- InChI
- InChI=1S/C10H22O/c1-2-3-4-5-6-7-8-9-10-11/h11H,2-10H2,1H3
- InChI Key
- MWKFXSUHUHTGQN-UHFFFAOYSA-N
- Formula
- C10H22O
- SMILES
- CCCCCCCCCCO
- Molecular Weight1
- 158.28
- CAS
- 112-30-1
- Other Names
-
- 1-Hydroxydecane
- Agent 504
- Alcohol C10
- Alfol 10
- Antak
- C 10 alcohol
- Capric alcohol
- Caprinic alcohol
- Conol 10N
- Decan-1-ol
- Decanol
- Decanol-(1)
- Decyl alcohol
- Decyl, n- alcohol
- Decylic Alcohol
- Dytol S-91
- Epal 10
- Kalcohl 10H
- Lorol 22
- Lorol C10
- NSC 406313
- Nacol 10-99
- Nonylcacarbinol
- Nonylcarbinol
- Primary decyl alcohol
- Royaltac
- Royaltac M-2
- Royaltac-85
- Sipol L10
- T-148
- n-Decan-1-ol
- n-Decanol
- n-Decyl alcohol
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- Tflash,cc : Flash Point (Closed Cup Method) (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).
- 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).
- NFPA Fire : NFPA Fire Rating.
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- ΔvapS : Entropy of vaporization 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).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | [-6619.00; -6593.10] | kJ/mol |
|
| ΔcH°liquid | -6619.00 ± 8.00 | kJ/mol | NIST |
| ΔcH°liquid | -6601.10 ± 1.10 | kJ/mol | NIST |
| ΔcH°liquid | -6599.63 ± 0.75 | kJ/mol | NIST |
| ΔcH°liquid | -6593.30 ± 3.30 | kJ/mol | NIST |
| ΔcH°liquid | -6593.10 | kJ/mol | NIST |
| μ | 1.80 | debye | KDB |
| η | 0.0111922 | Pa×s | Volumet... |
| Tflash,cc | 355.37 | K | KDB |
| ΔfG° | -104.30 | kJ/mol | KDB |
| ΔfH°gas | [-404.60; -387.20] | kJ/mol |
|
| ΔfH°gas | -401.90 | kJ/mol | KDB |
| ΔfH°gas | -387.20 | kJ/mol | NIST |
| ΔfH°gas | -396.60 ± 1.40 | kJ/mol | NIST |
| ΔfH°gas | -388.80 | kJ/mol | NIST |
| ΔfH°gas | -398.20 ± 1.20 | kJ/mol | NIST |
| ΔfH°gas | -395.20 ± 2.40 | kJ/mol | NIST |
| ΔfH°gas | -404.60 ± 3.10 | kJ/mol | NIST |
| ΔfH°liquid | [-486.10; -478.10] | kJ/mol |
|
| ΔfH°liquid | -478.10 ± 1.10 | kJ/mol | NIST |
| ΔfH°liquid | -479.74 ± 0.96 | kJ/mol | NIST |
| ΔfH°liquid | -486.10 ± 3.30 | kJ/mol | NIST |
| ΔfH°liquid | -486.10 ± 3.00 | kJ/mol | NIST |
| ΔfusH° | [31.40; 33.67] | kJ/mol |
|
| ΔfusH° | 33.67 | kJ/mol | Heat Ca... |
| ΔfusH° | 31.40 | kJ/mol | Measure... |
| ΔsubH° | 112.50 ± 6.30 | kJ/mol | NIST |
| ΔvapH° | [77.80; 90.90] | kJ/mol |
|
| ΔvapH° | 81.50 | kJ/mol | NIST |
| ΔvapH° | 80.90 | kJ/mol | NIST |
| ΔvapH° | 81.70 | kJ/mol | NIST |
| ΔvapH° | 79.30 | kJ/mol | NIST |
| ΔvapH° | 81.49 ± 0.78 | kJ/mol | NIST |
| ΔvapH° | 81.50 ± 0.80 | kJ/mol | NIST |
| ΔvapH° | 81.50 ± 0.75 | kJ/mol | NIST |
| ΔvapH° | 81.50 ± 0.80 | kJ/mol | NIST |
| ΔvapH° | 77.80 ± 0.80 | kJ/mol | NIST |
| ΔvapH° | 82.90 ± 2.10 | kJ/mol | NIST |
| ΔvapH° | Outlier 90.90 | kJ/mol | NIST |
| log10WS | [-3.63; -3.63] |
|
|
| log10WS | -3.63 | Aq. Sol... | |
| log10WS | -3.63 | Estimat... | |
| logPoct/wat | 3.119 | Crippen Calculated Property | |
| McVol | 157.630 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| Pc | [2310.00; 2320.00] | kPa |
|
| Pc | 2315.00 | kPa | KDB |
| Pc | 2320.00 ± 50.00 | kPa | NIST |
| Pc | 2310.00 ± 60.00 | kPa | NIST |
| Pc | 2320.00 ± 20.00 | kPa | NIST |
| Pc | 2320.00 ± 20.00 | kPa | NIST |
| Ptriple | 1.00e-04 ± 1.30e-05 | kPa | NIST |
| ρc | [243.75; 264.33] | kg/m3 |
|
| ρc | 243.75 ± 7.91 | kg/m3 | NIST |
| ρc | 264.33 | kg/m3 | NIST |
| ρc | 243.75 ± 6.33 | kg/m3 | NIST |
| ρc | 264.33 ± 3.17 | kg/m3 | NIST |
| Inp | [215.20; 1287.00] |
|
|
| Inp | 1271.19 | NIST | |
| Inp | 1255.70 | NIST | |
| Inp | 1280.00 | NIST | |
| Inp | 1262.00 | NIST | |
| Inp | 1254.00 | NIST | |
| Inp | 1254.00 | NIST | |
| Inp | 1254.00 | NIST | |
| Inp | 1255.00 | NIST | |
| Inp | 1255.00 | NIST | |
| Inp | 1255.00 | NIST | |
| Inp | 1255.00 | NIST | |
| Inp | 1256.00 | NIST | |
| Inp | 1262.00 | NIST | |
| Inp | 1262.00 | NIST | |
| Inp | 1262.00 | NIST | |
| Inp | 1249.00 | NIST | |
| Inp | 1247.00 | NIST | |
| Inp | 1247.00 | NIST | |
| Inp | 1244.00 | NIST | |
| Inp | 1247.00 | NIST | |
| Inp | 1241.00 | NIST | |
| Inp | 1256.00 | NIST | |
| Inp | 1246.00 | NIST | |
| Inp | 1252.00 | NIST | |
| Inp | 1260.00 | NIST | |
| Inp | 1253.00 | NIST | |
| Inp | 1264.00 | NIST | |
| Inp | 1262.00 | NIST | |
| Inp | 1264.00 | NIST | |
| Inp | 1276.00 | NIST | |
| Inp | 1263.00 | NIST | |
| Inp | 1259.00 | NIST | |
| Inp | 1255.00 | NIST | |
| Inp | 1257.00 | NIST | |
| Inp | 1257.00 | NIST | |
| Inp | 1272.00 | NIST | |
| Inp | 1256.00 | NIST | |
| Inp | 1272.00 | NIST | |
| Inp | 1275.00 | NIST | |
| Inp | 1275.00 | NIST | |
| Inp | 1279.00 | NIST | |
| Inp | 1272.00 | NIST | |
| Inp | 1255.20 | NIST | |
| Inp | 1273.80 | NIST | |
| Inp | 1258.00 | NIST | |
| Inp | 1281.00 | NIST | |
| Inp | 1272.00 | NIST | |
| Inp | 1272.00 | NIST | |
| Inp | 1285.00 | NIST | |
| Inp | 1259.00 | NIST | |
| Inp | 1273.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1267.00 | NIST | |
| Inp | 1256.90 | NIST | |
| Inp | 1258.90 | NIST | |
| Inp | 1269.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1282.50 | NIST | |
| Inp | 1264.00 | NIST | |
| Inp | 1254.00 | NIST | |
| Inp | 1259.00 | NIST | |
| Inp | 1271.00 | NIST | |
| Inp | 1269.00 | NIST | |
| Inp | 1267.00 | NIST | |
| Inp | 1267.00 | NIST | |
| Inp | 1273.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1275.00 | NIST | |
| Inp | 1271.00 | NIST | |
| Inp | 1273.00 | NIST | |
| Inp | 1273.00 | NIST | |
| Inp | 1273.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1275.00 | NIST | |
| Inp | 1276.00 | NIST | |
| Inp | 1278.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1263.00 | NIST | |
| Inp | 1278.00 | NIST | |
| Inp | 1272.00 | NIST | |
| Inp | 1272.00 | NIST | |
| Inp | 1255.00 | NIST | |
| Inp | 1255.00 | NIST | |
| Inp | 1270.00 | NIST | |
| Inp | 1270.00 | NIST | |
| Inp | 1275.00 | NIST | |
| Inp | 1275.00 | NIST | |
| Inp | 1272.00 | NIST | |
| Inp | 1270.00 | NIST | |
| Inp | 1272.00 | NIST | |
| Inp | 1263.00 | NIST | |
| Inp | 1266.00 | NIST | |
| Inp | 1272.00 | NIST | |
| Inp | 1266.00 | NIST | |
| Inp | 1269.00 | NIST | |
| Inp | 1254.00 | NIST | |
| Inp | 1263.00 | NIST | |
| Inp | 1257.00 | NIST | |
| Inp | 1255.00 | NIST | |
| Inp | 1266.00 | NIST | |
| Inp | 1275.00 | NIST | |
| Inp | 1279.00 | NIST | |
| Inp | 1283.00 | NIST | |
| Inp | 1259.00 | NIST | |
| Inp | 1279.00 | NIST | |
| Inp | 1281.00 | NIST | |
| Inp | 1285.00 | NIST | |
| Inp | 1261.00 | NIST | |
| Inp | 1269.00 | NIST | |
| Inp | 1263.00 | NIST | |
| Inp | 1272.00 | NIST | |
| Inp | 1272.00 | NIST | |
| Inp | 1287.00 | NIST | |
| Inp | 1270.00 | NIST | |
| Inp | 1281.00 | NIST | |
| Inp | 1284.00 | NIST | |
| Inp | 1287.00 | NIST | |
| Inp | 1261.00 | NIST | |
| Inp | 1269.00 | NIST | |
| Inp | 1272.00 | NIST | |
| Inp | 1264.00 | NIST | |
| Inp | 1263.00 | NIST | |
| Inp | 1256.00 | NIST | |
| Inp | 1272.10 | NIST | |
| Inp | 1259.00 | NIST | |
| Inp | 1259.00 | NIST | |
| Inp | 1257.00 | NIST | |
| Inp | 1257.00 | NIST | |
| Inp | 1263.00 | NIST | |
| Inp | 1283.00 | NIST | |
| Inp | 1257.00 | NIST | |
| Inp | 1249.00 | NIST | |
| Inp | 1261.00 | NIST | |
| Inp | Outlier 215.20 | NIST | |
| Inp | Outlier 216.62 | NIST | |
| Inp | Outlier 216.09 | NIST | |
| Inp | 1259.00 | NIST | |
| Inp | 1266.00 | NIST | |
| Inp | 1279.00 | NIST | |
| Inp | 1263.00 | NIST | |
| Inp | 1281.00 | NIST | |
| Inp | 1272.00 | NIST | |
| Inp | 1283.00 | NIST | |
| Inp | Outlier 215.20 | NIST | |
| Inp | 1273.00 | NIST | |
| Inp | 1269.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1271.00 | NIST | |
| Inp | 1271.19 | NIST | |
| Inp | 1254.00 | NIST | |
| Inp | 1255.00 | NIST | |
| Inp | 1249.00 | NIST | |
| Inp | 1241.00 | NIST | |
| Inp | 1253.00 | NIST | |
| I | [1714.00; 1783.00] |
|
|
| I | 1724.00 | NIST | |
| I | 1769.00 | NIST | |
| I | 1746.00 | NIST | |
| I | 1726.00 | NIST | |
| I | 1760.00 | NIST | |
| I | 1759.00 | NIST | |
| I | 1753.00 | NIST | |
| I | 1764.00 | NIST | |
| I | 1783.00 | NIST | |
| I | 1750.00 | NIST | |
| I | 1740.00 | NIST | |
| I | 1732.00 | NIST | |
| I | 1736.00 | NIST | |
| I | 1740.00 | NIST | |
| I | 1757.00 | NIST | |
| I | 1757.00 | NIST | |
| I | 1769.00 | NIST | |
| I | 1759.00 | NIST | |
| I | 1763.00 | NIST | |
| I | 1767.00 | NIST | |
| I | 1760.00 | NIST | |
| I | 1771.00 | NIST | |
| I | Outlier 1714.00 | NIST | |
| I | 1763.00 | NIST | |
| I | 1748.00 | NIST | |
| I | 1744.00 | NIST | |
| I | 1745.00 | NIST | |
| I | 1748.00 | NIST | |
| I | 1748.00 | NIST | |
| I | 1735.00 | NIST | |
| I | 1735.00 | NIST | |
| I | 1763.00 | NIST | |
| I | 1764.90 | NIST | |
| I | 1770.00 | NIST | |
| I | 1765.00 | NIST | |
| I | 1770.00 | NIST | |
| I | 1752.00 | NIST | |
| I | 1751.00 | NIST | |
| I | 1726.00 | NIST | |
| I | 1756.00 | NIST | |
| I | 1729.00 | NIST | |
| I | 1767.00 | NIST | |
| I | 1761.00 | NIST | |
| I | 1764.00 | NIST | |
| I | 1760.00 | NIST | |
| I | 1767.00 | NIST | |
| I | 1778.00 | NIST | |
| I | 1768.00 | NIST | |
| I | 1769.00 | NIST | |
| I | 1783.00 | NIST | |
| I | Outlier 1723.00 | NIST | |
| I | 1766.00 | NIST | |
| I | 1766.00 | NIST | |
| I | 1753.00 | NIST | |
| I | 1778.00 | NIST | |
| I | 1781.00 | NIST | |
| I | 1752.00 | NIST | |
| I | 1752.00 | NIST | |
| I | 1781.00 | NIST | |
| I | 1781.00 | NIST | |
| I | 1765.00 | NIST | |
| I | 1781.00 | NIST | |
| I | 1750.00 | NIST | |
| I | 1766.00 | NIST | |
| I | 1766.00 | NIST | |
| I | 1735.00 | NIST | |
| I | 1752.00 | NIST | |
| I | 1767.00 | NIST | |
| I | 1748.00 | NIST | |
| I | 1735.00 | NIST | |
| I | 1765.00 | NIST | |
| I | 1757.00 | NIST | |
| I | 1756.00 | NIST | |
| I | 1760.00 | NIST | |
| I | 1783.00 | NIST | |
| I | 1724.00 | NIST | |
| I | 1759.00 | NIST | |
| I | 1740.00 | NIST | |
| Tboil | [502.95; 504.20] | K |
|
| Tboil | 504.20 | K | KDB |
| Tboil | 503.70 | K | Phase e... |
| Tboil | 503.70 | K | (Liquid... |
| Tboil | 503.70 | K | (Liquid... |
| Tboil | 502.95 | K | Study o... |
| Tc | [687.00; 708.00] | K |
|
| Tc | 687.30 | K | KDB |
| Tc | 687.00 ± 1.00 | K | NIST |
| Tc | 687.70 ± 1.00 | K | NIST |
| Tc | 687.00 ± 0.70 | K | NIST |
| Tc | 687.00 ± 0.60 | K | NIST |
| Tc | 687.10 | K | NIST |
| Tc | 687.30 ± 1.30 | K | NIST |
| Tc | 687.00 | K | NIST |
| Tc | Outlier 708.00 ± 2.00 | K | NIST |
| Tfus | [276.15; 280.51] | K |
|
| Tfus | 279.87 | K | Aq. Sol... |
| Tfus | 280.00 | K | KDB |
| Tfus | 280.15 | K | Experim... |
| Tfus | 280.19 | K | SLE and... |
| Tfus | 280.10 | K | (Solid ... |
| Tfus | 278.20 | K | Phase e... |
| Tfus | Outlier 276.15 | K | The man... |
| Tfus | 278.67 | K | Experim... |
| Tfus | 280.51 | K | Phase E... |
| Tfus | 280.19 | K | Solid-L... |
| Tfus | 279.60 ± 0.50 | K | NIST |
| Tfus | 280.05 ± 0.40 | K | NIST |
| Tfus | 277.00 ± 3.00 | K | NIST |
| Ttriple | [275.64; 279.65] | K |
|
| Ttriple | 275.64 | K | Solid-l... |
| Ttriple | 279.65 ± 1.00 | K | NIST |
| Vc | [0.649; 0.649] | m3/kmol |
|
| Vc | 0.649 | m3/kmol | KDB |
| Vc | 0.649 | m3/kmol | NIST |
| Zc | 0.2629130 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [380.60; 452.73] | J/mol×K | [520.38; 678.87] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 380 390 400 410 420 430 440 450 550 600 650 | ||||
| Cp,gas | 380.60 | J/mol×K | 520.38 | Joback Calculated Property |
| Cp,gas | 393.83 | J/mol×K | 546.79 | Joback Calculated Property |
| Cp,gas | 406.56 | J/mol×K | 573.21 | Joback Calculated Property |
| Cp,gas | 418.80 | J/mol×K | 599.62 | Joback Calculated Property |
| Cp,gas | 430.56 | J/mol×K | 626.04 | Joback Calculated Property |
| Cp,gas | 441.87 | J/mol×K | 652.45 | Joback Calculated Property |
| Cp,gas | 452.73 | J/mol×K | 678.87 | Joback Calculated Property |
| Cp,liquid | [369.96; 387.80] | J/mol×K | [298.15; 305.79] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 370 375 380 385 298 300 302 304 | ||||
| Cp,liquid | 372.98 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 369.96 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 377.00 | J/mol×K | 301.00 | NIST |
| Cp,liquid | 377.30 | J/mol×K | 303.15 | NIST |
| Cp,liquid | 387.80 | J/mol×K | 304.05 | NIST |
| Cp,liquid | 377.80 | J/mol×K | 305.79 | NIST |
| η | [0.0023990; 0.0220640] | Pa×s | [283.15; 348.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 5.00e-3 0.01 0.02 0.02 300 320 340 | ||||
| η | 0.0220640 | Pa×s | 283.15 | Density... |
| η | 0.0220640 | Pa×s | 283.15 | Measure... |
| η | 0.0179880 | Pa×s | 288.15 | Measure... |
| η | 0.0144990 | Pa×s | 293.15 | Density... |
| η | 0.0143870 | Pa×s | 293.15 | Measure... |
| η | 0.0110900 | Pa×s | 298.15 | Density... |
| η | 0.0114710 | Pa×s | 298.15 | Density... |
| η | 0.0118250 | Pa×s | 298.15 | Acousti... |
| η | 0.0117350 | Pa×s | 298.15 | Measure... |
| η | 0.0103000 | Pa×s | 300.00 | Tempera... |
| η | 0.0095610 | Pa×s | 303.15 | Measure... |
| η | 0.0097540 | Pa×s | 303.15 | Acousti... |
| η | 0.0097150 | Pa×s | 303.15 | Densiti... |
| η | 0.0097160 | Pa×s | 303.15 | Densiti... |
| η | 0.0096100 | Pa×s | 303.15 | Density... |
| η | 0.0080000 | Pa×s | 308.15 | Measure... |
| η | 0.0081350 | Pa×s | 308.15 | Acousti... |
| η | 0.0076320 | Pa×s | 308.15 | Density... |
| η | 0.0070900 | Pa×s | 310.00 | Tempera... |
| η | 0.0069000 | Pa×s | 313.15 | Density... |
| η | 0.0068420 | Pa×s | 313.15 | Acousti... |
| η | 0.0068190 | Pa×s | 313.15 | Densiti... |
| η | 0.0068310 | Pa×s | 313.15 | Measure... |
| η | 0.0068200 | Pa×s | 313.15 | Densiti... |
| η | 0.0053750 | Pa×s | 318.15 | Density... |
| η | 0.0050000 | Pa×s | 320.00 | Tempera... |
| η | 0.0039280 | Pa×s | 328.15 | Density... |
| η | 0.0036700 | Pa×s | 330.00 | Tempera... |
| η | 0.0029640 | Pa×s | 338.15 | Density... |
| η | 0.0027400 | Pa×s | 340.00 | Tempera... |
| η | 0.0023990 | Pa×s | 348.15 | Density... |
| ΔfusH | [33.67; 37.66] | kJ/mol | [280.00; 280.10] |
|
| ΔfusH | 33.67 | kJ/mol | 280.00 | NIST |
| ΔfusH | 37.66 | kJ/mol | 280.10 | NIST |
| ΔfusH | 37.66 | kJ/mol | 280.10 | NIST |
| ΔsubH | 115.50 ± 6.30 | kJ/mol | 268.50 | NIST |
| ΔvapH | [50.21; 81.10] | kJ/mol | [304.00; 504.10] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 50 55 60 65 70 75 80 300 400 500 | ||||
| ΔvapH | 79.50 | kJ/mol | 304.00 | NIST |
| ΔvapH | 77.60 | kJ/mol | 311.50 | NIST |
| ΔvapH | 77.60 | kJ/mol | 311.50 | NIST |
| ΔvapH | 78.20 ± 0.80 | kJ/mol | 323.00 | NIST |
| ΔvapH | 78.18 | kJ/mol | 323.15 | NIST |
| ΔvapH | 81.10 | kJ/mol | 328.00 | NIST |
| ΔvapH | 75.40 | kJ/mol | 335.50 | NIST |
| ΔvapH | 71.60 | kJ/mol | 379.50 | NIST |
| ΔvapH | 69.60 | kJ/mol | 412.50 | NIST |
| ΔvapH | 69.50 | kJ/mol | 441.00 | NIST |
| ΔvapH | 62.60 | kJ/mol | 466.50 | NIST |
| ΔvapH | 53.90 | kJ/mol | 501.50 | NIST |
| ΔvapH | 50.21 | kJ/mol | 504.10 | KDB |
| Pvap | [1.00e-03; 94.90] | kPa | [308.15; 501.05] |
|
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 350 400 450 500 | ||||
| Pvap | 1.00e-03 | kPa | 308.15 | Vapor L... |
| Pvap | 4.00e-03 | kPa | 313.15 | Isother... |
| Pvap | 4.00e-03 | kPa | 313.15 | Vapor L... |
| Pvap | 7.00e-03 | kPa | 318.15 | Isother... |
| Pvap | 7.00e-03 | kPa | 318.15 | Vapor L... |
| Pvap | 0.01 | kPa | 323.15 | Isother... |
| Pvap | 0.01 | kPa | 323.15 | Vapor L... |
| Pvap | 13.32 | kPa | 436.56 | Isobari... |
| Pvap | 40.00 | kPa | 469.23 | Low-Pre... |
| Pvap | 39.99 | kPa | 469.52 | Isobari... |
| Pvap | 40.03 | kPa | 469.83 | Low-Pre... |
| Pvap | 44.40 | kPa | 472.98 | Low-Pre... |
| Pvap | 47.97 | kPa | 475.40 | Low-Pre... |
| Pvap | 50.19 | kPa | 476.80 | Low-Pre... |
| Pvap | 54.07 | kPa | 479.42 | Low-Pre... |
| Pvap | 57.04 | kPa | 481.36 | Low-Pre... |
| Pvap | 61.26 | kPa | 484.05 | Low-Pre... |
| Pvap | 66.66 | kPa | 487.85 | Isobari... |
| Pvap | 67.43 | kPa | 487.90 | Low-Pre... |
| Pvap | 73.44 | kPa | 491.16 | Low-Pre... |
| Pvap | 76.32 | kPa | 492.56 | Low-Pre... |
| Pvap | 79.92 | kPa | 494.46 | Low-Pre... |
| Pvap | 85.24 | kPa | 496.88 | Low-Pre... |
| Pvap | 94.90 | kPa | 501.05 | Isobari... |
| n0 | [1.43050; 1.43706] | [293.15; 308.15] |
|
|
|
T(K) Refractive Index 1.43 1.43 1.43 1.43 1.43 1.44 1.44 1.44 295 300 305 | ||||
| n0 | 1.43706 | 293.15 | Densiti... | |
| n0 | 1.43700 | 293.15 | Effect ... | |
| n0 | 1.43706 | 293.15 | Excess ... | |
| n0 | 1.43694 | 293.15 | Densiti... | |
| n0 | 1.43456 | 298.15 | Densiti... | |
| n0 | 1.43460 | 298.15 | Densiti... | |
| n0 | 1.43436 | 298.15 | Liquid ... | |
| n0 | 1.43440 | 298.20 | Tie-lin... | |
| n0 | 1.43490 | 298.20 | Solubil... | |
| n0 | 1.43440 | 298.20 | Ternary... | |
| n0 | 1.43302 | 303.15 | Densiti... | |
| n0 | 1.43364 | 303.15 | Densiti... | |
| n0 | 1.43260 | 303.15 | Densiti... | |
| n0 | 1.43256 | 303.15 | Densiti... | |
| n0 | 1.43266 | 303.15 | Densiti... | |
| n0 | 1.43050 | 308.15 | Densiti... | |
| n0 | 1.43050 | 308.15 | Densiti... | |
| ρl | [780.34; 836.51] | kg/m3 | [283.15; 363.15] |
|
|
T(K) Liquid Density (kg/m3) 780 790 800 810 820 830 840 300 320 340 360 | ||||
| ρl | 836.51 | kg/m3 | 283.15 | Densiti... |
| ρl | 833.14 | kg/m3 | 288.15 | Densiti... |
| ρl | 830.00 | kg/m3 | 293.00 | KDB |
| ρl | 829.50 | kg/m3 | 293.15 | Investi... |
| ρl | 829.99 | kg/m3 | 293.15 | Thermop... |
| ρl | 829.76 | kg/m3 | 293.15 | Densiti... |
| ρl | 829.97 | kg/m3 | 293.15 | Thermod... |
| ρl | 829.95 | kg/m3 | 293.15 | Thermod... |
| ρl | 829.76 | kg/m3 | 293.15 | Speeds ... |
| ρl | 829.50 | kg/m3 | 293.15 | Correla... |
| ρl | 826.58 | kg/m3 | 298.15 | Thermod... |
| ρl | 826.36 | kg/m3 | 298.15 | Volumet... |
| ρl | 826.10 | kg/m3 | 298.15 | Correla... |
| ρl | 826.10 | kg/m3 | 298.15 | Investi... |
| ρl | 826.49 | kg/m3 | 298.15 | Thermod... |
| ρl | 826.90 | kg/m3 | 298.15 | Viscosi... |
| ρl | 826.37 | kg/m3 | 298.15 | Speeds ... |
| ρl | 826.41 | kg/m3 | 298.15 | Densiti... |
| ρl | 826.95 | kg/m3 | 298.15 | Thermod... |
| ρl | 826.58 | kg/m3 | 298.15 | Thermod... |
| ρl | 826.56 | kg/m3 | 298.15 | Physico... |
| ρl | 827.21 | kg/m3 | 298.15 | Thermod... |
| ρl | 826.38 | kg/m3 | 298.15 | Densiti... |
| ρl | 826.47 | kg/m3 | 298.15 | Studies... |
| ρl | 826.38 | kg/m3 | 298.15 | Phase b... |
| ρl | 826.64 | kg/m3 | 298.15 | Experim... |
| ρl | 826.38 | kg/m3 | 298.15 | Phase b... |
| ρl | 826.31 | kg/m3 | 298.15 | Excess ... |
| ρl | 826.74 | kg/m3 | 298.15 | Effect ... |
| ρl | 826.41 | kg/m3 | 298.20 | Optimiz... |
| ρl | 826.86 | kg/m3 | 298.20 | Experim... |
| ρl | 822.95 | kg/m3 | 303.15 | Speeds ... |
| ρl | 822.88 | kg/m3 | 303.15 | Volumet... |
| ρl | 822.89 | kg/m3 | 303.15 | Effect ... |
| ρl | 822.95 | kg/m3 | 303.15 | Excess ... |
| ρl | 822.70 | kg/m3 | 303.15 | Correla... |
| ρl | 822.70 | kg/m3 | 303.15 | Investi... |
| ρl | 823.76 | kg/m3 | 303.15 | Thermod... |
| ρl | 822.98 | kg/m3 | 303.15 | Densiti... |
| ρl | 823.13 | kg/m3 | 303.15 | Thermod... |
| ρl | 823.15 | kg/m3 | 303.15 | Thermod... |
| ρl | 819.57 | kg/m3 | 308.15 | Speeds ... |
| ρl | 820.31 | kg/m3 | 308.15 | Thermod... |
| ρl | 819.43 | kg/m3 | 308.15 | Volumet... |
| ρl | 819.30 | kg/m3 | 308.15 | Correla... |
| ρl | 819.30 | kg/m3 | 308.15 | Investi... |
| ρl | 820.00 | kg/m3 | 308.15 | Viscosi... |
| ρl | 819.51 | kg/m3 | 308.15 | Effect ... |
| ρl | 819.57 | kg/m3 | 308.15 | Densiti... |
| ρl | 815.95 | kg/m3 | 313.15 | Effect ... |
| ρl | 816.12 | kg/m3 | 313.15 | Speeds ... |
| ρl | 815.97 | kg/m3 | 313.15 | Volumet... |
| ρl | 816.15 | kg/m3 | 313.15 | Densiti... |
| ρl | 816.83 | kg/m3 | 313.15 | Thermod... |
| ρl | 815.80 | kg/m3 | 313.15 | Correla... |
| ρl | 815.80 | kg/m3 | 313.15 | Investi... |
| ρl | 813.34 | kg/m3 | 318.15 | Thermod... |
| ρl | 812.40 | kg/m3 | 318.15 | Correla... |
| ρl | 812.49 | kg/m3 | 318.15 | Volumet... |
| ρl | 812.63 | kg/m3 | 318.15 | Speeds ... |
| ρl | 812.40 | kg/m3 | 318.15 | Investi... |
| ρl | 812.71 | kg/m3 | 318.15 | Densiti... |
| ρl | 813.00 | kg/m3 | 318.15 | Viscosi... |
| ρl | 809.03 | kg/m3 | 323.15 | Volumet... |
| ρl | 809.24 | kg/m3 | 323.15 | Densiti... |
| ρl | 808.90 | kg/m3 | 323.15 | Investi... |
| ρl | 808.90 | kg/m3 | 323.15 | Correla... |
| ρl | 809.82 | kg/m3 | 323.15 | Thermod... |
| ρl | 806.00 | kg/m3 | 328.15 | Viscosi... |
| ρl | 805.74 | kg/m3 | 328.15 | Densiti... |
| ρl | 802.21 | kg/m3 | 333.15 | Densiti... |
| ρl | 798.65 | kg/m3 | 338.15 | Densiti... |
| ρl | 798.90 | kg/m3 | 338.15 | Viscosi... |
| ρl | 795.06 | kg/m3 | 343.15 | Densiti... |
| ρl | 791.43 | kg/m3 | 348.15 | Densiti... |
| ρl | 787.77 | kg/m3 | 353.15 | Densiti... |
| ρl | 784.07 | kg/m3 | 358.15 | Densiti... |
| ρl | 780.34 | kg/m3 | 363.15 | Densiti... |
| csound,fluid | [1311.69; 1410.60] | m/s | [288.15; 318.18] |
|
|
T(K) Speed of sound in fluid (m/s) 1320 1340 1360 1380 1400 1420 290 300 310 | ||||
| csound,fluid | 1410.60 | m/s | 288.15 | Ultraso... |
| csound,fluid | 1397.23 | m/s | 293.10 | Excess ... |
| csound,fluid | 1393.60 | m/s | 293.15 | Ultraso... |
| csound,fluid | 1396.65 | m/s | 293.15 | Thermod... |
| csound,fluid | 1396.00 | m/s | 293.15 | Densiti... |
| csound,fluid | 1379.96 | m/s | 298.07 | Excess ... |
| csound,fluid | 1379.43 | m/s | 298.15 | Thermod... |
| csound,fluid | 1380.58 | m/s | 298.15 | Micella... |
| csound,fluid | 1377.30 | m/s | 298.15 | Ultraso... |
| csound,fluid | 1362.82 | m/s | 303.04 | Excess ... |
| csound,fluid | 1359.80 | m/s | 303.15 | Ultraso... |
| csound,fluid | 1362.00 | m/s | 303.15 | Densiti... |
| csound,fluid | 1363.52 | m/s | 303.15 | Micella... |
| csound,fluid | 1362.40 | m/s | 303.15 | Thermod... |
| csound,fluid | 1345.82 | m/s | 308.04 | Excess ... |
| csound,fluid | 1345.70 | m/s | 308.15 | Ultraso... |
| csound,fluid | 1345.62 | m/s | 308.15 | Thermod... |
| csound,fluid | 1346.58 | m/s | 308.15 | Micella... |
| csound,fluid | 1329.03 | m/s | 313.01 | Excess ... |
| csound,fluid | 1329.07 | m/s | 313.15 | Thermod... |
| csound,fluid | 1326.70 | m/s | 313.15 | Ultraso... |
| csound,fluid | 1329.00 | m/s | 313.15 | Densiti... |
| csound,fluid | 1312.10 | m/s | 318.15 | Ultraso... |
| csound,fluid | 1311.69 | m/s | 318.18 | Excess ... |
| γ | 0.03 | N/m | 293.20 | KDB |
| ΔvapS | 241.93 | J/mol×K | 323.15 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 380.70 | K | 0.90 | NIST |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 2000.00 | 0.0113 |
| 298.15 | 3990.00 | 0.0115 |
| 298.15 | 6010.00 | 0.0118 |
| 298.15 | 8010.00 | 0.0121 |
| 298.15 | 10010.00 | 0.0123 |
| 298.15 | 13010.00 | 0.0127 |
| 298.15 | 16010.00 | 0.0132 |
| 298.15 | 19010.00 | 0.0136 |
| 298.15 | 22010.00 | 0.0140 |
| 298.15 | 25000.00 | 0.0145 |
| 298.15 | 28000.00 | 0.0149 |
| 298.15 | 29990.00 | 0.0152 |
| 303.15 | 1990.00 | 0.0089 |
| 303.15 | 4000.00 | 0.0091 |
| 303.15 | 5980.00 | 0.0093 |
| 303.15 | 8010.00 | 0.0096 |
| 303.15 | 10020.00 | 0.0098 |
| 303.15 | 12980.00 | 0.0101 |
| 303.15 | 15970.00 | 0.0104 |
| 303.15 | 19020.00 | 0.0108 |
| 303.15 | 22000.00 | 0.0111 |
| 303.15 | 24980.00 | 0.0114 |
| 303.15 | 27980.00 | 0.0118 |
| 303.15 | 30010.00 | 0.0120 |
| 313.15 | 2030.00 | 0.0062 |
| 313.15 | 4020.00 | 0.0064 |
| 313.15 | 6000.00 | 0.0065 |
| 313.15 | 7980.00 | 0.0067 |
| 313.15 | 9980.00 | 0.0068 |
| 313.15 | 12990.00 | 0.0071 |
| 313.15 | 15990.00 | 0.0073 |
| 313.15 | 18990.00 | 0.0075 |
| 313.15 | 22010.00 | 0.0078 |
| 313.15 | 25020.00 | 0.0080 |
| 313.15 | 28020.00 | 0.0082 |
| 313.15 | 29980.00 | 0.0084 |
| 323.15 | 2000.00 | 0.0047 |
| 323.15 | 4010.00 | 0.0049 |
| 323.15 | 6010.00 | 0.0050 |
| 323.15 | 8010.00 | 0.0051 |
| 323.15 | 9990.00 | 0.0052 |
| 323.15 | 13010.00 | 0.0054 |
| 323.15 | 16010.00 | 0.0055 |
| 323.15 | 19020.00 | 0.0057 |
| 323.15 | 22020.00 | 0.0059 |
| 323.15 | 25010.00 | 0.0061 |
| 323.15 | 28000.00 | 0.0062 |
| 323.15 | 30010.00 | 0.0064 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 826.1 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 100.00 | 832.3 |
| 288.15 | 1000.00 | 832.8 |
| 288.15 | 5000.00 | 835.2 |
| 288.15 | 10000.00 | 838.0 |
| 288.15 | 15000.00 | 840.8 |
| 288.15 | 20000.00 | 843.5 |
| 288.15 | 25000.00 | 846.1 |
| 288.15 | 30000.00 | 848.6 |
| 288.15 | 35000.00 | 851.1 |
| 288.15 | 40000.00 | 853.5 |
| 288.15 | 45000.00 | 855.9 |
| 288.15 | 50000.00 | 858.2 |
| 288.15 | 55000.00 | 860.4 |
| 288.15 | 60000.00 | 862.7 |
| 298.15 | 100.00 | 825.5 |
| 298.15 | 1000.00 | 826.0 |
| 298.15 | 5000.00 | 828.5 |
| 298.15 | 10000.00 | 831.5 |
| 298.15 | 15000.00 | 834.4 |
| 298.15 | 20000.00 | 837.2 |
| 298.15 | 25000.00 | 839.8 |
| 298.15 | 30000.00 | 842.5 |
| 298.15 | 35000.00 | 845.1 |
| 298.15 | 40000.00 | 847.6 |
| 298.15 | 45000.00 | 850.0 |
| 298.15 | 50000.00 | 852.4 |
| 298.15 | 55000.00 | 854.7 |
| 298.15 | 60000.00 | 856.8 |
| 308.15 | 100.00 | 818.7 |
| 308.15 | 1000.00 | 819.3 |
| 308.15 | 5000.00 | 821.9 |
| 308.15 | 10000.00 | 825.0 |
| 308.15 | 15000.00 | 828.0 |
| 308.15 | 20000.00 | 830.9 |
| 308.15 | 25000.00 | 833.7 |
| 308.15 | 30000.00 | 836.4 |
| 308.15 | 35000.00 | 839.1 |
| 308.15 | 40000.00 | 841.7 |
| 308.15 | 45000.00 | 844.2 |
| 308.15 | 50000.00 | 846.6 |
| 308.15 | 55000.00 | 849.0 |
| 308.15 | 60000.00 | 851.2 |
| 318.15 | 100.00 | 811.9 |
| 318.15 | 1000.00 | 812.5 |
| 318.15 | 5000.00 | 815.3 |
| 318.15 | 10000.00 | 818.5 |
| 318.15 | 15000.00 | 821.7 |
| 318.15 | 20000.00 | 824.7 |
| 318.15 | 25000.00 | 827.6 |
| 318.15 | 30000.00 | 830.4 |
| 318.15 | 35000.00 | 833.2 |
| 318.15 | 40000.00 | 835.8 |
| 318.15 | 45000.00 | 838.5 |
| 318.15 | 50000.00 | 841.0 |
| 318.15 | 55000.00 | 843.4 |
| 318.15 | 60000.00 | 845.7 |
| 328.15 | 100.00 | 805.0 |
| 328.15 | 1000.00 | 805.7 |
| 328.15 | 5000.00 | 808.5 |
| 328.15 | 10000.00 | 811.9 |
| 328.15 | 15000.00 | 815.2 |
| 328.15 | 20000.00 | 818.3 |
| 328.15 | 25000.00 | 821.4 |
| 328.15 | 30000.00 | 824.3 |
| 328.15 | 35000.00 | 827.1 |
| 328.15 | 40000.00 | 829.9 |
| 328.15 | 45000.00 | 832.6 |
| 328.15 | 50000.00 | 835.2 |
| 328.15 | 55000.00 | 837.7 |
| 328.15 | 60000.00 | 840.2 |
| 338.15 | 100.00 | 798.0 |
| 338.15 | 1000.00 | 798.7 |
| 338.15 | 5000.00 | 801.7 |
| 338.15 | 10000.00 | 805.2 |
| 338.15 | 15000.00 | 808.7 |
| 338.15 | 20000.00 | 812.0 |
| 338.15 | 25000.00 | 815.1 |
| 338.15 | 30000.00 | 818.1 |
| 338.15 | 35000.00 | 821.1 |
| 338.15 | 40000.00 | 824.0 |
| 338.15 | 45000.00 | 826.7 |
| 338.15 | 50000.00 | 829.4 |
| 338.15 | 55000.00 | 832.1 |
| 338.15 | 60000.00 | 834.5 |
| 348.15 | 100.00 | 790.9 |
| 348.15 | 1000.00 | 791.6 |
| 348.15 | 5000.00 | 794.8 |
| 348.15 | 10000.00 | 798.5 |
| 348.15 | 15000.00 | 802.0 |
| 348.15 | 20000.00 | 805.5 |
| 348.15 | 25000.00 | 808.8 |
| 348.15 | 30000.00 | 811.9 |
| 348.15 | 35000.00 | 815.0 |
| 348.15 | 40000.00 | 817.9 |
| 348.15 | 45000.00 | 820.8 |
| 348.15 | 50000.00 | 823.6 |
| 348.15 | 55000.00 | 826.4 |
| 348.15 | 60000.00 | 829.0 |
| 358.15 | 100.00 | 783.6 |
| 358.15 | 1000.00 | 784.3 |
| 358.15 | 5000.00 | 787.6 |
| 358.15 | 10000.00 | 791.6 |
| 358.15 | 15000.00 | 795.3 |
| 358.15 | 20000.00 | 798.9 |
| 358.15 | 25000.00 | 802.3 |
| 358.15 | 30000.00 | 805.6 |
| 358.15 | 35000.00 | 808.8 |
| 358.15 | 40000.00 | 811.9 |
| 358.15 | 45000.00 | 814.8 |
| 358.15 | 50000.00 | 817.7 |
| 358.15 | 55000.00 | 820.5 |
| 358.15 | 60000.00 | 822.9 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 826.1 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 313.12 | 1025.00 | 816.79 |
| 313.12 | 2002.00 | 817.46 |
| 313.12 | 2995.00 | 817.98 |
| 313.12 | 4013.00 | 818.58 |
| 313.12 | 5004.00 | 819.21 |
| 313.12 | 5994.00 | 819.86 |
| 313.12 | 7003.00 | 820.47 |
| 313.12 | 7997.00 | 821.19 |
| 313.12 | 9000.00 | 821.73 |
| 313.12 | 9994.00 | 822.38 |
| 313.12 | 10995.00 | 823.02 |
| 313.12 | 11995.00 | 823.67 |
| 313.12 | 12997.00 | 824.2 |
| 313.12 | 13996.00 | 824.82 |
| 313.12 | 14998.00 | 825.42 |
| 313.12 | 15990.00 | 826.01 |
| 313.12 | 16995.00 | 826.61 |
| 313.12 | 17986.00 | 827.14 |
| 313.12 | 18992.00 | 827.76 |
| 313.12 | 19993.00 | 828.31 |
| 313.12 | 20999.00 | 828.88 |
| 313.12 | 21509.00 | 829.19 |
| 323.09 | 1002.00 | 809.87 |
| 323.09 | 2011.00 | 810.59 |
| 323.09 | 3019.00 | 811.21 |
| 323.09 | 4014.00 | 811.83 |
| 323.09 | 5006.00 | 812.47 |
| 323.09 | 6012.00 | 813.18 |
| 323.09 | 7002.00 | 813.8 |
| 323.09 | 8003.00 | 814.42 |
| 323.09 | 9008.00 | 815.1 |
| 323.09 | 10006.00 | 815.7 |
| 323.09 | 11000.00 | 816.38 |
| 323.09 | 12002.00 | 816.97 |
| 323.09 | 13002.00 | 817.64 |
| 323.09 | 14000.00 | 818.21 |
| 323.09 | 15017.00 | 818.84 |
| 323.09 | 16003.00 | 819.4 |
| 323.09 | 17015.00 | 820.02 |
| 323.09 | 18006.00 | 820.61 |
| 323.09 | 19007.00 | 821.24 |
| 323.09 | 20007.00 | 821.84 |
| 323.09 | 21002.00 | 822.41 |
| 323.09 | 22014.00 | 823.01 |
| 333.04 | 1046.00 | 802.82 |
| 333.04 | 2018.00 | 803.5 |
| 333.04 | 3008.00 | 804.21 |
| 333.04 | 4012.00 | 804.88 |
| 333.04 | 5059.00 | 805.62 |
| 333.04 | 6016.00 | 806.29 |
| 333.04 | 7022.00 | 807.0 |
| 333.04 | 8014.00 | 807.64 |
| 333.04 | 9015.00 | 808.34 |
| 333.04 | 10015.00 | 808.97 |
| 333.04 | 11019.00 | 809.64 |
| 333.04 | 12007.00 | 810.31 |
| 333.04 | 13019.00 | 810.96 |
| 333.04 | 14019.00 | 811.6 |
| 333.04 | 15014.00 | 812.24 |
| 333.04 | 16021.00 | 812.88 |
| 333.04 | 17026.00 | 813.5 |
| 333.04 | 18023.00 | 814.11 |
| 333.04 | 19018.00 | 814.72 |
| 333.04 | 20025.00 | 815.35 |
| 333.04 | 21020.00 | 815.94 |
| 333.04 | 22032.00 | 816.58 |
| 342.98 | 1058.00 | 795.63 |
| 342.98 | 2045.00 | 796.4 |
| 342.98 | 3022.00 | 797.12 |
| 342.98 | 4035.00 | 797.9 |
| 342.98 | 5028.00 | 798.63 |
| 342.98 | 6030.00 | 799.37 |
| 342.98 | 7023.00 | 800.07 |
| 342.98 | 8028.00 | 800.78 |
| 342.98 | 9062.00 | 801.51 |
| 342.98 | 10035.00 | 802.22 |
| 342.98 | 11029.00 | 802.92 |
| 342.98 | 12064.00 | 803.64 |
| 342.98 | 13023.00 | 804.31 |
| 342.98 | 14042.00 | 805.0 |
| 342.98 | 15022.00 | 805.66 |
| 342.98 | 16022.00 | 806.36 |
| 342.98 | 17021.00 | 807.0 |
| 342.98 | 18034.00 | 807.7 |
| 342.98 | 19025.00 | 808.35 |
| 342.98 | 20038.00 | 808.98 |
| 342.98 | 21018.00 | 809.62 |
| 342.98 | 22035.00 | 810.28 |
| 352.86 | 1069.00 | 788.44 |
| 352.86 | 2043.00 | 789.24 |
| 352.86 | 3040.00 | 790.04 |
| 352.86 | 4048.00 | 790.78 |
| 352.86 | 5038.00 | 791.59 |
| 352.86 | 6043.00 | 792.34 |
| 352.86 | 7038.00 | 793.09 |
| 352.86 | 8039.00 | 793.84 |
| 352.86 | 9040.00 | 794.57 |
| 352.86 | 10038.00 | 795.32 |
| 352.86 | 11032.00 | 796.04 |
| 352.86 | 12032.00 | 796.74 |
| 352.86 | 13040.00 | 797.47 |
| 352.86 | 14046.00 | 798.18 |
| 352.86 | 15043.00 | 798.89 |
| 352.86 | 16037.00 | 799.59 |
| 352.86 | 17040.00 | 800.26 |
| 352.86 | 18046.00 | 800.95 |
| 352.86 | 19040.00 | 801.63 |
| 352.86 | 20064.00 | 802.32 |
| 352.86 | 21048.00 | 802.96 |
| 352.86 | 22049.00 | 803.62 |
| 362.89 | 1077.00 | 781.02 |
| 362.89 | 2027.00 | 781.83 |
| 362.89 | 3089.00 | 782.69 |
| 362.89 | 4047.00 | 783.49 |
| 362.89 | 5061.00 | 784.29 |
| 362.89 | 6060.00 | 785.12 |
| 362.89 | 7041.00 | 785.91 |
| 362.89 | 8049.00 | 786.7 |
| 362.89 | 9049.00 | 787.47 |
| 362.89 | 10052.00 | 788.25 |
| 362.89 | 11045.00 | 788.99 |
| 362.89 | 12044.00 | 789.75 |
| 362.89 | 13054.00 | 790.54 |
| 362.89 | 14053.00 | 791.25 |
| 362.89 | 15052.00 | 792.0 |
| 362.89 | 16056.00 | 792.77 |
| 362.89 | 17063.00 | 793.47 |
| 362.89 | 18062.00 | 794.2 |
| 362.89 | 19062.00 | 794.91 |
| 362.89 | 20068.00 | 795.64 |
| 362.89 | 21072.00 | 796.35 |
| 362.89 | 22063.00 | 797.03 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [390.26; 531.78] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.62798e+01 | |||
| Coefficient B | -4.94119e+03 | |||
| Coefficient C | -8.12810e+01 | |||
| Temperature range, min. | 390.26 | |||
| Temperature range, max. | 531.78 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
| Pvap | 1.33 | kPa | 390.26 | Calculated Property |
| Pvap | 2.89 | kPa | 405.98 | Calculated Property |
| Pvap | 5.84 | kPa | 421.71 | Calculated Property |
| Pvap | 11.09 | kPa | 437.43 | Calculated Property |
| Pvap | 19.94 | kPa | 453.16 | Calculated Property |
| Pvap | 34.18 | kPa | 468.88 | Calculated Property |
| Pvap | 56.19 | kPa | 484.61 | Calculated Property |
| Pvap | 88.98 | kPa | 500.33 | Calculated Property |
| Pvap | 136.30 | kPa | 516.06 | Calculated Property |
| Pvap | 202.67 | kPa | 531.78 | Calculated Property |
| Pvap | [1.20e-04; 2421.30] | kPa | [280.05; 690.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 2.35419e+02 | |||
| Coefficient B | -1.88148e+04 | |||
| Coefficient C | -3.16474e+01 | |||
| Coefficient D | 1.36741e-05 | |||
| Temperature range, min. | 280.05 | |||
| Temperature range, max. | 690.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 300 400 500 600 | ||||
| Pvap | 1.20e-04 | kPa | 280.05 | Calculated Property |
| Pvap | 0.02 | kPa | 325.60 | Calculated Property |
| Pvap | 0.53 | kPa | 371.15 | Calculated Property |
| Pvap | 5.66 | kPa | 416.70 | Calculated Property |
| Pvap | 31.38 | kPa | 462.25 | Calculated Property |
| Pvap | 112.99 | kPa | 507.80 | Calculated Property |
| Pvap | 304.78 | kPa | 553.35 | Calculated Property |
| Pvap | 678.49 | kPa | 598.90 | Calculated Property |
| Pvap | 1332.65 | kPa | 644.45 | Calculated Property |
| Pvap | 2421.30 | kPa | 690.00 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Decanol.
Mixtures
- Benzene, 1-chloro-2-methyl- + 1-Decanol
- Benzene, 1-chloro-3-methyl- + 1-Decanol
- 1-Decanol + Benzene, 1-chloro-4-methyl-
- 1-Octene + 1-Decanol
- Pentanoic acid, 4-oxo- + 1-Decanol + Water
- Cholesterol + 1-Decanol
- Cholesterol + 1-Decanol + Cyclohexane
- Tributyl phosphate + 1-Decanol
- 1-Octanol + 1-Decanol
- Tridodecylamine + 1-Decanol
- Thymol + 1-Decanol
- 1-Decanol + Cyclohexane
- Tripalmitin + 1-Decanol
- Butane, 1-chloro- + 1-Decanol
- Ethane, 1,1,2,2-tetrabromo- + 1-Decanol
- 1-Decanol + Ethane, 1,1,2,2-tetrachloro-
- Heptane + 1-Decanol
- 1-Decanol + Propanoic acid + Water
- n-Butyl ether + 1-Decanol
- Lactic acid + 1-Decanol + Water
Find more mixtures with 1-Decanol.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 1-Decanol with Isomeric Chlorotoluenes
- Solubility of 9-fluorenone, thianthrene and xanthene in organic solvents
- The co-solubility of 2-ethylhexanoic acid and some liquid alcohols in supercritical carbon dioxide
- Phase behaviour of I-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium based ionic liquids with alcohols, water, ketones and hydrocarbons: The effect of cation and anion on solubility
- Phase equilibria of high molecular mass 1-alcohols in supercritical propane
- Excess molar enthalpy of 1-alkanol + 1-octene mixtures at 298.15K Experimental results and theoretical description by means of the ERAS and TB models
- Phase equilibria of (water + levunilic acid + alcohol) ternary systems
- (Solid + liquid) and (liquid + liquid) phase equilibria measurements and correlation of the binary systems {tri-iso-butyl(methyl)phosphonium tosylate + alcohol, or +hydrocarbon}
- Experimental solid-liquid phase equilibria of {cholesterol + binary solvent mixture: 1-Alcohol (C4-C10) + cyclohexane}
- (Solid + liquid) and (liquid + liquid) phase equilibria study and correlation of the binary systems {N-butyl-3-methylpyridinium tosylate + water, or + an alcohol, or + a hydrocarbon}
- SLE and LLE for tri-butylphosphate or tri-octylamine contained systems; extractive solvents of Molybdenum
- The solid-liquid phase diagrams of binary mixtures of even saturated fatty alcohols
- Liquid-liquid phase equilibrium of (piperidinium-based ionic liquid + an alcohol) binary systems and modelling with NRHB and PCP-SAFT
- Solid-liquid equilibrium, excess molar volume, and deviations in the molar refractivity for the binary and ternary mixtures of Alamine 304-1 with 1-octanol, 2-octanol, and 1-decanol
- Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
- Measurement and correlation of vapor-liquid equilibria for alkane + alkanol andalkane + alkanediol systems with group contribution COSMOSPACE model
- Unusual behavior of the isotope effect on miscibility of 1-hexyl-3-methylimidazolium bis(trifluorosulfonyl)imide with 1-alkanols
- Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
- High pressure phase behaviour of the CO2 + 1-decanol + n-dodecane system
- (Solid + liquid) equilibrium phase diagrams in binary mixtures containing terpenes: New experimental data and analysis of several modelling strategies with modified UNIFAC (Dortmund) and PC-SAFT equation of state
- Reactive extraction of pimelic (heptanedioic) acid from dilute aqueous solutions using trioctylamine in decan-1-ol
- The behavior of mercury in water, alcohols, monoethylene glycol and triethylene glycol II. Elemental mercury solubility in alcohols, ethers and acetone; gas plant mercury distribution; and speciation in monoethylene glycol solution
- Measurement and modelling of high pressure bubble- and dew-point data for the CO2 + 1-decanol + 3,7-dimethyl-1-octanol system
- Study of molecular interactions and preferential solvation in binary mixtures of cyclohexane and (C5-C10) 1-alkanol by Kirkwood-Buff integrals
- Solid-liquid phase equilibrium diagrams of binary mixtures containing fatty acids, fatty alcohol compounds and tripalmitin using differential scanning calorimetry
- Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
- Excess molar volumes and viscosities of (1,1,2,2-tetrabromoethane + 1-alkanols) at T = (293.15 and 303.15) K
- Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
- (Liquid + liquid) phase equilibria of 1-alkyl-3-methylimidazolium methylsulfate with alcohols, or ethers, or ketones
- Excess molar heat capacities for (decan-1-ol + n-heptane) at temperatures from (290 to 318) K. Experimental results and theoretical description using the ERAS model
- Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
- (Liquid + liquid) equilibria of (water + propionic acid + alcohol) ternary systems
- Phase equilibria of didecyldimethylammonium nitrate ionic liquid with water and organic solvents
- (Liquid + liquid) equilibria of (water + lactic acid + alcohol) ternary systems
- Molar excess enthalpies at T = 298.15 K for (1-alkanol + dibutylether) systems
- Thermophysical and sonochemical behaviour of binary mixtures of decan-1-ol with halohydrocarbons at (T = 293.15 and 313.15) K
- Volumetric, acoustic, and viscometric studies of molecular interactions in binary mixtures of diethylene glycol monomethyl ether with 1-alkanols at temperatures from (293.15 to 308.15) K
- Thermophysical properties and phase equilibria study of the binary systems {N-hexylquinolinium bis(trifluoromethylsulfonyl)imide + aromatic hydrocarbons, or an alcohol}
- Measurement and correlation of the excess molar enthalpy of (1-nonanol, or 1-decanol + acetonitrile) mixtures at (298.15, 303.15, and 308.15) K and atmospheric pressure
- PrhoT measurements and derived properties of liquid 1-alkanols
- Ternary equilibrium data of mixtures consisting of 2-butanol, water, and heavy alcohols at T = 298.2 K
- Studies of thermophysical properties of binary liquid mixtures of amine and alcohols at various temperatures
- Phase equilibria of ternary systems (water + pyruvic acid + high boiling alcohol). Thermodynamic modeling and optimization of extraction
- Physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-octanol, 1-nonanol and 1-decanol at different temperatures
- Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
- Thermodynamics of 1-alkanol + linear polyether mixtures
- Thermodynamic, transport and excess properties of 2-butoxy ethanol +1-alkanol (C6,C8,C10) at different temperatures
- Volumetric and compressibility studies on tri-n-butyl phosphate (TBP)-phase modifier (1-octanol, 1-decanol and isodecanol) interactions from T = (298.15 to 323.15) K
- Densities, speeds of sound and viscosities of binary mixtures of tetrahydrofuran with 1-hexanol, 1-octanol and 1-decanol at T = (298.15 to 313.15) K
- Effect of temperature and chain length on the viscosity and surface tension of binary systems of N,N-dimethylformamide with 1-octanol, 1-nonanol and 1-decanol
- Thermodynamics of mixtures with strongly negative deviations from Raoult s law. XII. Densities, viscosities and refractive indices at T = (293.15 to 303.15) K for (1-heptanol, or 1-decanol + cyclohexylamine) systems. Application of the ERAS model to (1-alkanol + cyclohexylamine) mixtures
- Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
- Thermodynamics of mixing for binary mixtures of 1-octanol and 1-decanol with n-dodecane and ternary mixture of (TBP + 1-octanol + dodecane) at T = (298.15 to 323.15) K
- Optimization and modeling of extraction equilibria of the type 2 ternary systems containing (water + isovaleric acid + solvent)
- Studies on the importance of chain length of alkanols on the thermodynamic and transport properties of liquid mixtures at various temperatures
- Super- and near-critical fluid phase behavior and phenomena of the ternary system CO2 + 1-decanol + n-tetradecane
- FT-IR studies and excess thermodynamic properties of binary liquid mixtures 2-(2-butoxyethoxy) ethanol with 1-hexanol, 1-octanol and 1-decanol at different temperatures
- Excess molar enthalpies and heat capacities of dimethyl sulfoxide + seven normal alkanols at 303.15K and atmospheric pressure
- Temperature and composition dependence of the density and viscosity of binary mixtures of (1-decanol + fragrance material)
- Measurement and correlation of tie-line data in ternary aqueous mixtures of 1,3-butanediol with decanol at different temperatures
- Tie-line data for water- formic acid-1-decanol ternary system at T = (298.2, 303.2, 313.2, 323.2) K
- Solubility and Tie Line Data of the Water - Phosphoric Acid Solvents at T = (303.2 and 313.2) K: An Experimental and Correlational Study
- Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
- Thermodynamics of mixtures containing amines. XVI. CE pm of 1-butanol, 1-octanol or 1-decanol + benzylamine systems at (298.15, 308.15, 318.15 and 333.15) K
- Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
- The manufacture of organic carbonate-poly(methyl ethylacrylate) nanowebs with thermal buffering effect
- Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
- Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
- Extraction of Citric Acid and Maleic Acid from Their Aqueous Solutions Using a Phosphorus-Bonded Extractant, Tri-n-octylphosphineoxide, and a Secondary Amine, Dioctylamine
- Experimental Data of Citric Acid Extraction from Aqueous Solution with 1-Decanol by Using Liquid-Liquid Equilibrium
- Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
- Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
- Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
- Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
- Twenty Years of Experimental Determinations of Thermophysical Properties with High Accuracy: Thermodynamics Laboratory, ESIQIE-IPN, Mexico
- Comparison of Extractability of Oxalic Acid from Dilute Aqueous Solutions Using Dioctylamine and Trioctylphosphine Oxide
- Kirkwood-Buff Integrals, Excess Volume, and Preferential Solvation in Pentanoic Acid/(C5-C10) 1-Alkanol Binary Mixtures
- Thermodynamic Properties of 1-Hexyl-3-methylimidazolium Nitrate and 1-Alkanols Mixtures: PC-SAFT Model
- Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T ) 298.15 K for 1-Bromobutane with 1-Octanol or 1-Decanol
- Experimental Solid + Liquid Equilibria and Excess Molar Volume of Alkanol + Octylamine Mixtures. Analysis in Terms of ERAS, DISQUAC, and Modified UNIFAC
- Heat Capacities and Derived Thermodynamic Functions of 1-Hexanol, 1-Heptanol, 1-Octanol, and 1-Decanol between 5 K and 390 K
- Measurement of Density and Viscosity of Binary 1-Alkanol Systems (C8-C11) at 101 kPa and Temperatures from (283.15 to 313.15) K
- Experimental (Solid + Liquid) and (Liquid + Liquid) Equilibria and Excess Molar Volume of Alkanol + Acetonitrile, Propanenitrile, and Butanenitrile Mixtures
- Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Octan-1-ol and Decan-1-ol at (303.15 and 313.15) K
- Densities, Viscosities, and Speed of Sound Studies of Binary Mixtures of Methylbenzene with Heptan-1-ol, Octan-1-ol, and Decan-1-ol at (303.15 and 313.15) K
- Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
- Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
- Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
- Vapor-Liquid Equilibria of Binary Systems of Ethene Oxide + Dodecane, Ethene Oxide + 1-Decanol, and Ethene Oxide + 1-Dodecanol and Prediction with the Predictive Soave-Redlich-Kwong (PSRK) Equation of State
- Liquid-Liquid Phase Behavior of Solutions of 1-Dodecyl-3-methylimidazolium Bis(trifluoromethylsulphonyl)imide (C12mimNTf2) in n- Alkyl Alcohols
- Densities, Speeds of Sound, and Refractive Indices of Binary Mixtures of Decan-1-ol with Anisole, o-Cresol, m-Cresol, and p-Cresol at T = (298.15, 303.15, and 308.15) K
- Measurements, Correlations, and Mod. UNIFAC (Do) Prediction of (Solid-Liquid) Phase Equilibria Diagrams in Binary Systems (Aliphatic Ketone + an Alcohol)
- Densities, Speeds of Sound, and Isentropic Compressibilities of Binary Mixtures of {Alkan-1-ols + 1,2-Dimethylbenzene, or 1,3-Dimethylbenzene, or 1,4-Dimethylbenzene, or Ethylbenzene} at (293.15, 303.15, and 313.15) K
- Influence of the Temperature on the Liquid-Liquid-Solid Equilibria of the Ternary System Water + Ethanol + 1-Decanol
- Liquid-Liquid Phase Behavior of Solutions of 1-Hexyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C6mimNTf2) in n-Alkyl Alcohols
- Micellar Properties and Related Thermodynamic Parameters of Aqueous Anionic Surfactants in the Presence of Monohydric Alcohols
- Liquid Liquid Phase Equilibria of 1-Propanol + Water + n-Alcohol Ternary Systems at 298.15 K and Atmospheric Pressure
- Liquid Liquid Phase Behavior of Solutions of 1-Butyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C4mimNTf2) in n-Alkyl Alcohols
- Phase Equilibria of the Carbon Dioxide + 1-Decanol System at High Pressures
- Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
- Solubility Determination and Correlation of (2R,3S,4S,5S)-6-(Hydroxymethyl)-tetrahydro-2H-pyran-2,3,4, 5-tetraol in Fatty Alcohol
- Densities, Isothermal Compressibilities, and Isobaric Thermal Expansivities of Hexan-2-ol, Octan-1-ol, and Decan-1-ol from (313 to 363) K and Pressures up to 22 MPa
- Study of a Binary Liquid Mixture of Diethylamine and 1-Decanol and Validation of Theoretical Approaches of Sound Speed at Different Temperatures
- Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water)
- Experimental and Theoretical Study of the Phase Equilibria in Ternary Aqueous Mixtures of 1,4-Butanediol with Alcohols at 298.2 K
- Volumetric and Viscometric Properties of Binary Liquid Mixtures of Ethylene Glycol Monomethyl Ether + 1-Hexanol, 1-Octanol, and 1-Decanol at Temperatures of T = (293.15, 298.15, 303.15, and 308.15) K
- Solid-Liquid Equilibria, Excess Molar Volumes, and Molar Refractivity Deviations for Extractive Solvents of Molybdenum
- Liquid-Liquid Phase Behavior of Solutions of 1-Octyl- and 1-Decyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide (C8,10mimNTf2) in n-Alkyl Alcohols
- Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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