 | NIST | |
| Ip | 1579.00 | NIST | |
| Ip | Outlier 1628.00 | NIST | |
| Ip | 1602.00 | NIST | |
| Ip | 1594.00 | NIST | |
| Ip | 1585.00 | NIST | |
| Ip | 1590.00 | NIST | |
| Tboil | [440.15; 505.15] | K |
|
| Tboil | 504.70 | K | NIST |
| Tboil | 501.00 ± 0.60 | K | NIST |
| Tboil | 501.00 ± 0.50 | K | NIST |
| Tboil | 503.15 ± 2.00 | K | NIST |
| Tboil | 505.15 ± 2.00 | K | NIST |
| Tboil | Outlier 440.15 ± 2.00 | K | NIST |
| Tboil | 503.75 ± 2.00 | K | NIST |
| Tboil | 501.20 ± 0.50 | K | NIST |
| Tboil | 505.15 ± 2.00 | K | NIST |
| Tboil | 498.15 ± 2.00 | K | NIST |
| Tboil | 498.15 ± 2.00 | K | NIST |
| Tboil | 505.15 ± 2.00 | K | NIST |
| Tboil | 498.65 ± 2.00 | K | NIST |
| Tc | [687.80; 688.00] | K |
|
| Tc | 688.00 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Tc | 687.80 ± 1.60 | K | NIST |
| Tfus | [285.30; 290.00] | K |
|
| Tfus | 285.65 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 290.00 ± 0.20 | K | NIST |
| Tfus | 285.30 ± 0.40 | K | NIST |
| Vc | 0.692 | m3/kmol | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔfusH | [28.78; 28.78] | kJ/mol | [290.50; 290.50] |
|
| ΔfusH | 28.78 | kJ/mol | 290.50 | NIST |
| ΔfusH | 28.78 | kJ/mol | 290.50 | NIST |
| ΔvapH | [46.40; 61.90] | kJ/mol | [384.00; 506.00] |
|
| ΔvapH | 61.60 | kJ/mol | 384.00 | NIST |
| ΔvapH | 61.90 | kJ/mol | 419.00 | NIST |
| ΔvapH | 56.20 | kJ/mol | 458.00 | NIST |
| ΔvapH | 51.50 | kJ/mol | 499.50 | NIST |
| ΔvapH | 46.40 | kJ/mol | 506.00 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 379.20 | K | 1.60 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [239.76; 575.85] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 2.48000e-01 | |||
| Coefficient B | 1.02084e+00 | |||
| Coefficient C | -5.55900e-04 | |||
| Coefficient D | 1.10660e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 239.76 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 296.72 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 347.97 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 393.84 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 434.68 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 470.86 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 502.72 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 530.60 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 554.86 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 575.85 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0027511; 0.0002924] | Pa×s | [286.98; 481.53] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.14445e+01 | |||
| Coefficient B | 1.59239e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 286.98 | |||
| Temperature range, max. | 481.53 | |||
| η | 0.0027511 | Pa×s | 286.98 | Calculated Property |
| η | 0.0018652 | Pa×s | 308.60 | Calculated Property |
| η | 0.0013305 | Pa×s | 330.22 | Calculated Property |
| η | 0.0009893 | Pa×s | 351.83 | Calculated Property |
| η | 0.0007613 | Pa×s | 373.45 | Calculated Property |
| η | 0.0006029 | Pa×s | 395.06 | Calculated Property |
| η | 0.0004891 | Pa×s | 416.68 | Calculated Property |
| η | 0.0004051 | Pa×s | 438.30 | Calculated Property |
| η | 0.0003415 | Pa×s | 459.91 | Calculated Property |
| η | 0.0002924 | Pa×s | 481.53 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [378.28; 532.02] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.50451e+01 | |||
| Coefficient B | -4.39569e+03 | |||
| Coefficient C | -8.04220e+01 | |||
| Temperature range, min. | 378.28 | |||
| Temperature range, max. | 532.02 | |||
| Pvap | 1.33 | kPa | 378.28 | Calculated Property |
| Pvap | 2.97 | kPa | 395.36 | Calculated Property |
| Pvap | 6.09 | kPa | 412.44 | Calculated Property |
| Pvap | 11.63 | kPa | 429.53 | Calculated Property |
| Pvap | 20.93 | kPa | 446.61 | Calculated Property |
| Pvap | 35.74 | kPa | 463.69 | Calculated Property |
| Pvap | 58.29 | kPa | 480.77 | Calculated Property |
| Pvap | 91.36 | kPa | 497.86 | Calculated Property |
| Pvap | 138.21 | kPa | 514.94 | Calculated Property |
| Pvap | 202.64 | kPa | 532.02 | Calculated Property |
| Pvap | [0.13; 100.92] | kPa | [341.30; 497.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.74891e+01 | |||
| Coefficient B | -5.89220e+03 | |||
| Coefficient C | -3.93420e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 341.30 | |||
| Temperature range, max. | 497.00 | |||
| Pvap | 0.13 | kPa | 341.30 | Calculated Property |
| Pvap | 0.38 | kPa | 358.60 | Calculated Property |
| Pvap | 0.98 | kPa | 375.90 | Calculated Property |
| Pvap | 2.31 | kPa | 393.20 | Calculated Property |
| Pvap | 5.02 | kPa | 410.50 | Calculated Property |
| Pvap | 10.18 | kPa | 427.80 | Calculated Property |
| Pvap | 19.44 | kPa | 445.10 | Calculated Property |
| Pvap | 35.21 | kPa | 462.40 | Calculated Property |
| Pvap | 60.86 | kPa | 479.70 | Calculated Property |
| Pvap | 100.92 | kPa | 497.00 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Undecanone.
Mixtures
Sources
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Solubility of fragrance raw materials in water: Experimental study, correlations, and Mod. UNIFAC (Do) predictions
- Measurements, Correlations, and Mod. UNIFAC (Do) Prediction of (Solid-Liquid) Phase Equilibria Diagrams in Binary Systems (Aliphatic Ketone + an Alcohol)
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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