- InChI
- InChI=1S/C8H18O/c1-3-5-6-7-8(9)4-2/h8-9H,3-7H2,1-2H3
- InChI Key
- NMRPBPVERJPACX-UHFFFAOYSA-N
- Formula
- C8H18O
- SMILES
- CCCCCC(O)CC
- Molecular Weight1
- 130.23
- CAS
- 20296-29-1
- Other Names
-
- Amylethylcarbinol
- D-n-Octanol
- Ethyl-n-amylcarbinol
- Octan-3-ol
- Octanol-3
- ethylamylcarbinol
- n-octan-3-ol
- 3-Octanol
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid 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).
- 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).
- 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 | 0.6330 | Relay (1.0) Calculated Property | |
| Cp,liquid | 339.89 | J/mol×K | Vapour pressures and heat capacity measurements on the C7 C9 secondary aliphatic alcohols |
| ΔfG° | -122.78 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -379.51 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 17.04 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 67.90 ± 0.30 | kJ/mol | NIST |
| IE | 9.79 | eV | Relay (1.0) Calculated Property |
| log10WS | [-1.98; -1.98] |
|
|
| log10WS | -1.98 | Aq. Solubility Prediction | |
| log10WS | -1.98 | Estimated Solubility | |
| logPoct/wat | 2.338 | Crippen Calculated Property | |
| McVol | 129.450 | ml/mol | McGowan Calculated Property |
| Pc | 2811.36 | kPa | Joback Calculated Property |
| ρc | [252.64; 252.64] | kg/m3 |
|
| ρc | 252.64 | kg/m3 | NIST |
| ρc | 252.64 ± 6.51 | kg/m3 | NIST |
| Inp | [961.00; 1013.00] |
|
|
| Inp | 996.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 991.00 | NIST | |
| Inp | 999.00 | NIST | |
| Inp | 998.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 985.40 | NIST | |
| Inp | 990.00 | NIST | |
| Inp | 996.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 990.00 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 992.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | Outlier 1013.00 | NIST | |
| Inp | 980.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 997.00 | NIST | |
| Inp | 996.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 989.00 | NIST | |
| Inp | 995.90 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 991.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 988.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 999.00 | NIST | |
| Inp | 991.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 988.00 | NIST | |
| Inp | 998.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 997.00 | NIST | |
| Inp | 1004.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 996.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 997.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 977.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 979.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 990.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | Outlier 971.00 | NIST | |
| Inp | 980.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 980.00 | NIST | |
| Inp | 997.00 | NIST | |
| Inp | 998.00 | NIST | |
| Inp | 1001.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 996.00 | NIST | |
| Inp | Outlier 963.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 990.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 991.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 992.00 | NIST | |
| Inp | 998.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 1004.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 992.00 | NIST | |
| Inp | 999.00 | NIST | |
| Inp | 991.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 990.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 977.00 | NIST | |
| Inp | 988.00 | NIST | |
| Inp | 991.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 979.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 989.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 991.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 991.00 | NIST | |
| Inp | 992.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | Outlier 971.00 | NIST | |
| Inp | 987.00 | NIST | |
| Inp | 991.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 984.00 | NIST | |
| Inp | 988.00 | NIST | |
| Inp | 999.00 | NIST | |
| Inp | 980.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 983.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 984.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 996.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 1004.00 | NIST | |
| Inp | 996.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 990.00 | NIST | |
| Inp | 990.00 | NIST | |
| Inp | 991.00 | NIST | |
| Inp | Outlier 1012.00 | NIST | |
| Inp | Outlier 1013.00 | NIST | |
| Inp | 989.00 | NIST | |
| Inp | 991.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 988.00 | NIST | |
| Inp | Outlier 961.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 996.00 | NIST | |
| Inp | 987.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 979.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | Outlier 971.00 | NIST | |
| Inp | 980.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 990.00 | NIST | |
| Inp | 989.00 | NIST | |
| Inp | 988.00 | NIST | |
| Inp | 979.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 977.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 984.00 | NIST | |
| Inp | 983.00 | NIST | |
| Inp | 997.00 | NIST | |
| Inp | 985.40 | NIST | |
| Ip | [1356.00; 1427.00] |
|
|
| Ip | Outlier 1356.00 | NIST | |
| Ip | Outlier 1359.00 | NIST | |
| Ip | 1383.00 | NIST | |
| Ip | 1386.00 | NIST | |
| Ip | 1383.00 | NIST | |
| Ip | 1390.00 | NIST | |
| Ip | 1390.00 | NIST | |
| Ip | 1398.00 | NIST | |
| Ip | 1398.00 | NIST | |
| Ip | 1396.00 | NIST | |
| Ip | 1394.00 | NIST | |
| Ip | 1394.00 | NIST | |
| Ip | 1396.00 | NIST | |
| Ip | 1400.00 | NIST | |
| Ip | 1394.00 | NIST | |
| Ip | Outlier 1423.00 | NIST | |
| Ip | 1383.00 | NIST | |
| Ip | 1389.00 | NIST | |
| Ip | 1395.00 | NIST | |
| Ip | 1392.00 | NIST | |
| Ip | 1395.00 | NIST | |
| Ip | 1383.00 | NIST | |
| Ip | Outlier 1427.00 | NIST | |
| Ip | 1384.00 | NIST | |
| Ip | 1387.00 | NIST | |
| Ip | 1398.00 | NIST | |
| Ip | 1380.00 | NIST | |
| Ip | 1381.00 | NIST | |
| Ip | 1397.00 | NIST | |
| Ip | 1395.00 | NIST | |
| Ip | 1400.00 | NIST | |
| Ip | 1406.00 | NIST | |
| Ip | 1406.00 | NIST | |
| Ip | 1406.00 | NIST | |
| Ip | 1404.00 | NIST | |
| Ip | Outlier 1368.00 | NIST | |
| Ip | 1400.00 | NIST | |
| Ip | 1386.00 | NIST | |
| Ip | 1385.00 | NIST | |
| Ip | 1395.00 | NIST | |
| Ip | 1380.00 | NIST | |
| Ip | 1395.00 | NIST | |
| Ip | 1396.00 | NIST | |
| Ip | 1392.00 | NIST | |
| Ip | 1385.00 | NIST | |
| Ip | 1400.00 | NIST | |
| Ip | Outlier 1417.80 | NIST | |
| Ip | Outlier 1417.80 | NIST | |
| Ip | 1386.00 | NIST | |
| Ip | Outlier 1368.00 | NIST | |
| Ip | 1408.00 | NIST | |
| Ip | 1384.00 | NIST | |
| Ip | 1380.00 | NIST | |
| Ip | 1383.00 | NIST | |
| Ip | 1393.00 | NIST | |
| Ip | 1391.00 | NIST | |
| Ip | 1375.00 | NIST | |
| Ip | 1383.00 | NIST | |
| Ip | Outlier 1357.00 | NIST | |
| Ip | 1411.00 | NIST | |
| Ip | 1395.00 | NIST | |
| Ip | 1396.00 | NIST | |
| Ip | 1395.00 | NIST | |
| Ip | Outlier 1364.00 | NIST | |
| Ip | 1391.00 | NIST | |
| Ip | 1379.00 | NIST | |
| Ip | 1397.00 | NIST | |
| Ip | 1380.00 | NIST | |
| Ip | 1398.00 | NIST | |
| Ip | 1398.00 | NIST | |
| Ip | 1398.00 | NIST | |
| Ip | 1398.00 | NIST | |
| Ip | 1389.00 | NIST | |
| Ip | 1382.00 | NIST | |
| Ip | 1388.00 | NIST | |
| Ip | 1390.00 | NIST | |
| Ip | 1405.00 | NIST | |
| Ip | 1395.00 | NIST | |
| Ip | 1400.00 | NIST | |
| Ip | 1390.00 | NIST | |
| Ip | 1399.00 | NIST | |
| Ip | 1406.00 | NIST | |
| Ip | 1411.00 | NIST | |
| Ip | 1393.00 | NIST | |
| Ip | 1399.00 | NIST | |
| Ip | 1395.00 | NIST | |
| Ip | 1399.00 | NIST | |
| Ip | 1394.00 | NIST | |
| Ip | 1403.00 | NIST | |
| Ip | 1394.00 | NIST | |
| Ip | 1383.00 | NIST | |
| Ip | 1393.00 | NIST | |
| Ip | 1393.00 | NIST | |
| Ip | 1393.00 | NIST | |
| Ip | 1393.00 | NIST | |
| Ip | 1393.00 | NIST | |
| Ip | 1393.00 | NIST | |
| Ip | 1393.00 | NIST | |
| Ip | 1393.00 | NIST | |
| Ip | 1379.00 | NIST | |
| Ip | 1393.00 | NIST | |
| Ip | 1393.00 | NIST | |
| Ip | 1393.00 | NIST | |
| Ip | 1393.00 | NIST | |
| Ip | 1393.00 | NIST | |
| Ip | 1401.00 | NIST | |
| Ip | 1379.00 | NIST | |
| Ip | 1394.00 | NIST | |
| Ip | 1396.00 | NIST | |
| Ip | 1394.00 | NIST | |
| Ip | 1392.00 | NIST | |
| Ip | 1387.00 | NIST | |
| Ip | 1395.00 | NIST | |
| Ip | 1404.00 | NIST | |
| Ip | 1383.00 | NIST | |
| Ip | 1399.00 | NIST | |
| Ip | 1393.00 | NIST | |
| Ip | 1401.00 | NIST | |
| Ip | Outlier 1368.00 | NIST | |
| Ip | 1411.00 | NIST | |
| Ip | 1391.00 | NIST | |
| Ip | 1398.00 | NIST | |
| Ip | 1388.00 | NIST | |
| Ip | 1390.00 | NIST | |
| Ip | Outlier 1356.00 | NIST | |
| Ip | 1386.00 | NIST | |
| Ip | Outlier 1417.80 | NIST | |
| Tboil | 448.20 | K | NIST |
| Tc | [628.45; 628.50] | K |
|
| Tc | 628.50 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value |
| Tc | 628.50 ± 0.50 | K | NIST |
| Tc | 628.50 | K | NIST |
| Tc | 628.45 ± 0.30 | K | NIST |
| Tfus | [228.15; 235.40] | K |
|
| Tfus | 228.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 235.40 | K | Aq. Solubility Prediction |
| Vc | [0.515; 0.515] | m3/kmol |
|
| Vc | 0.515 | m3/kmol | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value |
| Vc | 0.515 | m3/kmol | NIST |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | 338.50 | J/mol×K | 298.50 | NIST |
| ΔvapH | [54.50; 71.60] | kJ/mol | [300.50; 408.00] |
|
| ΔvapH | 71.60 | kJ/mol | 300.50 | NIST |
| ΔvapH | 64.10 | kJ/mol | 381.50 | NIST |
| ΔvapH | 58.80 | kJ/mol | 399.00 | NIST |
| ΔvapH | 54.50 | kJ/mol | 408.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [187.38; 451.27] | 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 | -7.75000e-01 | |||
| Coefficient B | 8.03740e-01 | |||
| Coefficient C | -4.45000e-04 | |||
| Coefficient D | 9.33000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 187.38 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 232.01 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 272.12 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 308.01 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 339.98 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 368.31 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 393.32 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 415.28 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 434.50 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 451.27 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0851073; 0.0002684] | Pa×s | [231.77; 439.94] |
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 | -1.46357e+01 | |||
| Coefficient B | 2.82113e+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. | 231.77 | |||
| Temperature range, max. | 439.94 | |||
| η | 0.0851073 | Pa×s | 231.77 | Calculated Property |
| η | 0.0282039 | Pa×s | 254.90 | Calculated Property |
| η | 0.0112320 | Pa×s | 278.03 | Calculated Property |
| η | 0.0051526 | Pa×s | 301.16 | Calculated Property |
| η | 0.0026416 | Pa×s | 324.29 | Calculated Property |
| η | 0.0014803 | Pa×s | 347.42 | Calculated Property |
| η | 0.0008917 | Pa×s | 370.55 | Calculated Property |
| η | 0.0005701 | Pa×s | 393.68 | Calculated Property |
| η | 0.0003831 | Pa×s | 416.81 | Calculated Property |
| η | 0.0002684 | Pa×s | 439.94 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [342.20; 467.50] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.68983e+01 | |||
| Coefficient B | -4.80013e+03 | |||
| Coefficient C | -5.32220e+01 | |||
| Temperature range, min. | 342.20 | |||
| Temperature range, max. | 467.50 | |||
| Pvap | 1.33 | kPa | 342.20 | Calculated Property |
| Pvap | 2.86 | kPa | 356.12 | Calculated Property |
| Pvap | 5.74 | kPa | 370.04 | Calculated Property |
| Pvap | 10.86 | kPa | 383.97 | Calculated Property |
| Pvap | 19.52 | kPa | 397.89 | Calculated Property |
| Pvap | 33.52 | kPa | 411.81 | Calculated Property |
| Pvap | 55.28 | kPa | 425.73 | Calculated Property |
| Pvap | 87.94 | kPa | 439.66 | Calculated Property |
| Pvap | 135.46 | kPa | 453.58 | Calculated Property |
| Pvap | 202.67 | kPa | 467.50 | Calculated Property |
| Pvap | [7.61e-03; 2.17] | kPa | [283.00; 353.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.57646e+01 | |||
| Coefficient B | -3.82994e+03 | |||
| Coefficient C | -9.74700e+01 | |||
| Reference | Geiseler, Fruwert, et al., 1966 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 283.00 | |||
| Temperature range, max. | 353.00 | |||
| Pvap | 7.61e-03 | kPa | 283.00 | Calculated Property |
| Pvap | 0.02 | kPa | 290.78 | Calculated Property |
| Pvap | 0.04 | kPa | 298.56 | Calculated Property |
| Pvap | 0.08 | kPa | 306.33 | Calculated Property |
| Pvap | 0.15 | kPa | 314.11 | Calculated Property |
| Pvap | 0.27 | kPa | 321.89 | Calculated Property |
| Pvap | 0.48 | kPa | 329.67 | Calculated Property |
| Pvap | 0.82 | kPa | 337.44 | Calculated Property |
| Pvap | 1.36 | kPa | 345.22 | Calculated Property |
| Pvap | 2.17 | kPa | 353.00 | Calculated Property |
Similar Compounds
Find more compounds similar to (±)-octan-3-ol.
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 4 ChEDL chemicals 1.5.2, from Gude, M.; Teja, A. S. Vapor-Liquid Critical Properties of Elements and Compounds. 4. Aliphatic Alkanols. J. Chem. Eng. Data 1995, 40, 1025-1036.
- Cheméo Relay (1.0)
- Crippen Method
- Vapour pressures and heat capacity measurements on the C7 C9 secondary aliphatic alcohols
- Joback Method
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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