- InChI
- InChI=1S/C5H12O/c1-3-4-5(2)6/h5-6H,3-4H2,1-2H3
- InChI Key
- JYVLIDXNZAXMDK-UHFFFAOYSA-N
- Formula
- C5H12O
- SMILES
- CCCC(C)O
- Molecular Weight1
- 88.15
- CAS
- 6032-29-7
- Other Names
-
- (R,S)-2-pentanol
- 1-Methyl-1-butanol
- 1-Methylbutanol
- 2-Pentyl alcohol
- Isoamyl alcohol, secondary
- Methylpropylcarbinol
- Pentan-2-ol
- Pentanol-2
- dl-2-pentanol
- n-C3H7CH(OH)CH3
- sec-Amyl alcohol
- sec-Pentanol
- sec-Pentyl alcohol
- sec-n-Amyl 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).
- 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).
- 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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical 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.
- S°gas : Molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | -3315.40 ± 0.67 | kJ/mol | NIST |
| η | 0.0034210 | Pa×s | Speeds ... |
| ΔfG° | -148.04 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-314.60; -312.70] | kJ/mol |
|
| ΔfH°gas | -312.70 | kJ/mol | NIST |
| ΔfH°gas | -313.80 ± 1.10 | kJ/mol | NIST |
| ΔfH°gas | -314.60 ± 1.50 | kJ/mol | NIST |
| ΔfH°liquid | [-367.10; -365.20] | kJ/mol |
|
| ΔfH°liquid | -365.20 ± 1.10 | kJ/mol | NIST |
| ΔfH°liquid | -366.40 ± 1.70 | kJ/mol | NIST |
| ΔfH°liquid | -367.10 ± 0.75 | kJ/mol | NIST |
| ΔfusH° | 9.27 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [52.60; 54.20] | kJ/mol |
|
| ΔvapH° | 53.60 | kJ/mol | NIST |
| ΔvapH° | 54.20 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 52.60 ± 1.30 | kJ/mol | NIST |
| ΔvapH° | 52.60 ± 1.30 | kJ/mol | NIST |
| ΔvapH° | 53.00 | kJ/mol | NIST |
| IE | [9.78; 10.27] | eV |
|
| IE | 9.78 ± 0.03 | eV | NIST |
| IE | 9.78 ± 0.07 | eV | NIST |
| IE | 9.78 | eV | NIST |
| IE | 10.27 | eV | NIST |
| log10WS | [-0.29; -0.29] |
|
|
| log10WS | -0.29 | Aq. Sol... | |
| log10WS | -0.29 | Estimat... | |
| logPoct/wat | 1.167 | Crippen Calculated Property | |
| McVol | 87.180 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [3640.00; 3710.00] | kPa |
|
| Pc | 3675.00 | kPa | KDB |
| Pc | 3680.00 ± 20.00 | kPa | NIST |
| Pc | 3640.00 ± 40.00 | kPa | NIST |
| Pc | 3710.00 ± 20.00 | kPa | NIST |
| Pc | 3710.00 ± 20.00 | kPa | NIST |
| ρc | [267.97; 267.97] | kg/m3 |
|
| ρc | 267.97 ± 1.76 | kg/m3 | NIST |
| ρc | 267.97 ± 20.27 | kg/m3 | NIST |
| Inp | [661.00; 730.00] |
|
|
| Inp | 692.00 | NIST | |
| Inp | 697.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 701.00 | NIST | |
| Inp | 704.00 | NIST | |
| Inp | 697.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 701.00 | NIST | |
| Inp | 704.00 | NIST | |
| Inp | 697.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 666.00 | NIST | |
| Inp | 671.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 665.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | Outlier 661.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 705.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 706.00 | NIST | |
| Inp | 702.00 | NIST | |
| Inp | Outlier 730.00 | NIST | |
| Inp | 705.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 662.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 717.00 | NIST | |
| Inp | 717.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 718.00 | NIST | |
| Inp | Outlier 730.00 | NIST | |
| Inp | 712.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 703.00 | NIST | |
| Inp | 704.00 | NIST | |
| Inp | 700.00 | NIST | |
| Inp | 703.00 | NIST | |
| Inp | 706.00 | NIST | |
| Inp | 718.00 | NIST | |
| Inp | 672.00 | NIST | |
| Inp | 674.00 | NIST | |
| Inp | 674.00 | NIST | |
| Inp | 674.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 699.00 | NIST | |
| Inp | 699.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 701.00 | NIST | |
| Inp | 706.00 | NIST | |
| Inp | 700.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 700.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 706.00 | NIST | |
| Inp | 671.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 710.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 718.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 703.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 706.00 | NIST | |
| Inp | 662.00 | NIST | |
| Inp | 691.00 | NIST | |
| I | [1081.00; 1153.00] |
|
|
| I | 1130.00 | NIST | |
| I | 1129.00 | NIST | |
| I | 1121.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1129.00 | NIST | |
| I | 1121.00 | NIST | |
| I | 1112.00 | NIST | |
| I | 1115.00 | NIST | |
| I | 1117.00 | NIST | |
| I | 1117.00 | NIST | |
| I | 1112.00 | NIST | |
| I | 1113.00 | NIST | |
| I | 1100.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1138.00 | NIST | |
| I | 1119.00 | NIST | |
| I | 1138.00 | NIST | |
| I | 1100.00 | NIST | |
| I | 1096.00 | NIST | |
| I | 1094.00 | NIST | |
| I | 1120.00 | NIST | |
| I | 1122.00 | NIST | |
| I | 1120.00 | NIST | |
| I | 1105.00 | NIST | |
| I | 1127.00 | NIST | |
| I | 1107.00 | NIST | |
| I | 1116.00 | NIST | |
| I | 1107.00 | NIST | |
| I | 1107.00 | NIST | |
| I | 1109.00 | NIST | |
| I | 1110.00 | NIST | |
| I | 1109.00 | NIST | |
| I | 1109.00 | NIST | |
| I | 1116.00 | NIST | |
| I | 1139.00 | NIST | |
| I | 1142.00 | NIST | |
| I | 1139.00 | NIST | |
| I | 1122.00 | NIST | |
| I | 1109.00 | NIST | |
| I | 1109.00 | NIST | |
| I | 1118.00 | NIST | |
| I | Outlier 1153.00 | NIST | |
| I | 1112.00 | NIST | |
| I | 1135.00 | NIST | |
| I | 1136.00 | NIST | |
| I | 1124.00 | NIST | |
| I | Outlier 1081.00 | NIST | |
| I | 1112.00 | NIST | |
| I | 1123.00 | NIST | |
| I | 1123.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1114.00 | NIST | |
| I | 1118.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1142.00 | NIST | |
| I | 1117.00 | NIST | |
| I | 1122.00 | NIST | |
| I | 1138.00 | NIST | |
| I | 1121.00 | NIST | |
| I | 1116.00 | NIST | |
| I | 1135.00 | NIST | |
| I | 1136.00 | NIST | |
| I | 1113.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1094.00 | NIST | |
| I | 1117.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1119.00 | NIST | |
| I | 1135.00 | NIST | |
| I | 1120.00 | NIST | |
| I | Outlier 1091.00 | NIST | |
| I | 1116.00 | NIST | |
| I | 1100.00 | NIST | |
| I | 1116.00 | NIST | |
| I | Outlier 1085.00 | NIST | |
| I | 1122.00 | NIST | |
| I | 1126.00 | NIST | |
| I | 1129.00 | NIST | |
| I | 1142.00 | NIST | |
| I | 1140.00 | NIST | |
| I | 1124.00 | NIST | |
| I | Outlier 1148.00 | NIST | |
| I | 1121.00 | NIST | |
| I | Outlier 1091.00 | NIST | |
| I | 1105.00 | NIST | |
| I | 1107.00 | NIST | |
| I | 1110.00 | NIST | |
| I | 1116.00 | NIST | |
| I | 1135.00 | NIST | |
| I | 1123.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1121.00 | NIST | |
| I | 1116.00 | NIST | |
| I | 1122.00 | NIST | |
| I | 1124.00 | NIST | |
| I | 1107.00 | NIST | |
| S°gas | 392.00 ± 0.90 | J/mol×K | NIST |
| Tboil | [364.15; 400.65] | K |
|
| Tboil | 392.40 | K | KDB |
| Tboil | 392.10 | K | NIST |
| Tboil | 391.40 ± 1.00 | K | NIST |
| Tboil | 391.15 ± 2.00 | K | NIST |
| Tboil | 388.20 ± 3.00 | K | NIST |
| Tboil | 391.15 ± 4.00 | K | NIST |
| Tboil | 392.45 ± 1.00 | K | NIST |
| Tboil | 392.45 ± 0.30 | K | NIST |
| Tboil | 392.15 ± 1.00 | K | NIST |
| Tboil | 392.35 ± 0.50 | K | NIST |
| Tboil | 391.65 ± 1.00 | K | NIST |
| Tboil | 392.65 ± 0.50 | K | NIST |
| Tboil | 390.40 ± 2.00 | K | NIST |
| Tboil | 392.35 ± 0.50 | K | NIST |
| Tboil | 392.95 ± 0.50 | K | NIST |
| Tboil | Outlier 364.15 ± 2.00 | K | NIST |
| Tboil | 392.50 ± 1.00 | K | NIST |
| Tboil | 392.00 ± 0.50 | K | NIST |
| Tboil | 392.65 ± 1.00 | K | NIST |
| Tboil | 392.60 ± 0.50 | K | NIST |
| Tboil | 392.15 ± 1.00 | K | NIST |
| Tboil | 392.70 ± 0.30 | K | NIST |
| Tboil | 393.00 ± 0.10 | K | NIST |
| Tboil | 392.15 ± 1.00 | K | NIST |
| Tboil | 392.45 ± 0.40 | K | NIST |
| Tboil | 392.15 ± 2.00 | K | NIST |
| Tboil | 392.15 ± 2.00 | K | NIST |
| Tboil | 392.45 ± 0.50 | K | NIST |
| Tboil | 392.00 ± 1.50 | K | NIST |
| Tboil | 391.00 ± 1.00 | K | NIST |
| Tboil | Outlier 400.65 ± 3.00 | K | NIST |
| Tboil | 392.15 ± 1.00 | K | NIST |
| Tboil | 392.36 ± 0.20 | K | NIST |
| Tboil | 392.15 ± 2.00 | K | NIST |
| Tboil | 392.15 ± 1.00 | K | NIST |
| Tboil | 392.15 ± 1.00 | K | NIST |
| Tboil | 392.35 ± 0.50 | K | NIST |
| Tboil | 392.15 ± 1.00 | K | NIST |
| Tboil | 392.05 ± 0.50 | K | NIST |
| Tboil | 393.65 ± 2.00 | K | NIST |
| Tboil | 393.15 ± 2.00 | K | NIST |
| Tboil | 392.15 ± 1.00 | K | NIST |
| Tboil | 391.15 ± 1.00 | K | NIST |
| Tboil | 392.15 ± 2.00 | K | NIST |
| Tc | [560.00; 560.40] | K |
|
| Tc | 560.30 | K | KDB |
| Tc | 560.30 ± 0.50 | K | NIST |
| Tc | Outlier 560.00 ± 0.70 | K | NIST |
| Tc | 560.40 ± 0.60 | K | NIST |
| Tc | 560.40 ± 0.60 | K | NIST |
| Tc | 560.40 | K | NIST |
| Tc | 560.40 ± 0.25 | K | NIST |
| Tfus | [200.00; 211.65] | K |
|
| Tfus | 211.65 | K | Aq. Sol... |
| Tfus | 200.00 | K | KDB |
| Vc | [0.329; 0.329] | m3/kmol |
|
| Vc | 0.329 | m3/kmol | KDB |
| Vc | 0.329 | m3/kmol | NIST |
| Zc | 0.2595350 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [169.82; 216.94] | J/mol×K | [405.54; 570.76] |
|
| Cp,gas | 169.82 | J/mol×K | 405.54 | Joback Calculated Property |
| Cp,gas | 178.43 | J/mol×K | 433.08 | Joback Calculated Property |
| Cp,gas | 186.73 | J/mol×K | 460.61 | Joback Calculated Property |
| Cp,gas | 194.72 | J/mol×K | 488.15 | Joback Calculated Property |
| Cp,gas | 202.42 | J/mol×K | 515.68 | Joback Calculated Property |
| Cp,gas | 209.82 | J/mol×K | 543.22 | Joback Calculated Property |
| Cp,gas | 216.94 | J/mol×K | 570.76 | Joback Calculated Property |
| Cp,liquid | [138.34; 235.81] | J/mol×K | [134.18; 301.07] |
|
| Cp,liquid | 138.36 | J/mol×K | 134.18 | Heat Ca... |
| Cp,liquid | 145.14 | J/mol×K | 134.47 | Heat Ca... |
| Cp,liquid | 146.40 | J/mol×K | 135.24 | Heat Ca... |
| Cp,liquid | 146.52 | J/mol×K | 136.00 | Heat Ca... |
| Cp,liquid | 138.34 | J/mol×K | 136.05 | Heat Ca... |
| Cp,liquid | 145.03 | J/mol×K | 136.39 | Heat Ca... |
| Cp,liquid | 146.29 | J/mol×K | 137.22 | Heat Ca... |
| Cp,liquid | 138.35 | J/mol×K | 137.97 | Heat Ca... |
| Cp,liquid | 145.17 | J/mol×K | 138.36 | Heat Ca... |
| Cp,liquid | 146.59 | J/mol×K | 138.84 | Heat Ca... |
| Cp,liquid | 146.22 | J/mol×K | 139.21 | Heat Ca... |
| Cp,liquid | 138.69 | J/mol×K | 139.90 | Heat Ca... |
| Cp,liquid | 145.48 | J/mol×K | 140.33 | Heat Ca... |
| Cp,liquid | 146.34 | J/mol×K | 141.20 | Heat Ca... |
| Cp,liquid | 146.74 | J/mol×K | 141.77 | Heat Ca... |
| Cp,liquid | 139.02 | J/mol×K | 141.83 | Heat Ca... |
| Cp,liquid | 145.81 | J/mol×K | 142.30 | Heat Ca... |
| Cp,liquid | 146.48 | J/mol×K | 143.19 | Heat Ca... |
| Cp,liquid | 139.32 | J/mol×K | 143.77 | Heat Ca... |
| Cp,liquid | 146.91 | J/mol×K | 144.73 | Heat Ca... |
| Cp,liquid | 146.45 | J/mol×K | 145.18 | Heat Ca... |
| Cp,liquid | 146.59 | J/mol×K | 147.18 | Heat Ca... |
| Cp,liquid | 147.17 | J/mol×K | 147.68 | Heat Ca... |
| Cp,liquid | 146.66 | J/mol×K | 149.17 | Heat Ca... |
| Cp,liquid | 147.42 | J/mol×K | 150.63 | Heat Ca... |
| Cp,liquid | 146.74 | J/mol×K | 151.16 | Heat Ca... |
| Cp,liquid | 146.86 | J/mol×K | 153.16 | Heat Ca... |
| Cp,liquid | 147.65 | J/mol×K | 153.58 | Heat Ca... |
| Cp,liquid | 147.04 | J/mol×K | 155.16 | Heat Ca... |
| Cp,liquid | 148.06 | J/mol×K | 156.54 | Heat Ca... |
| Cp,liquid | 147.26 | J/mol×K | 157.16 | Heat Ca... |
| Cp,liquid | 147.41 | J/mol×K | 159.16 | Heat Ca... |
| Cp,liquid | 148.35 | J/mol×K | 159.50 | Heat Ca... |
| Cp,liquid | 147.59 | J/mol×K | 161.15 | Heat Ca... |
| Cp,liquid | 148.75 | J/mol×K | 162.46 | Heat Ca... |
| Cp,liquid | 147.87 | J/mol×K | 163.15 | Heat Ca... |
| Cp,liquid | 148.07 | J/mol×K | 165.15 | Heat Ca... |
| Cp,liquid | 149.14 | J/mol×K | 165.42 | Heat Ca... |
| Cp,liquid | 148.38 | J/mol×K | 167.15 | Heat Ca... |
| Cp,liquid | 149.64 | J/mol×K | 168.38 | Heat Ca... |
| Cp,liquid | 148.62 | J/mol×K | 169.15 | Heat Ca... |
| Cp,liquid | 148.98 | J/mol×K | 171.15 | Heat Ca... |
| Cp,liquid | 150.12 | J/mol×K | 171.34 | Heat Ca... |
| Cp,liquid | 149.17 | J/mol×K | 173.15 | Heat Ca... |
| Cp,liquid | 150.62 | J/mol×K | 174.31 | Heat Ca... |
| Cp,liquid | 149.61 | J/mol×K | 175.15 | Heat Ca... |
| Cp,liquid | 150.03 | J/mol×K | 177.14 | Heat Ca... |
| Cp,liquid | 151.24 | J/mol×K | 177.27 | Heat Ca... |
| Cp,liquid | 150.37 | J/mol×K | 179.14 | Heat Ca... |
| Cp,liquid | 151.84 | J/mol×K | 180.22 | Heat Ca... |
| Cp,liquid | 150.83 | J/mol×K | 181.14 | Heat Ca... |
| Cp,liquid | 151.22 | J/mol×K | 183.13 | Heat Ca... |
| Cp,liquid | 152.41 | J/mol×K | 183.15 | Heat Ca... |
| Cp,liquid | 151.66 | J/mol×K | 185.13 | Heat Ca... |
| Cp,liquid | 153.18 | J/mol×K | 186.06 | Heat Ca... |
| Cp,liquid | 152.22 | J/mol×K | 187.13 | Heat Ca... |
| Cp,liquid | 153.85 | J/mol×K | 188.97 | Heat Ca... |
| Cp,liquid | 152.69 | J/mol×K | 189.12 | Heat Ca... |
| Cp,liquid | 153.28 | J/mol×K | 191.11 | Heat Ca... |
| Cp,liquid | 154.61 | J/mol×K | 191.86 | Heat Ca... |
| Cp,liquid | 153.79 | J/mol×K | 193.10 | Heat Ca... |
| Cp,liquid | 155.46 | J/mol×K | 194.73 | Heat Ca... |
| Cp,liquid | 154.43 | J/mol×K | 195.09 | Heat Ca... |
| Cp,liquid | 155.04 | J/mol×K | 197.08 | Heat Ca... |
| Cp,liquid | 156.28 | J/mol×K | 197.60 | Heat Ca... |
| Cp,liquid | 155.64 | J/mol×K | 199.07 | Heat Ca... |
| Cp,liquid | 157.17 | J/mol×K | 200.45 | Heat Ca... |
| Cp,liquid | 156.37 | J/mol×K | 201.05 | Heat Ca... |
| Cp,liquid | 157.14 | J/mol×K | 203.04 | Heat Ca... |
| Cp,liquid | 158.12 | J/mol×K | 203.28 | Heat Ca... |
| Cp,liquid | 157.90 | J/mol×K | 205.02 | Heat Ca... |
| Cp,liquid | 159.16 | J/mol×K | 206.11 | Heat Ca... |
| Cp,liquid | 158.71 | J/mol×K | 207.00 | Heat Ca... |
| Cp,liquid | 160.23 | J/mol×K | 208.92 | Heat Ca... |
| Cp,liquid | 159.59 | J/mol×K | 208.98 | Heat Ca... |
| Cp,liquid | 160.43 | J/mol×K | 210.96 | Heat Ca... |
| Cp,liquid | 161.38 | J/mol×K | 211.71 | Heat Ca... |
| Cp,liquid | 161.43 | J/mol×K | 212.93 | Heat Ca... |
| Cp,liquid | 162.60 | J/mol×K | 214.50 | Heat Ca... |
| Cp,liquid | 162.36 | J/mol×K | 214.90 | Heat Ca... |
| Cp,liquid | 163.53 | J/mol×K | 216.87 | Heat Ca... |
| Cp,liquid | 163.98 | J/mol×K | 217.27 | Heat Ca... |
| Cp,liquid | 164.58 | J/mol×K | 218.83 | Heat Ca... |
| Cp,liquid | 165.38 | J/mol×K | 220.03 | Heat Ca... |
| Cp,liquid | 165.86 | J/mol×K | 220.79 | Heat Ca... |
| Cp,liquid | 167.19 | J/mol×K | 222.74 | Heat Ca... |
| Cp,liquid | 166.74 | J/mol×K | 222.77 | Heat Ca... |
| Cp,liquid | 168.30 | J/mol×K | 224.69 | Heat Ca... |
| Cp,liquid | 168.21 | J/mol×K | 225.50 | Heat Ca... |
| Cp,liquid | 169.58 | J/mol×K | 226.64 | Heat Ca... |
| Cp,liquid | 169.75 | J/mol×K | 228.21 | Heat Ca... |
| Cp,liquid | 170.97 | J/mol×K | 228.58 | Heat Ca... |
| Cp,liquid | 172.40 | J/mol×K | 230.52 | Heat Ca... |
| Cp,liquid | 171.38 | J/mol×K | 230.92 | Heat Ca... |
| Cp,liquid | 173.26 | J/mol×K | 232.46 | Heat Ca... |
| Cp,liquid | 173.02 | J/mol×K | 233.61 | Heat Ca... |
| Cp,liquid | 174.28 | J/mol×K | 234.41 | Heat Ca... |
| Cp,liquid | 174.82 | J/mol×K | 236.28 | Heat Ca... |
| Cp,liquid | 175.25 | J/mol×K | 236.37 | Heat Ca... |
| Cp,liquid | 176.25 | J/mol×K | 238.35 | Heat Ca... |
| Cp,liquid | 176.57 | J/mol×K | 238.94 | Heat Ca... |
| Cp,liquid | 177.32 | J/mol×K | 240.33 | Heat Ca... |
| Cp,liquid | 178.24 | J/mol×K | 241.59 | Heat Ca... |
| Cp,liquid | 178.65 | J/mol×K | 242.31 | Heat Ca... |
| Cp,liquid | 179.98 | J/mol×K | 244.22 | Heat Ca... |
| Cp,liquid | 180.19 | J/mol×K | 244.29 | Heat Ca... |
| Cp,liquid | 181.71 | J/mol×K | 246.27 | Heat Ca... |
| Cp,liquid | 181.91 | J/mol×K | 246.84 | Heat Ca... |
| Cp,liquid | 183.24 | J/mol×K | 248.24 | Heat Ca... |
| Cp,liquid | 183.85 | J/mol×K | 249.45 | Heat Ca... |
| Cp,liquid | 184.81 | J/mol×K | 250.22 | Heat Ca... |
| Cp,liquid | 185.96 | J/mol×K | 252.04 | Heat Ca... |
| Cp,liquid | 186.49 | J/mol×K | 252.19 | Heat Ca... |
| Cp,liquid | 187.53 | J/mol×K | 254.17 | Heat Ca... |
| Cp,liquid | 187.26 | J/mol×K | 254.62 | Heat Ca... |
| Cp,liquid | 189.21 | J/mol×K | 256.15 | Heat Ca... |
| Cp,liquid | 189.40 | J/mol×K | 257.20 | Heat Ca... |
| Cp,liquid | 190.90 | J/mol×K | 258.13 | Heat Ca... |
| Cp,liquid | 191.63 | J/mol×K | 259.75 | Heat Ca... |
| Cp,liquid | 192.75 | J/mol×K | 260.11 | Heat Ca... |
| Cp,liquid | 194.51 | J/mol×K | 262.08 | Heat Ca... |
| Cp,liquid | 193.87 | J/mol×K | 262.30 | Heat Ca... |
| Cp,liquid | 196.40 | J/mol×K | 264.06 | Heat Ca... |
| Cp,liquid | 196.18 | J/mol×K | 264.83 | Heat Ca... |
| Cp,liquid | 198.15 | J/mol×K | 266.04 | Heat Ca... |
| Cp,liquid | 198.56 | J/mol×K | 267.34 | Heat Ca... |
| Cp,liquid | 200.17 | J/mol×K | 268.01 | Heat Ca... |
| Cp,liquid | 201.01 | J/mol×K | 269.84 | Heat Ca... |
| Cp,liquid | 202.16 | J/mol×K | 269.99 | Heat Ca... |
| Cp,liquid | 204.25 | J/mol×K | 271.96 | Heat Ca... |
| Cp,liquid | 203.73 | J/mol×K | 272.33 | Heat Ca... |
| Cp,liquid | 206.27 | J/mol×K | 273.94 | Heat Ca... |
| Cp,liquid | 206.33 | J/mol×K | 274.80 | Heat Ca... |
| Cp,liquid | 208.32 | J/mol×K | 275.91 | Heat Ca... |
| Cp,liquid | 208.61 | J/mol×K | 277.26 | Heat Ca... |
| Cp,liquid | 210.50 | J/mol×K | 277.88 | Heat Ca... |
| Cp,liquid | 211.18 | J/mol×K | 279.70 | Heat Ca... |
| Cp,liquid | 212.62 | J/mol×K | 279.86 | Heat Ca... |
| Cp,liquid | 214.76 | J/mol×K | 281.83 | Heat Ca... |
| Cp,liquid | 213.77 | J/mol×K | 282.13 | Heat Ca... |
| Cp,liquid | 216.99 | J/mol×K | 283.81 | Heat Ca... |
| Cp,liquid | 216.55 | J/mol×K | 284.54 | Heat Ca... |
| Cp,liquid | 219.38 | J/mol×K | 285.79 | Heat Ca... |
| Cp,liquid | 219.25 | J/mol×K | 286.94 | Heat Ca... |
| Cp,liquid | 221.67 | J/mol×K | 287.77 | Heat Ca... |
| Cp,liquid | 222.07 | J/mol×K | 289.33 | Heat Ca... |
| Cp,liquid | 224.09 | J/mol×K | 289.75 | Heat Ca... |
| Cp,liquid | 224.87 | J/mol×K | 291.70 | Heat Ca... |
| Cp,liquid | 226.30 | J/mol×K | 291.73 | Heat Ca... |
| Cp,liquid | 228.63 | J/mol×K | 293.71 | Heat Ca... |
| Cp,liquid | 227.43 | J/mol×K | 294.06 | Heat Ca... |
| Cp,liquid | 231.18 | J/mol×K | 295.69 | Heat Ca... |
| Cp,liquid | 230.08 | J/mol×K | 296.41 | Heat Ca... |
| Cp,liquid | 233.65 | J/mol×K | 297.66 | Heat Ca... |
| Cp,liquid | 233.00 | J/mol×K | 298.75 | Heat Ca... |
| Cp,liquid | 235.81 | J/mol×K | 299.65 | Heat Ca... |
| Cp,liquid | 235.62 | J/mol×K | 301.07 | Heat Ca... |
| η | [0.0013900; 0.0040010] | Pa×s | [293.15; 323.15] |
|
| η | 0.0040010 | Pa×s | 293.15 | Viscosi... |
| η | 0.0040010 | Pa×s | 293.15 | Dynamic... |
| η | 0.0040010 | Pa×s | 293.15 | Viscosi... |
| η | 0.0032730 | Pa×s | 298.15 | Viscosi... |
| η | 0.0032730 | Pa×s | 298.15 | Dynamic... |
| η | 0.0033200 | Pa×s | 298.15 | Studies... |
| η | 0.0034780 | Pa×s | 298.15 | Densiti... |
| η | 0.0034990 | Pa×s | 298.15 | Densiti... |
| η | 0.0032730 | Pa×s | 298.15 | Viscosi... |
| η | 0.0028010 | Pa×s | 303.15 | Densiti... |
| η | 0.0027080 | Pa×s | 303.15 | Dynamic... |
| η | 0.0027740 | Pa×s | 303.15 | Viscosi... |
| η | 0.0028100 | Pa×s | 303.15 | Studies... |
| η | 0.0027740 | Pa×s | 303.15 | Viscosi... |
| η | 0.0028010 | Pa×s | 303.15 | Densiti... |
| η | 0.0023700 | Pa×s | 308.15 | Studies... |
| η | 0.0023340 | Pa×s | 308.15 | Densiti... |
| η | 0.0023350 | Pa×s | 308.15 | Densiti... |
| η | 0.0019930 | Pa×s | 313.15 | Densiti... |
| η | 0.0019900 | Pa×s | 313.15 | Studies... |
| η | 0.0019930 | Pa×s | 313.15 | Densiti... |
| η | 0.0016600 | Pa×s | 318.15 | Studies... |
| η | 0.0013900 | Pa×s | 323.15 | Studies... |
| ΔfusH | [8.48; 8.48] | kJ/mol | [200.00; 200.00] |
|
| ΔfusH | 8.48 | kJ/mol | 200.00 | NIST |
| ΔfusH | 8.48 | kJ/mol | 200.00 | NIST |
| ΔvapH | [45.40; 58.90] | kJ/mol | [313.00; 368.00] |
|
| ΔvapH | 52.70 ± 0.20 | kJ/mol | 313.00 | NIST |
| ΔvapH | 50.90 ± 0.20 | kJ/mol | 328.00 | NIST |
| ΔvapH | 58.90 | kJ/mol | 333.50 | NIST |
| ΔvapH | 53.70 | kJ/mol | 340.50 | NIST |
| ΔvapH | 49.00 ± 0.20 | kJ/mol | 343.00 | NIST |
| ΔvapH | 54.00 | kJ/mol | 345.50 | NIST |
| ΔvapH | 51.20 | kJ/mol | 357.50 | NIST |
| ΔvapH | 50.30 | kJ/mol | 357.50 | NIST |
| ΔvapH | 46.90 ± 0.10 | kJ/mol | 358.00 | NIST |
| ΔvapH | 45.40 ± 0.10 | kJ/mol | 368.00 | NIST |
| Pvap | [2.13; 101.38] | kPa | [313.15; 392.26] |
|
| Pvap | 2.29 | kPa | 313.15 | Thermod... |
| Pvap | 2.13 | kPa | 313.15 | Vapor-L... |
| Pvap | 2.29 | kPa | 313.15 | Charact... |
| Pvap | 4.16 | kPa | 323.15 | Vapor-L... |
| Pvap | 4.16 | kPa | 323.84 | Vapor-L... |
| Pvap | 4.41 | kPa | 324.19 | Vapor-L... |
| Pvap | 4.39 | kPa | 324.55 | Vapor-L... |
| Pvap | 4.67 | kPa | 325.09 | Vapor-L... |
| Pvap | 4.93 | kPa | 326.00 | Vapor-L... |
| Pvap | 4.89 | kPa | 326.22 | Vapor-L... |
| Pvap | 5.27 | kPa | 326.99 | Vapor-L... |
| Pvap | 5.20 | kPa | 327.15 | Vapor-L... |
| Pvap | 5.43 | kPa | 327.64 | Vapor-L... |
| Pvap | 5.71 | kPa | 328.19 | Vapor-L... |
| Pvap | 5.64 | kPa | 328.23 | Vapor-L... |
| Pvap | 5.91 | kPa | 329.05 | Vapor-L... |
| Pvap | 5.95 | kPa | 329.11 | Vapor-L... |
| Pvap | 6.04 | kPa | 329.11 | Vapor-L... |
| Pvap | 6.16 | kPa | 329.66 | Vapor-L... |
| Pvap | 6.33 | kPa | 329.90 | Vapor-L... |
| Pvap | 6.71 | kPa | 330.86 | Vapor-L... |
| Pvap | 7.08 | kPa | 331.78 | Vapor-L... |
| Pvap | 7.17 | kPa | 332.29 | Vapor-L... |
| Pvap | 7.40 | kPa | 332.55 | Vapor-L... |
| Pvap | 7.31 | kPa | 332.61 | Vapor-L... |
| Pvap | 7.43 | kPa | 332.92 | Vapor-L... |
| Pvap | 7.57 | kPa | 333.15 | Vapor-L... |
| Pvap | 7.52 | kPa | 333.15 | Vapor-L... |
| Pvap | 7.76 | kPa | 333.37 | Vapor-L... |
| Pvap | 7.99 | kPa | 333.88 | Vapor-L... |
| Pvap | 8.33 | kPa | 334.61 | Vapor-L... |
| Pvap | 8.77 | kPa | 335.52 | Vapor-L... |
| Pvap | 9.17 | kPa | 336.34 | Vapor-L... |
| Pvap | 9.19 | kPa | 336.37 | Vapor-L... |
| Pvap | 9.59 | kPa | 337.20 | Vapor-L... |
| Pvap | 9.95 | kPa | 337.85 | Vapor-L... |
| Pvap | 9.99 | kPa | 338.15 | Vapor-L... |
| Pvap | 10.43 | kPa | 338.74 | Vapor-L... |
| Pvap | 10.81 | kPa | 339.44 | Vapor-L... |
| Pvap | 11.21 | kPa | 340.10 | Vapor-L... |
| Pvap | 11.67 | kPa | 340.82 | Vapor-L... |
| Pvap | 12.11 | kPa | 341.54 | Vapor-L... |
| Pvap | 12.52 | kPa | 342.20 | Vapor-L... |
| Pvap | 12.77 | kPa | 342.83 | Vapor-L... |
| Pvap | 12.97 | kPa | 342.88 | Vapor-L... |
| Pvap | 13.00 | kPa | 343.15 | Vapor-L... |
| Pvap | 13.07 | kPa | 343.26 | Vapor-L... |
| Pvap | 13.11 | kPa | 343.30 | Vapor-L... |
| Pvap | 13.16 | kPa | 343.38 | Vapor-L... |
| Pvap | 13.99 | kPa | 344.38 | Vapor-L... |
| Pvap | 14.65 | kPa | 345.27 | Vapor-L... |
| Pvap | 15.31 | kPa | 346.15 | Vapor-L... |
| Pvap | 15.96 | kPa | 347.02 | Vapor-L... |
| Pvap | 16.63 | kPa | 347.80 | Vapor-L... |
| Pvap | 17.32 | kPa | 348.68 | Vapor-L... |
| Pvap | 17.95 | kPa | 349.38 | Vapor-L... |
| Pvap | 18.63 | kPa | 350.16 | Vapor-L... |
| Pvap | 18.66 | kPa | 350.91 | Vapor p... |
| Pvap | 19.31 | kPa | 350.93 | Vapor-L... |
| Pvap | 19.96 | kPa | 351.64 | Vapor-L... |
| Pvap | 20.00 | kPa | 351.88 | Vapor-L... |
| Pvap | 20.43 | kPa | 352.33 | Vapor-L... |
| Pvap | 20.65 | kPa | 352.60 | Vapor-L... |
| Pvap | 20.72 | kPa | 352.70 | Vapor-L... |
| Pvap | 20.83 | kPa | 352.76 | Vapor-L... |
| Pvap | 20.96 | kPa | 352.89 | Vapor-L... |
| Pvap | 21.12 | kPa | 353.05 | Vapor-L... |
| Pvap | 21.19 | kPa | 353.10 | Vapor-L... |
| Pvap | 21.20 | kPa | 353.15 | Vapor-L... |
| Pvap | 21.40 | kPa | 353.35 | Vapor-L... |
| Pvap | 21.33 | kPa | 353.74 | Vapor p... |
| Pvap | 22.16 | kPa | 354.12 | Vapor-L... |
| Pvap | 22.55 | kPa | 354.47 | Solvent... |
| Pvap | 22.83 | kPa | 354.72 | Vapor-L... |
| Pvap | 23.55 | kPa | 355.42 | Vapor-L... |
| Pvap | 24.12 | kPa | 355.92 | Vapor-L... |
| Pvap | 24.00 | kPa | 356.29 | Vapor p... |
| Pvap | 24.44 | kPa | 356.39 | Vapor-L... |
| Pvap | 24.84 | kPa | 356.55 | Vapor-L... |
| Pvap | 25.05 | kPa | 356.60 | Solvent... |
| Pvap | 25.47 | kPa | 357.15 | Vapor-L... |
| Pvap | 26.20 | kPa | 357.76 | Vapor-L... |
| Pvap | 26.00 | kPa | 357.79 | Vapor-L... |
| Pvap | 26.75 | kPa | 358.23 | Vapor-L... |
| Pvap | 26.66 | kPa | 358.61 | Vapor p... |
| Pvap | 27.45 | kPa | 358.83 | Vapor-L... |
| Pvap | 27.47 | kPa | 358.86 | Solvent... |
| Pvap | 27.32 | kPa | 358.88 | Vapor-L... |
| Pvap | 27.45 | kPa | 359.01 | Vapor-L... |
| Pvap | 28.19 | kPa | 359.53 | Vapor-L... |
| Pvap | 28.67 | kPa | 359.91 | Vapor-L... |
| Pvap | 29.25 | kPa | 360.35 | Vapor-L... |
| Pvap | 29.41 | kPa | 360.50 | Vapor-L... |
| Pvap | 30.03 | kPa | 360.81 | Solvent... |
| Pvap | 30.29 | kPa | 361.12 | Vapor-L... |
| Pvap | 30.00 | kPa | 361.26 | Vapor p... |
| Pvap | 30.68 | kPa | 361.45 | Vapor-L... |
| Pvap | 31.59 | kPa | 362.10 | Vapor-L... |
| Pvap | 32.13 | kPa | 362.50 | Vapor-L... |
| Pvap | 32.55 | kPa | 362.76 | Solvent... |
| Pvap | 32.73 | kPa | 362.93 | Vapor-L... |
| Pvap | 33.35 | kPa | 363.38 | Vapor-L... |
| Pvap | 33.33 | kPa | 363.69 | Vapor p... |
| Pvap | 34.05 | kPa | 363.85 | Vapor-L... |
| Pvap | 34.64 | kPa | 364.28 | Vapor-L... |
| Pvap | 35.08 | kPa | 364.38 | Solvent... |
| Pvap | 35.47 | kPa | 364.84 | Vapor-L... |
| Pvap | 35.95 | kPa | 365.13 | Vapor-L... |
| Pvap | 36.71 | kPa | 365.62 | Vapor-L... |
| Pvap | 36.66 | kPa | 365.92 | Vapor p... |
| Pvap | 37.56 | kPa | 366.00 | Solvent... |
| Pvap | 37.32 | kPa | 366.01 | Vapor-L... |
| Pvap | 37.95 | kPa | 366.40 | Vapor-L... |
| Pvap | 38.64 | kPa | 366.86 | Vapor-L... |
| Pvap | 39.31 | kPa | 367.24 | Vapor-L... |
| Pvap | 40.03 | kPa | 367.49 | Solvent... |
| Pvap | 39.97 | kPa | 367.65 | Vapor-L... |
| Pvap | 40.00 | kPa | 368.00 | Vapor p... |
| Pvap | 40.64 | kPa | 368.06 | Vapor-L... |
| Pvap | 41.27 | kPa | 368.44 | Vapor-L... |
| Pvap | 41.96 | kPa | 368.85 | Vapor-L... |
| Pvap | 42.51 | kPa | 369.03 | Solvent... |
| Pvap | 42.73 | kPa | 369.31 | Vapor-L... |
| Pvap | 43.23 | kPa | 369.58 | Vapor-L... |
| Pvap | 44.05 | kPa | 370.05 | Vapor-L... |
| Pvap | 44.00 | kPa | 370.31 | Vapor p... |
| Pvap | 44.75 | kPa | 370.46 | Vapor-L... |
| Pvap | 45.07 | kPa | 370.52 | Solvent... |
| Pvap | 45.40 | kPa | 370.74 | Vapor-L... |
| Pvap | 45.91 | kPa | 371.07 | Vapor-L... |
| Pvap | 46.64 | kPa | 371.47 | Vapor-L... |
| Pvap | 47.54 | kPa | 371.77 | Solvent... |
| Pvap | 47.45 | kPa | 371.82 | Vapor-L... |
| Pvap | 47.93 | kPa | 372.15 | Vapor-L... |
| Pvap | 48.00 | kPa | 372.45 | Vapor p... |
| Pvap | 48.64 | kPa | 372.50 | Vapor-L... |
| Pvap | 49.31 | kPa | 372.91 | Vapor-L... |
| Pvap | 50.02 | kPa | 373.05 | Solvent... |
| Pvap | 49.87 | kPa | 373.16 | Vapor-L... |
| Pvap | 50.71 | kPa | 373.57 | Vapor-L... |
| Pvap | 51.25 | kPa | 373.88 | Vapor-L... |
| Pvap | 52.03 | kPa | 374.25 | Vapor-L... |
| Pvap | 52.58 | kPa | 374.33 | Solvent... |
| Pvap | 52.00 | kPa | 374.46 | Vapor p... |
| Pvap | 52.55 | kPa | 374.47 | Vapor-L... |
| Pvap | 53.37 | kPa | 374.85 | Vapor-L... |
| Pvap | 53.95 | kPa | 375.14 | Vapor-L... |
| Pvap | 54.67 | kPa | 375.44 | Vapor-L... |
| Pvap | 55.03 | kPa | 375.51 | Solvent... |
| Pvap | 55.37 | kPa | 375.83 | Vapor-L... |
| Pvap | 56.01 | kPa | 376.13 | Vapor-L... |
| Pvap | 55.99 | kPa | 376.35 | Vapor p... |
| Pvap | 56.71 | kPa | 376.47 | Vapor-L... |
| Pvap | 57.48 | kPa | 376.68 | Solvent... |
| Pvap | 57.36 | kPa | 376.74 | Vapor-L... |
| Pvap | 58.00 | kPa | 377.07 | Vapor-L... |
| Pvap | 58.64 | kPa | 377.32 | Vapor-L... |
| Pvap | 59.32 | kPa | 377.65 | Vapor-L... |
| Pvap | 60.03 | kPa | 377.81 | Solvent... |
| Pvap | 59.97 | kPa | 377.91 | Vapor-L... |
| Pvap | 59.99 | kPa | 378.13 | Vapor p... |
| Pvap | 60.67 | kPa | 378.22 | Vapor-L... |
| Pvap | 61.40 | kPa | 378.56 | Vapor-L... |
| Pvap | 61.97 | kPa | 378.81 | Vapor-L... |
| Pvap | 62.45 | kPa | 378.95 | Solvent... |
| Pvap | 62.61 | kPa | 379.04 | Vapor-L... |
| Pvap | 63.39 | kPa | 379.39 | Vapor-L... |
| Pvap | 63.91 | kPa | 379.60 | Vapor-L... |
| Pvap | 64.60 | kPa | 379.89 | Vapor-L... |
| Pvap | 65.05 | kPa | 379.97 | Solvent... |
| Pvap | 65.20 | kPa | 380.13 | Vapor-L... |
| Pvap | 65.33 | kPa | 380.36 | Vapor p... |
| Pvap | 65.99 | kPa | 380.47 | Vapor-L... |
| Pvap | 66.63 | kPa | 380.70 | Vapor-L... |
| Pvap | 67.31 | kPa | 381.00 | Vapor-L... |
| Pvap | 67.58 | kPa | 381.01 | Solvent... |
| Pvap | 68.01 | kPa | 381.26 | Vapor-L... |
| Pvap | 68.67 | kPa | 381.53 | Vapor-L... |
| Pvap | 69.31 | kPa | 381.76 | Vapor-L... |
| Pvap | 70.03 | kPa | 381.96 | Solvent... |
| Pvap | 70.21 | kPa | 382.08 | Vapor-L... |
| Pvap | 70.63 | kPa | 382.28 | Vapor-L... |
| Pvap | 70.66 | kPa | 382.45 | Vapor p... |
| Pvap | 71.31 | kPa | 382.55 | Vapor-L... |
| Pvap | 71.95 | kPa | 382.78 | Vapor-L... |
| Pvap | 72.56 | kPa | 382.90 | Solvent... |
| Pvap | 72.65 | kPa | 383.05 | Vapor-L... |
| Pvap | 73.35 | kPa | 383.29 | Vapor-L... |
| Pvap | 73.93 | kPa | 383.53 | Vapor-L... |
| Pvap | 74.63 | kPa | 383.76 | Vapor-L... |
| Pvap | 75.05 | kPa | 383.88 | Solvent... |
| Pvap | 75.48 | kPa | 384.09 | Vapor-L... |
| Pvap | 75.99 | kPa | 384.26 | Vapor-L... |
| Pvap | 75.99 | kPa | 384.42 | Vapor p... |
| Pvap | 76.63 | kPa | 384.50 | Vapor-L... |
| Pvap | 77.35 | kPa | 384.74 | Vapor-L... |
| Pvap | 77.59 | kPa | 384.79 | Solvent... |
| Pvap | 77.93 | kPa | 384.95 | Vapor-L... |
| Pvap | 79.27 | kPa | 385.42 | Vapor-L... |
| Pvap | 80.03 | kPa | 385.64 | Solvent... |
| Pvap | 80.00 | kPa | 385.65 | Vapor-L... |
| Pvap | 80.56 | kPa | 385.87 | Vapor-L... |
| Pvap | 81.79 | kPa | 386.24 | Vapor-L... |
| Pvap | 81.33 | kPa | 386.27 | Vapor p... |
| Pvap | 81.88 | kPa | 386.32 | Vapor-L... |
| Pvap | 82.68 | kPa | 386.54 | Vapor-L... |
| Pvap | 82.58 | kPa | 386.56 | Solvent... |
| Pvap | 83.23 | kPa | 386.76 | Vapor-L... |
| Pvap | 84.05 | kPa | 386.96 | Vapor-L... |
| Pvap | 85.01 | kPa | 387.35 | Solvent... |
| Pvap | 85.27 | kPa | 387.37 | Vapor-L... |
| Pvap | 86.61 | kPa | 387.80 | Vapor-L... |
| Pvap | 87.55 | kPa | 388.19 | Solvent... |
| Pvap | 88.00 | kPa | 388.23 | Vapor-L... |
| Pvap | 87.99 | kPa | 388.47 | Vapor p... |
| Pvap | 89.39 | kPa | 388.66 | Vapor-L... |
| Pvap | 90.09 | kPa | 389.00 | Solvent... |
| Pvap | 90.69 | kPa | 389.07 | Vapor-L... |
| Pvap | 92.16 | kPa | 389.51 | Vapor-L... |
| Pvap | 92.52 | kPa | 389.76 | Solvent... |
| Pvap | 93.44 | kPa | 389.90 | Vapor-L... |
| Pvap | 94.61 | kPa | 390.26 | Vapor-L... |
| Pvap | 94.66 | kPa | 390.53 | Vapor p... |
| Pvap | 95.02 | kPa | 390.55 | Solvent... |
| Pvap | 95.95 | kPa | 390.65 | Vapor-L... |
| Pvap | 97.27 | kPa | 391.05 | Vapor-L... |
| Pvap | 97.55 | kPa | 391.31 | Solvent... |
| Pvap | 97.33 | kPa | 391.32 | Vapor p... |
| Pvap | 98.71 | kPa | 391.46 | Vapor-L... |
| Pvap | 100.03 | kPa | 392.07 | Solvent... |
| Pvap | 101.38 | kPa | 392.26 | Solvent... |
| n0 | [1.37030; 1.40600] | [293.15; 318.15] |
|
|
| n0 | 1.40600 | 293.15 | Densiti... | |
| n0 | 1.40450 | 298.15 | Densiti... | |
| n0 | 1.40320 | 298.15 | Densiti... | |
| n0 | 1.40450 | 298.15 | Densiti... | |
| n0 | 1.40490 | 298.20 | Experim... | |
| n0 | 1.37240 | 303.15 | Densiti... | |
| n0 | 1.40216 | 303.15 | Liquid-... | |
| n0 | 1.37030 | 308.15 | Densiti... | |
| n0 | 1.39900 | 308.15 | Densiti... | |
| n0 | 1.39500 | 318.15 | Densiti... | |
| ρl | [770.37; 824.00] | kg/m3 | [273.65; 338.15] |
|
| ρl | 824.00 | kg/m3 | 273.65 | Tempera... |
| ρl | 823.60 | kg/m3 | 274.15 | Tempera... |
| ρl | 823.20 | kg/m3 | 274.65 | Tempera... |
| ρl | 822.80 | kg/m3 | 275.15 | Tempera... |
| ρl | 822.50 | kg/m3 | 275.65 | Tempera... |
| ρl | 822.10 | kg/m3 | 276.15 | Tempera... |
| ρl | 821.70 | kg/m3 | 276.65 | Tempera... |
| ρl | 821.30 | kg/m3 | 277.15 | Tempera... |
| ρl | 820.90 | kg/m3 | 277.65 | Tempera... |
| ρl | 820.60 | kg/m3 | 278.15 | Tempera... |
| ρl | 820.20 | kg/m3 | 278.65 | Tempera... |
| ρl | 819.80 | kg/m3 | 279.15 | Tempera... |
| ρl | 819.40 | kg/m3 | 279.65 | Tempera... |
| ρl | 819.10 | kg/m3 | 280.15 | Tempera... |
| ρl | 818.70 | kg/m3 | 280.65 | Tempera... |
| ρl | 818.30 | kg/m3 | 281.15 | Tempera... |
| ρl | 817.90 | kg/m3 | 281.65 | Tempera... |
| ρl | 817.50 | kg/m3 | 282.15 | Tempera... |
| ρl | 813.34 | kg/m3 | 288.15 | Densiti... |
| ρl | 813.27 | kg/m3 | 288.15 | Volumet... |
| ρl | 813.55 | kg/m3 | 288.15 | Densiti... |
| ρl | 810.10 | kg/m3 | 293.15 | Effect ... |
| ρl | 809.30 | kg/m3 | 293.15 | Studies... |
| ρl | 809.59 | kg/m3 | 293.15 | Densiti... |
| ρl | 809.30 | kg/m3 | 293.15 | Volumet... |
| ρl | 809.38 | kg/m3 | 293.15 | Densiti... |
| ρl | 809.30 | kg/m3 | 293.15 | Densiti... |
| ρl | 809.30 | kg/m3 | 293.15 | Evaluat... |
| ρl | 809.40 | kg/m3 | 293.15 | Acousti... |
| ρl | 809.30 | kg/m3 | 293.15 | Thermod... |
| ρl | 809.30 | kg/m3 | 293.15 | Influen... |
| ρl | 805.35 | kg/m3 | 298.15 | Densiti... |
| ρl | 805.37 | kg/m3 | 298.15 | The stu... |
| ρl | 806.57 | kg/m3 | 298.15 | Isobari... |
| ρl | 805.40 | kg/m3 | 298.15 | Thermod... |
| ρl | 805.05 | kg/m3 | 298.15 | Densiti... |
| ρl | 805.30 | kg/m3 | 298.15 | Thermod... |
| ρl | 805.37 | kg/m3 | 298.15 | Acousti... |
| ρl | 806.11 | kg/m3 | 298.15 | Excess ... |
| ρl | 805.30 | kg/m3 | 298.15 | Densiti... |
| ρl | 805.30 | kg/m3 | 298.15 | Influen... |
| ρl | 806.48 | kg/m3 | 298.15 | Excess ... |
| ρl | 805.30 | kg/m3 | 298.15 | Studies... |
| ρl | 805.27 | kg/m3 | 298.15 | Volumet... |
| ρl | 805.30 | kg/m3 | 298.15 | Evaluat... |
| ρl | 805.55 | kg/m3 | 298.15 | Densiti... |
| ρl | 805.37 | kg/m3 | 298.20 | Liquid-... |
| ρl | 801.16 | kg/m3 | 303.15 | Volumet... |
| ρl | 801.44 | kg/m3 | 303.15 | Densiti... |
| ρl | 801.24 | kg/m3 | 303.15 | Densiti... |
| ρl | 800.90 | kg/m3 | 303.15 | Thermod... |
| ρl | 801.20 | kg/m3 | 303.15 | Thermod... |
| ρl | 801.20 | kg/m3 | 303.15 | Influen... |
| ρl | 801.20 | kg/m3 | 303.15 | Densiti... |
| ρl | 801.20 | kg/m3 | 303.15 | Evaluat... |
| ρl | 800.88 | kg/m3 | 303.15 | Densiti... |
| ρl | 801.20 | kg/m3 | 303.15 | Studies... |
| ρl | 801.27 | kg/m3 | 303.15 | Acousti... |
| ρl | 796.97 | kg/m3 | 308.15 | Volumet... |
| ρl | 797.00 | kg/m3 | 308.15 | Thermod... |
| ρl | 796.90 | kg/m3 | 308.15 | Thermod... |
| ρl | 797.00 | kg/m3 | 308.15 | Densiti... |
| ρl | 796.89 | kg/m3 | 308.15 | Densiti... |
| ρl | 797.00 | kg/m3 | 308.15 | Studies... |
| ρl | 797.05 | kg/m3 | 308.15 | Densiti... |
| ρl | 797.00 | kg/m3 | 308.15 | Influen... |
| ρl | 797.25 | kg/m3 | 308.15 | Densiti... |
| ρl | 797.08 | kg/m3 | 308.15 | Acousti... |
| ρl | 798.00 | kg/m3 | 308.15 | Excess ... |
| ρl | 797.00 | kg/m3 | 308.15 | Evaluat... |
| ρl | 796.95 | kg/m3 | 308.15 | The stu... |
| ρl | 792.70 | kg/m3 | 313.15 | Volumet... |
| ρl | 792.62 | kg/m3 | 313.15 | Densiti... |
| ρl | 792.70 | kg/m3 | 313.15 | Influen... |
| ρl | 792.70 | kg/m3 | 313.15 | Evaluat... |
| ρl | 792.60 | kg/m3 | 313.15 | Thermod... |
| ρl | 792.70 | kg/m3 | 313.15 | Densiti... |
| ρl | 792.70 | kg/m3 | 313.15 | Studies... |
| ρl | 792.78 | kg/m3 | 313.15 | Densiti... |
| ρl | 792.98 | kg/m3 | 313.15 | Densiti... |
| ρl | 792.70 | kg/m3 | 313.15 | Thermod... |
| ρl | 788.40 | kg/m3 | 318.15 | Thermod... |
| ρl | 788.38 | kg/m3 | 318.15 | The stu... |
| ρl | 788.63 | kg/m3 | 318.15 | Densiti... |
| ρl | 788.40 | kg/m3 | 318.15 | Densiti... |
| ρl | 788.40 | kg/m3 | 318.15 | Studies... |
| ρl | 788.42 | kg/m3 | 318.15 | Densiti... |
| ρl | 788.40 | kg/m3 | 318.15 | Evaluat... |
| ρl | 788.40 | kg/m3 | 318.15 | Influen... |
| ρl | 784.00 | kg/m3 | 323.15 | Densiti... |
| ρl | 784.19 | kg/m3 | 323.15 | Densiti... |
| ρl | 783.99 | kg/m3 | 323.15 | Densiti... |
| ρl | 784.00 | kg/m3 | 323.15 | Studies... |
| ρl | 784.00 | kg/m3 | 323.15 | Thermod... |
| ρl | 784.00 | kg/m3 | 323.15 | Influen... |
| ρl | 784.00 | kg/m3 | 323.15 | Evaluat... |
| ρl | 779.67 | kg/m3 | 328.15 | Densiti... |
| ρl | 779.46 | kg/m3 | 328.15 | Densiti... |
| ρl | 779.17 | kg/m3 | 328.15 | The stu... |
| ρl | 775.07 | kg/m3 | 333.15 | Densiti... |
| ρl | 770.37 | kg/m3 | 338.15 | Densiti... |
| csound,fluid | [1168.10; 1286.70] | m/s | [283.15; 313.15] |
|
| csound,fluid | 1286.70 | m/s | 283.15 | Excess ... |
| csound,fluid | 1232.60 | m/s | 298.15 | Excess ... |
| csound,fluid | 1168.10 | m/s | 313.15 | Excess ... |
| γ | [0.02; 0.02] | N/m | [293.15; 323.15] |
|
| γ | 0.02 | N/m | 293.15 | Surface... |
| γ | 0.02 | N/m | 298.15 | Surface... |
| γ | 0.02 | N/m | 303.15 | Surface... |
| γ | 0.02 | N/m | 308.15 | Surface... |
| γ | 0.02 | N/m | 313.15 | Surface... |
| γ | 0.02 | N/m | 318.15 | Surface... |
| γ | 0.02 | N/m | 323.15 | Surface... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [304.46; 413.88] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.42610e+01 | |||
| Coefficient B | -2.72373e+03 | |||
| Coefficient C | -1.09535e+02 | |||
| Temperature range, min. | 304.46 | |||
| Temperature range, max. | 413.88 | |||
| Pvap | 1.33 | kPa | 304.46 | Calculated Property |
| Pvap | 3.03 | kPa | 316.62 | Calculated Property |
| Pvap | 6.28 | kPa | 328.78 | Calculated Property |
| Pvap | 12.07 | kPa | 340.93 | Calculated Property |
| Pvap | 21.71 | kPa | 353.09 | Calculated Property |
| Pvap | 36.95 | kPa | 365.25 | Calculated Property |
| Pvap | 59.92 | kPa | 377.41 | Calculated Property |
| Pvap | 93.17 | kPa | 389.56 | Calculated Property |
| Pvap | 139.66 | kPa | 401.72 | Calculated Property |
| Pvap | 202.67 | kPa | 413.88 | Calculated Property |
| Pvap | [5.64e-06; 3752.61] | kPa | [200.00; 552.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.30709e+02 | |||
| Coefficient B | -1.10289e+04 | |||
| Coefficient C | -1.66000e+01 | |||
| Coefficient D | 7.56865e-06 | |||
| Temperature range, min. | 200.00 | |||
| Temperature range, max. | 552.00 | |||
| Pvap | 5.64e-06 | kPa | 200.00 | Calculated Property |
| Pvap | 2.74e-03 | kPa | 239.11 | Calculated Property |
| Pvap | 0.17 | kPa | 278.22 | Calculated Property |
| Pvap | 3.01 | kPa | 317.33 | Calculated Property |
| Pvap | 24.15 | kPa | 356.44 | Calculated Property |
| Pvap | 114.22 | kPa | 395.56 | Calculated Property |
| Pvap | 375.23 | kPa | 434.67 | Calculated Property |
| Pvap | 954.14 | kPa | 473.78 | Calculated Property |
| Pvap | 2020.91 | kPa | 512.89 | Calculated Property |
| Pvap | 3752.61 | kPa | 552.00 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Pentanol.
Mixtures
- 2-Pentanol + Pentane, 2,2,4-trimethyl-
- 2-Pentanol + Heptane
- n-Hexane + 2-Pentanol
- 1-Hexene + 2-Pentanol
- 2-Pentanol + Benzene, 1,2,4-trimethyl-
- 2-Pentanol + Cyclohexane, methyl-
- Cyclopentane, methyl- + 2-Pentanol
- 2-Pentanol + Formamide
- 2-Pentanol + n-Butyl ether
- 2-Pentanol + Ethanamine, N-ethyl-
- 2-Pentanol + Cyclohexanamine, N-methyl-
- 5-Hydroxymethylfurfural + 2-Pentanol + Water
- 2-Pentanol + Water
- Propanal + 2-Pentanol
- 2-Pentanol + 1-Butanamine, N-butyl-
- 2-Pentanol + Diisopropylamine
- Furfural + 2-Pentanol
- Furan, 2-methyl- + 2-Pentanol
- Acetonitrile + 2-Pentanol
- 2-Pentanol + Ethane, 1,2-dichloro-
Find more mixtures with 2-Pentanol.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Vapor liquid equilibria for nitrogen with 2-propanol, 2-butanol, or 2-pentanol binary systems
- Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
- The influence of cation, anion and temperature on the liquid-liquid equilibrium of some pentanols-water system
- Thermodynamic behaviour of second generation biofuels: Vapour liquid equilibria and excess enthalpies of the binary mixtures 2-pentanol and n-heptane or 2,2,4-trimethylpentane
- Thermodynamics properties, VLE and HE, of the systems 2-pentanol and cyclohexane or methylbenzene for contributing to the knowledge of new biofuels
- Characterizing second generation biofuels: Excess enthalpies and vapour-liquid equilibria of the binary mixtures containing 1-pentanol or 2-pentanol and n-hexane
- Vapor-liquid equilibria and excess enthalpies of the binary systems 1- pentanol or 2-pentanol and 1-hexene or 1,2,4-trimethylbenzene for the development of biofuels
- Solubility of 1-methyl-4-nitropyrazole in seventeen pure solvents at temperatures from 283.15 K to 323.15 K
- Liquid-liquid equilibria of ternary and quaternary systems involving 5-hydroxymethylfurfural, water, organic solvents, and salts at 313.15 K and atmospheric pressure
- A thermodynamic study of the ketoreductase-catalyzed reduction of 2-alkanones in non-aqueous solvents
- Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in 1-pentanol, 2-pentanol and 3-pentanol
- Speeds of sound, isentropic compressibilities, viscosities and excess molar volumes of binary mixtures of methylcyclohexane + 2-alkanols or ethanol at T = 298.15 K
- Henry's law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-pentanol, 3-pentanol, 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
- Viscosity, density, and speed of sound of methylcyclopentane with primary and secondary alcohols at T = (293.15, 298.15, and 303.15) K
- Measurement and modeling of high-pressure (vapor + liquid) equilibria of (CO2 + alkanol) binary systems
- Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
- Excess molar enthalpies of the binary systems: (Dibutyl ether + isomers of pentanol) at T = (298.15 and 308.15) K
- Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
- Liquid-liquid equilibria for ternary mixtures of 1-alkyl-3-methyl imidazolium bis{(trifluoromethyl)sulfonyl}imides, n-hexane and organic compounds at 303.15 K and 0.1 MPa
- The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K
- Liquid-liquid equilibrium in systems used for the production of 5-hydroxymethylfurfural from biomass using alcohols as solvents
- Studies on physicochemical behavior of binary mixtures containing propanal and Alkan-2-ol
- Temperature of maximum density for aqueous mixtures of three pentanol isomers
- Phase equilibria of the water + 1-butanol + 2-pentanol ternary system at 101.3 kPa
- Acoustic, volumetric and spectral studies of binary liquid mixtures of aliphatic dialkylamine and 2-alkanols at different temperatures
- Effect of 1-ethyl-3-methylimidazolium tetrafluoroborate on the phase equilibria for systems containing 5-hydroxymethylfurfural, water, organic solvent in the absence and presence of sodium chloride
- Excess volumes and partial molar volumes of binary liquid mixtures of furfural or 2-methylfuran with alcohols at 298.15 K
- Experimental and modeling study of liquid phase equilibria for (water + phosphoric acid + sec-alcohols) systems
- Thermophysical study of binary mixtures of 1-butyl-3-methylimidazolium nitrate ionic liquid + alcohols at different temperatures
- Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
- Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
- Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
- Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
- Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
- Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
- Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
- Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
- Solubility in Binary Solvent Mixtures: Anthracene Dissolved in Alcohol + Acetonitrile Mixtures at 298.2 K
- Solubility in Binary Solvent Mixtures: Pyrene Dissolved in Alcohol + Acetonitrile Mixtures at 299.2 K
- Solubility in Binary Solvent Mixtures: Anthracene Dissolved in Alcohol + 2-Methyl-1-butanol Mixtures at 298.2 K
- Dynamic Viscosities of 2-Pentanol with Alkanes (Octane, Decane, and Dodecane) at Three Temperatures T ) (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO Interaction Parameters
- Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
- Measurement and Correlation of Vapor-Liquid Equilibria for Water + 2-Propanol, Water + 2-Butanol, and Water + 2-Pentanol Systems at High Temperatures and Pressures
- Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
- Excess Molar Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 1- or 2-Pentanol at (283.15, 298.15, and 313.15) K
- Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
- Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
- Densities and Viscosities of Binary Mixtures Containing Diethylene Glycol and 2-Alkanol
- Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
- Isobaric Vapor Liquid Equilibria of Binary Systems (Propyl Acetate + n-Pentanol), (Propyl Acetate + 1-Methyl-1-butanol), and (Propyl Acetate + 3-Methyl-1-butanol) at 101.3 kPa
- Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
- Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
- Measurement of Infinite Dilution Activity Coefficients of Alcohols, Ketones, and Aromatic Hydrocarbons in 4-Methyl-N-butylpyridinium Tetrafluoroborate and 1-Butyl-3-methylimidazolium Hexafluorophosphate by Gas-Liquid Chromatography
- Solubility of D(-)-p-Hydroxyphenylglycine Dane Salt in Eight Alcohols between (293 and 343) K
- Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
- Vapor-Liquid Equilibria in Binary Systems Formed by n-Hexane with Alcohols
- Densities, Viscosities, and Refractive Indices of Binary Mixtures of Acetophenone and 2-Alkanols
- Temperature Dependence of Limiting Activity Coefficients, Henry s Law Constants, and Related Infinite Dilution Properties of Branched Pentanols in Water. Measurement, Critical Compilation, Correlation, and Recommended Data
- Densities, Viscosities, and Refractive Indices of Binary Mixtures of Methyl Ethyl Ketone + Pentanol Isomers at Different Temperatures
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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