- InChI
- InChI=1S/C9H18O/c1-3-4-5-6-7-8-9(2)10/h3-8H2,1-2H3
- InChI Key
- VKCYHJWLYTUGCC-UHFFFAOYSA-N
- Formula
- C9H18O
- SMILES
- CCCCCCCC(C)=O
- Molecular Weight1
- 142.24
- CAS
- 821-55-6
- Other Names
-
- Ketone, heptyl methyl
- METHYL-N-HEPTYL KETONE
- Methyl n-heptyl ketone
- NONANONE-2
- Nonan-2-one
- heptyl methyl ketone
- methyl heptyl ketone
- n-C7H15COCH3
- «beta»-Nonanone
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- 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).
- 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).
- 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.
- I : 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 | 0.5347 | Relay (1.0) Calculated Property | |
| ΔcH°liquid | -5716.80 ± 1.20 | kJ/mol | NIST |
| ΔfG° | -104.02 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -340.80 ± 1.70 | kJ/mol | NIST |
| ΔfH°liquid | -397.20 ± 1.70 | kJ/mol | NIST |
| 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° | 56.44 ± 0.06 | kJ/mol | NIST |
| IE | [9.16; 9.38] | eV |
|
| IE | 9.16 | eV | NIST |
| IE | 9.32 ± 0.02 | eV | NIST |
| IE | 9.38 | eV | NIST |
| log10WS | [-2.58; -2.58] |
|
|
| log10WS | -2.58 | Aq. Solubility Prediction | |
| log10WS | -2.58 | Estimated Solubility | |
| logPoct/wat | 2.936 | Crippen Calculated Property | |
| McVol | 139.240 | ml/mol | McGowan Calculated Property |
| Pc | 2482.00 ± 10.00 | kPa | NIST |
| ρc | 254.61 ± 3.56 | kg/m3 | NIST |
| Inp | [180.86; 1104.00] |
|
|
| Inp | 1059.00 | NIST | |
| Inp | 1069.76 | NIST | |
| Inp | 1076.02 | NIST | |
| Inp | 1078.68 | NIST | |
| Inp | 1090.28 | NIST | |
| Inp | 1093.07 | NIST | |
| Inp | 1094.79 | NIST | |
| Inp | 1093.10 | NIST | |
| Inp | 1073.40 | NIST | |
| Inp | 1079.80 | NIST | |
| Inp | 1094.30 | NIST | |
| Inp | 1095.20 | NIST | |
| Inp | 1096.80 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1055.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1099.10 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1079.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1099.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1098.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1068.40 | NIST | |
| Inp | 1089.60 | NIST | |
| Inp | 1103.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1077.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1098.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1077.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1101.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1099.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1092.40 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1085.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1049.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1100.00 | NIST | |
| Inp | 1098.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1087.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1079.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1102.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1087.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | Outlier 180.86 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1098.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1087.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1092.40 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1075.00 | NIST | |
| I | [1342.00; 1420.00] |
|
|
| I | 1367.90 | NIST | |
| I | 1380.00 | NIST | |
| I | 1385.70 | NIST | |
| I | 1397.00 | NIST | |
| I | 1386.00 | NIST | |
| I | 1385.00 | NIST | |
| I | 1386.00 | NIST | |
| I | 1390.00 | NIST | |
| I | 1379.00 | NIST | |
| I | 1387.00 | NIST | |
| I | 1382.00 | NIST | |
| I | 1379.00 | NIST | |
| I | 1391.00 | NIST | |
| I | 1385.00 | NIST | |
| I | 1381.00 | NIST | |
| I | 1380.00 | NIST | |
| I | 1413.00 | NIST | |
| I | 1415.00 | NIST | |
| I | 1374.00 | NIST | |
| I | 1382.00 | NIST | |
| I | 1386.00 | NIST | |
| I | 1380.00 | NIST | |
| I | 1398.00 | NIST | |
| I | 1393.00 | NIST | |
| I | 1386.00 | NIST | |
| I | 1393.00 | NIST | |
| I | 1379.00 | NIST | |
| I | 1389.00 | NIST | |
| I | 1374.00 | NIST | |
| I | 1394.00 | NIST | |
| I | 1403.00 | NIST | |
| I | 1394.00 | NIST | |
| I | 1389.00 | NIST | |
| I | 1393.00 | NIST | |
| I | 1393.00 | NIST | |
| I | 1391.00 | NIST | |
| I | 1384.00 | NIST | |
| I | 1391.00 | NIST | |
| I | Outlier 1342.00 | NIST | |
| I | Outlier 1347.00 | NIST | |
| I | Outlier 1347.00 | NIST | |
| I | 1377.00 | NIST | |
| I | 1394.00 | NIST | |
| I | 1396.00 | NIST | |
| I | 1380.00 | NIST | |
| I | 1370.00 | NIST | |
| I | 1382.00 | NIST | |
| I | 1394.00 | NIST | |
| I | 1394.00 | NIST | |
| I | 1392.00 | NIST | |
| I | 1394.00 | NIST | |
| I | 1374.00 | NIST | |
| I | 1413.00 | NIST | |
| I | 1390.00 | NIST | |
| I | 1395.00 | NIST | |
| I | 1379.00 | NIST | |
| I | 1394.00 | NIST | |
| I | 1391.00 | NIST | |
| I | 1393.00 | NIST | |
| I | 1392.00 | NIST | |
| I | 1402.00 | NIST | |
| I | 1366.00 | NIST | |
| I | 1388.00 | NIST | |
| I | 1385.00 | NIST | |
| I | 1380.00 | NIST | |
| I | 1392.00 | NIST | |
| I | 1392.00 | NIST | |
| I | 1392.00 | NIST | |
| I | 1389.00 | NIST | |
| I | 1391.00 | NIST | |
| I | 1393.00 | NIST | |
| I | 1398.00 | NIST | |
| I | 1412.00 | NIST | |
| I | 1417.00 | NIST | |
| I | 1405.00 | NIST | |
| I | 1415.00 | NIST | |
| I | 1379.00 | NIST | |
| I | Outlier 1350.00 | NIST | |
| I | 1380.00 | NIST | |
| I | 1388.00 | NIST | |
| I | 1388.00 | NIST | |
| I | 1388.00 | NIST | |
| I | Outlier 1420.00 | NIST | |
| I | 1372.00 | NIST | |
| I | 1383.00 | NIST | |
| I | 1397.00 | NIST | |
| I | 1405.00 | NIST | |
| I | 1405.00 | NIST | |
| I | 1401.00 | NIST | |
| I | 1381.00 | NIST | |
| I | 1389.00 | NIST | |
| I | 1405.00 | NIST | |
| I | 1366.00 | NIST | |
| I | 1373.00 | NIST | |
| I | Outlier 1420.00 | NIST | |
| I | 1397.00 | NIST | |
| I | 1401.00 | NIST | |
| I | 1384.00 | NIST | |
| I | 1390.00 | NIST | |
| I | 1386.00 | NIST | |
| I | 1389.00 | NIST | |
| I | 1390.00 | NIST | |
| I | 1398.00 | NIST | |
| I | 1366.00 | NIST | |
| I | 1392.00 | NIST | |
| I | 1394.00 | NIST | |
| I | 1392.00 | NIST | |
| I | 1388.00 | NIST | |
| I | 1392.00 | NIST | |
| I | 1398.00 | NIST | |
| I | 1398.00 | NIST | |
| I | 1374.00 | NIST | |
| I | 1398.00 | NIST | |
| I | 1398.00 | NIST | |
| I | 1377.00 | NIST | |
| I | Outlier 1420.00 | NIST | |
| I | 1402.00 | NIST | |
| I | 1395.00 | NIST | |
| I | 1396.00 | NIST | |
| I | 1387.00 | NIST | |
| I | 1396.00 | NIST | |
| I | Outlier 1420.00 | NIST | |
| I | 1367.90 | NIST | |
| I | 1390.00 | NIST | |
| I | 1391.00 | NIST | |
| I | 1415.00 | NIST | |
| I | 1398.00 | NIST | |
| I | 1389.00 | NIST | |
| I | 1394.00 | NIST | |
| Tboil | [461.65; 473.15] | K |
|
| Tboil | 468.50 | K | NIST |
| Tboil | 468.15 ± 2.00 | K | NIST |
| Tboil | 467.15 ± 2.00 | K | NIST |
| Tboil | 467.55 ± 2.00 | K | NIST |
| Tboil | Outlier 461.65 ± 2.00 | K | NIST |
| Tboil | 467.15 ± 2.00 | K | NIST |
| Tboil | Outlier 473.15 ± 2.00 | K | NIST |
| Tboil | 468.45 ± 2.00 | K | NIST |
| Tboil | 468.15 ± 2.00 | K | NIST |
| Tboil | 464.65 ± 2.00 | K | NIST |
| Tboil | 468.15 ± 2.00 | K | NIST |
| Tc | [651.90; 652.50] | K |
|
| Tc | 651.90 ± 0.20 | K | NIST |
| Tc | 652.50 ± 0.25 | K | NIST |
| Tfus | [205.90; 262.98] | K |
|
| Tfus | 262.98 | K | Aq. Solubility Prediction |
| Tfus | 205.90 ± 0.40 | K | NIST |
| Vc | 0.535 | m3/kmol | Relay (1.0) Calculated Property |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 465.20 | K | 99.10 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [197.33; 472.67] | 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 | 2.06600e+00 | |||
| Coefficient B | 8.30840e-01 | |||
| Coefficient C | -4.47100e-04 | |||
| Coefficient D | 8.68600e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 197.33 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 243.89 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 285.81 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 323.38 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 356.86 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 386.54 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 412.68 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 435.57 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 455.47 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 472.67 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0053139; 0.0002884] | Pa×s | [234.44; 456.54] |
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 | -1.12265e+01 | |||
| Coefficient B | 1.40407e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 234.44 | |||
| Temperature range, max. | 456.54 | |||
| η | 0.0053139 | Pa×s | 234.44 | Calculated Property |
| η | 0.0030040 | Pa×s | 259.12 | Calculated Property |
| η | 0.0018753 | Pa×s | 283.80 | Calculated Property |
| η | 0.0012623 | Pa×s | 308.47 | Calculated Property |
| η | 0.0009010 | Pa×s | 333.15 | Calculated Property |
| η | 0.0006738 | Pa×s | 357.83 | Calculated Property |
| η | 0.0005231 | Pa×s | 382.51 | Calculated Property |
| η | 0.0004188 | Pa×s | 407.18 | Calculated Property |
| η | 0.0003439 | Pa×s | 431.86 | Calculated Property |
| η | 0.0002884 | Pa×s | 456.54 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [351.22; 496.37] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.50095e+01 | |||
| Coefficient B | -4.12511e+03 | |||
| Coefficient C | -7.10180e+01 | |||
| Temperature range, min. | 351.22 | |||
| Temperature range, max. | 496.37 | |||
| Pvap | 1.33 | kPa | 351.22 | Calculated Property |
| Pvap | 2.97 | kPa | 367.35 | Calculated Property |
| Pvap | 6.09 | kPa | 383.48 | Calculated Property |
| Pvap | 11.65 | kPa | 399.60 | Calculated Property |
| Pvap | 20.96 | kPa | 415.73 | Calculated Property |
| Pvap | 35.79 | kPa | 431.86 | Calculated Property |
| Pvap | 58.36 | kPa | 447.99 | Calculated Property |
| Pvap | 91.43 | kPa | 464.11 | Calculated Property |
| Pvap | 138.27 | kPa | 480.24 | Calculated Property |
| Pvap | 202.63 | kPa | 496.37 | Calculated Property |
| Pvap | [0.66; 105.02] | kPa | [335.15; 468.15] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.28514e+02 | |||
| Coefficient B | -1.12636e+04 | |||
| Coefficient C | -1.65872e+01 | |||
| Coefficient D | 9.99868e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 335.15 | |||
| Temperature range, max. | 468.15 | |||
| Pvap | 0.66 | kPa | 335.15 | Calculated Property |
| Pvap | 1.47 | kPa | 349.93 | Calculated Property |
| Pvap | 3.04 | kPa | 364.71 | Calculated Property |
| Pvap | 5.84 | kPa | 379.48 | Calculated Property |
| Pvap | 10.56 | kPa | 394.26 | Calculated Property |
| Pvap | 18.13 | kPa | 409.04 | Calculated Property |
| Pvap | 29.73 | kPa | 423.82 | Calculated Property |
| Pvap | 46.83 | kPa | 438.59 | Calculated Property |
| Pvap | 71.22 | kPa | 453.37 | Calculated Property |
| Pvap | 105.02 | kPa | 468.15 | Calculated Property |
| Pvap | [0.13; 100.55] | kPa | [305.30; 468.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.54824e+01 | |||
| Coefficient B | -4.67541e+03 | |||
| Coefficient C | -3.79480e+01 | |||
| Reference | Stull, 1947 | |||
| Temperature range, min. | 305.30 | |||
| Temperature range, max. | 468.00 | |||
| Pvap | 0.13 | kPa | 305.30 | Calculated Property |
| Pvap | 0.41 | kPa | 323.38 | Calculated Property |
| Pvap | 1.08 | kPa | 341.46 | Calculated Property |
| Pvap | 2.57 | kPa | 359.53 | Calculated Property |
| Pvap | 5.57 | kPa | 377.61 | Calculated Property |
| Pvap | 11.17 | kPa | 395.69 | Calculated Property |
| Pvap | 20.94 | kPa | 413.77 | Calculated Property |
| Pvap | 37.07 | kPa | 431.84 | Calculated Property |
| Pvap | 62.40 | kPa | 449.92 | Calculated Property |
| Pvap | 100.55 | kPa | 468.00 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Nonanone.
Mixtures
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Crippen Method
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- Measurements, Correlations, and Mod. UNIFAC (Do) Prediction of (Solid-Liquid) Phase Equilibria Diagrams in Binary Systems (Aliphatic Ketone + an Alcohol)
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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