- InChI
- InChI=1S/C6H14O/c1-3-4-5-6(2)7/h6-7H,3-5H2,1-2H3
- InChI Key
- QNVRIHYSUZMSGM-UHFFFAOYSA-N
- Formula
- C6H14O
- SMILES
- CCCCC(C)O
- Molecular Weight1
- 102.17
- CAS
- 626-93-7
- Other Names
-
- 2-Hexyl alcohol
- 2-hydroxyhexane
- Hexan-2-ol
- Hexanol-(2)
- butylmethylcarbinol
- methyl butyl carbinol
- n-Butylmethylcarbinol
- n-C4H9CH(OH)CH3
- n-Hexan-2-ol
- sec-Hexyl alcohol
- 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).
- 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.
- 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.
- 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 |
|---|---|---|---|
| η | 0.0042040 | Pa×s | Speeds ... |
| ΔfG° | -139.62 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-335.60; -329.90] | kJ/mol |
|
| ΔfH°gas | -333.50 ± 2.20 | kJ/mol | NIST |
| ΔfH°gas | -335.60 ± 2.20 | kJ/mol | NIST |
| ΔfH°gas | -329.90 ± 2.10 | kJ/mol | NIST |
| ΔfH°liquid | [-394.10; -388.40] | kJ/mol |
|
| ΔfH°liquid | -392.00 ± 0.88 | kJ/mol | NIST |
| ΔfH°liquid | -394.10 ± 0.88 | kJ/mol | NIST |
| ΔfH°liquid | -388.40 ± 0.75 | kJ/mol | NIST |
| ΔfusH° | 11.86 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [57.00; 58.47] | kJ/mol |
|
| ΔvapH° | 58.47 | kJ/mol | NIST |
| ΔvapH° | 57.00 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 58.30 ± 0.30 | kJ/mol | NIST |
| IE | [9.80; 10.24] | eV |
|
| IE | 9.80 ± 0.03 | eV | NIST |
| IE | 10.24 | eV | NIST |
| log10WS | [-0.89; -0.89] |
|
|
| log10WS | -0.89 | Aq. Sol... | |
| log10WS | -0.89 | Estimat... | |
| logPoct/wat | 1.557 | Crippen Calculated Property | |
| McVol | 101.270 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| Pc | [3310.00; 3310.00] | kPa |
|
| Pc | 3310.00 | kPa | KDB |
| Pc | 3310.00 ± 20.00 | kPa | NIST |
| Pc | 3310.00 ± 20.00 | kPa | NIST |
| Pc | 3310.00 ± 20.00 | kPa | NIST |
| ρc | [265.65; 265.65] | kg/m3 |
|
| ρc | 265.65 ± 2.04 | kg/m3 | NIST |
| ρc | 265.65 ± 6.13 | kg/m3 | NIST |
| Inp | [128.24; 812.60] |
|
|
| Inp | 780.30 | NIST | |
| Inp | 777.70 | NIST | |
| Inp | 787.60 | NIST | |
| Inp | 775.90 | NIST | |
| Inp | 778.50 | NIST | |
| Inp | 803.10 | NIST | |
| Inp | 804.40 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 775.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 793.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 801.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 812.60 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | 811.00 | NIST | |
| Inp | 777.00 | NIST | |
| Inp | 777.00 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | 780.00 | NIST | |
| Inp | 795.00 | NIST | |
| Inp | 809.00 | NIST | |
| Inp | 774.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 793.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | 799.00 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | Outlier 128.24 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 780.30 | NIST | |
| Inp | 803.10 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 777.00 | NIST | |
| Inp | 809.00 | NIST | |
| I | [1179.00; 1254.00] |
|
|
| I | 1254.00 | NIST | |
| I | 1254.00 | NIST | |
| I | 1229.00 | NIST | |
| I | 1219.00 | NIST | |
| I | 1207.00 | NIST | |
| I | 1240.00 | NIST | |
| I | 1226.00 | NIST | |
| I | 1232.00 | NIST | |
| I | 1195.00 | NIST | |
| I | 1232.00 | NIST | |
| I | 1216.00 | NIST | |
| I | 1243.00 | NIST | |
| I | 1222.00 | NIST | |
| I | 1233.00 | NIST | |
| I | 1238.00 | NIST | |
| I | 1211.00 | NIST | |
| I | 1234.00 | NIST | |
| I | 1218.00 | NIST | |
| I | 1182.00 | NIST | |
| I | 1182.00 | NIST | |
| I | 1227.00 | NIST | |
| I | 1217.00 | NIST | |
| I | 1239.00 | NIST | |
| I | 1210.00 | NIST | |
| I | 1241.00 | NIST | |
| I | 1236.00 | NIST | |
| I | 1182.00 | NIST | |
| I | 1182.00 | NIST | |
| I | 1245.00 | NIST | |
| I | 1216.00 | NIST | |
| I | 1192.00 | NIST | |
| I | 1216.00 | NIST | |
| I | 1232.00 | NIST | |
| I | 1220.00 | NIST | |
| I | 1202.00 | NIST | |
| I | 1231.00 | NIST | |
| I | 1238.00 | NIST | |
| I | 1238.00 | NIST | |
| I | 1179.00 | NIST | |
| I | 1179.00 | NIST | |
| I | 1219.00 | NIST | |
| I | 1222.00 | NIST | |
| I | 1219.00 | NIST | |
| I | 1191.00 | NIST | |
| I | 1232.00 | NIST | |
| I | 1192.00 | NIST | |
| I | 1192.00 | NIST | |
| I | 1192.00 | NIST | |
| I | 1195.00 | NIST | |
| I | 1233.00 | NIST | |
| I | 1238.00 | NIST | |
| I | 1226.00 | NIST | |
| I | 1232.00 | NIST | |
| Tboil | [409.15; 413.35] | K |
|
| Tboil | 411.00 | K | KDB |
| Tboil | 409.20 | K | NIST |
| Tboil | 413.00 | K | NIST |
| Tboil | 411.15 ± 2.00 | K | NIST |
| Tboil | 411.65 ± 1.50 | K | NIST |
| Tboil | 413.15 ± 0.50 | K | NIST |
| Tboil | 413.05 ± 0.50 | K | NIST |
| Tboil | 411.15 ± 3.00 | K | NIST |
| Tboil | 412.65 ± 2.00 | K | NIST |
| Tboil | 410.15 ± 3.00 | K | NIST |
| Tboil | 412.55 ± 1.00 | K | NIST |
| Tboil | 411.65 ± 3.00 | K | NIST |
| Tboil | 409.65 ± 2.00 | K | NIST |
| Tboil | 412.65 ± 1.00 | K | NIST |
| Tboil | 409.15 ± 2.00 | K | NIST |
| Tboil | 411.65 ± 2.00 | K | NIST |
| Tboil | 412.95 ± 0.30 | K | NIST |
| Tboil | 411.65 ± 2.00 | K | NIST |
| Tboil | 413.35 ± 0.50 | K | NIST |
| Tboil | 412.65 ± 1.00 | K | NIST |
| Tboil | 410.15 ± 2.00 | K | NIST |
| Tboil | 412.65 ± 0.70 | K | NIST |
| Tboil | 410.65 ± 2.00 | K | NIST |
| Tboil | 409.15 ± 2.00 | K | NIST |
| Tboil | 409.15 ± 2.00 | K | NIST |
| Tc | [568.20; 586.20] | K |
|
| Tc | 585.90 | K | KDB |
| Tc | 585.90 ± 0.50 | K | NIST |
| Tc | 585.40 ± 0.60 | K | NIST |
| Tc | 585.40 ± 0.60 | K | NIST |
| Tc | 585.80 | K | NIST |
| Tc | 586.01 ± 0.30 | K | NIST |
| Tc | Outlier 568.20 | K | NIST |
| Tc | 586.20 ± 0.30 | K | NIST |
| Tfus | 203.20 | K | Joback Calculated Property |
| Vc | [0.384; 0.384] | m3/kmol |
|
| Vc | 0.384 | m3/kmol | KDB |
| Vc | 0.384 | m3/kmol | NIST |
| Zc | 0.2609150 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [207.74; 261.25] | J/mol×K | [428.42; 592.97] |
|
| Cp,gas | 207.74 | J/mol×K | 428.42 | Joback Calculated Property |
| Cp,gas | 217.54 | J/mol×K | 455.85 | Joback Calculated Property |
| Cp,gas | 226.97 | J/mol×K | 483.27 | Joback Calculated Property |
| Cp,gas | 236.05 | J/mol×K | 510.70 | Joback Calculated Property |
| Cp,gas | 244.78 | J/mol×K | 538.12 | Joback Calculated Property |
| Cp,gas | 253.18 | J/mol×K | 565.55 | Joback Calculated Property |
| Cp,gas | 261.25 | J/mol×K | 592.97 | Joback Calculated Property |
| Cp,liquid | [256.31; 260.34] | J/mol×K | [298.15; 298.15] |
|
| Cp,liquid | 256.31 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 260.34 | J/mol×K | 298.15 | NIST |
| η | [0.0016400; 0.0041010] | Pa×s | [298.15; 323.15] |
|
| η | 0.0041010 | Pa×s | 298.15 | Densiti... |
| η | 0.0041010 | Pa×s | 298.15 | Densiti... |
| η | 0.0034110 | Pa×s | 303.15 | Densiti... |
| η | 0.0032300 | Pa×s | 303.15 | Density... |
| η | 0.0034110 | Pa×s | 303.15 | Densiti... |
| η | 0.0028190 | Pa×s | 308.15 | Densiti... |
| η | 0.0028190 | Pa×s | 308.15 | Densiti... |
| η | 0.0022900 | Pa×s | 313.15 | Density... |
| η | 0.0022190 | Pa×s | 313.15 | Densiti... |
| η | 0.0022190 | Pa×s | 313.15 | Densiti... |
| η | 0.0016400 | Pa×s | 323.15 | Density... |
| ΔvapH | [41.01; 61.80] | kJ/mol | [273.50; 413.00] |
|
| ΔvapH | 61.80 | kJ/mol | 273.50 | NIST |
| ΔvapH | 56.80 ± 0.20 | kJ/mol | 313.00 | NIST |
| ΔvapH | 55.00 ± 0.20 | kJ/mol | 328.00 | NIST |
| ΔvapH | 53.00 ± 0.20 | kJ/mol | 343.00 | NIST |
| ΔvapH | 49.70 | kJ/mol | 355.50 | NIST |
| ΔvapH | 50.70 ± 0.20 | kJ/mol | 358.00 | NIST |
| ΔvapH | 53.10 | kJ/mol | 358.00 | NIST |
| ΔvapH | 49.20 ± 0.20 | kJ/mol | 368.00 | NIST |
| ΔvapH | 52.40 | kJ/mol | 375.00 | NIST |
| ΔvapH | 47.80 | kJ/mol | 381.50 | NIST |
| ΔvapH | 48.70 | kJ/mol | 387.50 | NIST |
| ΔvapH | 41.01 | kJ/mol | 413.00 | NIST |
| Pvap | [0.04; 0.69] | kPa | [274.50; 309.40] |
|
| Pvap | 0.04 | kPa | 274.50 | Measure... |
| Pvap | 0.04 | kPa | 275.50 | Measure... |
| Pvap | 0.05 | kPa | 276.30 | Measure... |
| Pvap | 0.05 | kPa | 276.50 | Measure... |
| Pvap | 0.06 | kPa | 278.30 | Measure... |
| Pvap | 0.06 | kPa | 279.50 | Measure... |
| Pvap | 0.07 | kPa | 281.30 | Measure... |
| Pvap | 0.08 | kPa | 282.20 | Measure... |
| Pvap | 0.08 | kPa | 282.50 | Measure... |
| Pvap | 0.10 | kPa | 284.30 | Measure... |
| Pvap | 0.10 | kPa | 285.40 | Measure... |
| Pvap | 0.10 | kPa | 285.50 | Measure... |
| Pvap | 0.12 | kPa | 287.50 | Measure... |
| Pvap | 0.13 | kPa | 288.40 | Measure... |
| Pvap | 0.16 | kPa | 290.50 | Measure... |
| Pvap | 0.17 | kPa | 291.40 | Measure... |
| Pvap | 0.18 | kPa | 292.10 | Measure... |
| Pvap | 0.19 | kPa | 293.20 | Measure... |
| Pvap | 0.20 | kPa | 293.40 | Measure... |
| Pvap | 0.21 | kPa | 294.40 | Measure... |
| Pvap | 0.25 | kPa | 296.20 | Measure... |
| Pvap | 0.26 | kPa | 296.50 | Measure... |
| Pvap | 0.27 | kPa | 297.40 | Measure... |
| Pvap | 0.33 | kPa | 299.50 | Measure... |
| Pvap | 0.34 | kPa | 300.40 | Measure... |
| Pvap | 0.41 | kPa | 302.50 | Measure... |
| Pvap | 0.42 | kPa | 303.40 | Measure... |
| Pvap | 0.52 | kPa | 305.50 | Measure... |
| Pvap | 0.53 | kPa | 306.40 | Measure... |
| Pvap | 0.60 | kPa | 307.60 | Measure... |
| Pvap | 0.69 | kPa | 309.40 | Measure... |
| n0 | [1.40770; 1.41350] | [293.15; 308.15] |
|
|
| n0 | 1.41350 | 293.15 | Densiti... | |
| n0 | 1.41160 | 298.15 | Densiti... | |
| n0 | 1.41160 | 298.15 | Densiti... | |
| n0 | 1.40930 | 303.15 | Densiti... | |
| n0 | 1.40770 | 308.15 | Densiti... | |
| ρl | [784.60; 818.06] | kg/m3 | [288.15; 328.15] |
|
| ρl | 818.06 | kg/m3 | 288.15 | Volumet... |
| ρl | 816.00 | kg/m3 | 293.00 | KDB |
| ρl | 814.17 | kg/m3 | 293.15 | Volumet... |
| ρl | 810.23 | kg/m3 | 298.15 | Volumet... |
| ρl | 810.84 | kg/m3 | 298.15 | Study o... |
| ρl | 810.14 | kg/m3 | 298.15 | Densiti... |
| ρl | 810.17 | kg/m3 | 298.15 | The stu... |
| ρl | 810.84 | kg/m3 | 298.15 | Densiti... |
| ρl | 810.10 | kg/m3 | 298.15 | Thermod... |
| ρl | 806.23 | kg/m3 | 303.15 | Volumet... |
| ρl | 806.10 | kg/m3 | 303.15 | Thermod... |
| ρl | 806.13 | kg/m3 | 303.15 | Densiti... |
| ρl | 802.10 | kg/m3 | 308.15 | Thermod... |
| ρl | 802.06 | kg/m3 | 308.15 | Densiti... |
| ρl | 801.75 | kg/m3 | 308.15 | Densiti... |
| ρl | 801.94 | kg/m3 | 308.15 | The stu... |
| ρl | 802.16 | kg/m3 | 308.15 | Volumet... |
| ρl | 798.00 | kg/m3 | 313.15 | Thermod... |
| ρl | 798.04 | kg/m3 | 313.15 | Volumet... |
| ρl | 797.96 | kg/m3 | 313.15 | Densiti... |
| ρl | 793.57 | kg/m3 | 318.15 | The stu... |
| ρl | 784.60 | kg/m3 | 328.15 | The stu... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 313.13 | 1010.00 | 799.26 |
| 313.13 | 2006.00 | 800.05 |
| 313.13 | 2999.00 | 800.83 |
| 313.13 | 4008.00 | 801.59 |
| 313.13 | 4999.00 | 802.35 |
| 313.13 | 5986.00 | 803.12 |
| 313.13 | 7000.00 | 803.86 |
| 313.13 | 8010.00 | 804.64 |
| 313.13 | 9026.00 | 805.38 |
| 313.13 | 10004.00 | 806.09 |
| 313.13 | 11005.00 | 806.84 |
| 313.13 | 12001.00 | 807.56 |
| 313.13 | 13010.00 | 808.28 |
| 313.13 | 14002.00 | 808.98 |
| 313.13 | 14998.00 | 809.67 |
| 313.13 | 16001.00 | 810.39 |
| 313.13 | 17006.00 | 811.08 |
| 313.13 | 18000.00 | 811.7 |
| 313.13 | 19005.00 | 812.39 |
| 313.13 | 20015.00 | 813.1 |
| 313.13 | 21029.00 | 813.74 |
| 313.13 | 22004.00 | 814.4 |
| 323.09 | 1037.00 | 791.0 |
| 323.09 | 2000.00 | 791.79 |
| 323.09 | 3010.00 | 792.63 |
| 323.09 | 4029.00 | 793.48 |
| 323.09 | 5004.00 | 794.27 |
| 323.09 | 6020.00 | 795.1 |
| 323.09 | 7007.00 | 795.84 |
| 323.09 | 8009.00 | 796.68 |
| 323.09 | 9017.00 | 797.48 |
| 323.09 | 10003.00 | 798.25 |
| 323.09 | 11001.00 | 799.0 |
| 323.09 | 12000.00 | 799.77 |
| 323.09 | 13021.00 | 800.56 |
| 323.09 | 14001.00 | 801.3 |
| 323.09 | 15002.00 | 802.0 |
| 323.09 | 16000.00 | 802.74 |
| 323.09 | 17004.00 | 803.48 |
| 323.09 | 18008.00 | 804.21 |
| 323.09 | 19001.00 | 804.9 |
| 323.09 | 20011.00 | 805.62 |
| 323.09 | 21003.00 | 806.31 |
| 323.09 | 22004.00 | 807.01 |
| 333.04 | 1055.00 | 782.56 |
| 333.04 | 2007.00 | 783.43 |
| 333.04 | 3005.00 | 784.28 |
| 333.04 | 4007.00 | 785.21 |
| 333.04 | 5015.00 | 786.06 |
| 333.04 | 6009.00 | 786.93 |
| 333.04 | 7006.00 | 787.77 |
| 333.04 | 7998.00 | 788.61 |
| 333.04 | 9006.00 | 789.47 |
| 333.04 | 10004.00 | 790.32 |
| 333.04 | 11007.00 | 791.11 |
| 333.04 | 12012.00 | 791.93 |
| 333.04 | 13003.00 | 792.72 |
| 333.04 | 14008.00 | 793.51 |
| 333.04 | 15005.00 | 794.3 |
| 333.04 | 16001.00 | 795.06 |
| 333.04 | 17006.00 | 795.85 |
| 333.04 | 18010.00 | 796.61 |
| 333.04 | 19002.00 | 797.35 |
| 333.04 | 20000.00 | 798.08 |
| 333.04 | 21000.00 | 798.82 |
| 333.04 | 22004.00 | 799.56 |
| 342.98 | 1032.00 | 774.05 |
| 342.98 | 2015.00 | 775.01 |
| 342.98 | 3012.00 | 775.95 |
| 342.98 | 4017.00 | 776.87 |
| 342.98 | 5013.00 | 777.79 |
| 342.98 | 6012.00 | 778.72 |
| 342.98 | 7025.00 | 779.62 |
| 342.98 | 8000.00 | 780.47 |
| 342.98 | 9000.00 | 781.35 |
| 342.98 | 9996.00 | 782.25 |
| 342.98 | 11020.00 | 783.12 |
| 342.98 | 11999.00 | 783.92 |
| 342.98 | 12996.00 | 784.76 |
| 342.98 | 14007.00 | 785.6 |
| 342.98 | 15003.00 | 786.41 |
| 342.98 | 16005.00 | 787.17 |
| 342.98 | 17002.00 | 787.98 |
| 342.98 | 18010.00 | 788.76 |
| 342.98 | 19005.00 | 789.49 |
| 342.98 | 20010.00 | 790.27 |
| 342.98 | 21006.00 | 791.0 |
| 342.98 | 22005.00 | 791.75 |
| 352.86 | 1053.00 | 765.06 |
| 352.86 | 2014.00 | 766.05 |
| 352.86 | 3019.00 | 767.09 |
| 352.86 | 4033.00 | 768.08 |
| 352.86 | 4996.00 | 769.01 |
| 352.86 | 6006.00 | 770.06 |
| 352.86 | 7013.00 | 771.02 |
| 352.86 | 8004.00 | 771.95 |
| 352.86 | 9035.00 | 772.93 |
| 352.86 | 10009.00 | 773.84 |
| 352.86 | 11007.00 | 774.75 |
| 352.86 | 12007.00 | 775.66 |
| 352.86 | 12999.00 | 776.54 |
| 352.86 | 14012.00 | 777.47 |
| 352.86 | 15010.00 | 778.33 |
| 352.86 | 16003.00 | 779.21 |
| 352.86 | 17002.00 | 780.07 |
| 352.86 | 18017.00 | 780.92 |
| 352.86 | 19005.00 | 781.75 |
| 352.86 | 20014.00 | 782.58 |
| 352.86 | 21013.00 | 783.39 |
| 352.86 | 22010.00 | 784.18 |
| 362.73 | 1075.00 | 754.97 |
| 362.73 | 2006.00 | 756.02 |
| 362.73 | 3018.00 | 757.16 |
| 362.73 | 4034.00 | 758.26 |
| 362.73 | 5016.00 | 759.29 |
| 362.73 | 6066.00 | 760.41 |
| 362.73 | 6998.00 | 761.37 |
| 362.73 | 8041.00 | 762.44 |
| 362.73 | 9014.00 | 763.43 |
| 362.73 | 10001.00 | 764.37 |
| 362.73 | 11026.00 | 765.39 |
| 362.73 | 12000.00 | 766.35 |
| 362.73 | 13010.00 | 767.31 |
| 362.73 | 13999.00 | 768.28 |
| 362.73 | 15006.00 | 769.21 |
| 362.73 | 16006.00 | 770.12 |
| 362.73 | 17005.00 | 771.02 |
| 362.73 | 18000.00 | 771.92 |
| 362.73 | 19003.00 | 772.82 |
| 362.73 | 20017.00 | 773.7 |
| 362.73 | 21006.00 | 774.56 |
| 362.73 | 22010.00 | 775.42 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [314.79; 434.35] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.50376e+01 | |||
| Coefficient B | -3.41427e+03 | |||
| Coefficient C | -8.33130e+01 | |||
| Temperature range, min. | 314.79 | |||
| Temperature range, max. | 434.35 | |||
| Pvap | 1.33 | kPa | 314.79 | Calculated Property |
| Pvap | 2.97 | kPa | 328.07 | Calculated Property |
| Pvap | 6.09 | kPa | 341.36 | Calculated Property |
| Pvap | 11.64 | kPa | 354.64 | Calculated Property |
| Pvap | 20.94 | kPa | 367.93 | Calculated Property |
| Pvap | 35.75 | kPa | 381.21 | Calculated Property |
| Pvap | 58.31 | kPa | 394.50 | Calculated Property |
| Pvap | 91.37 | kPa | 407.78 | Calculated Property |
| Pvap | 138.22 | kPa | 421.07 | Calculated Property |
| Pvap | 202.63 | kPa | 434.35 | Calculated Property |
| Pvap | [9.61e-05; 3339.22] | kPa | [223.00; 586.20] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.05887e+02 | |||
| Coefficient B | -1.03384e+04 | |||
| Coefficient C | -1.27495e+01 | |||
| Coefficient D | 3.27083e-06 | |||
| Temperature range, min. | 223.00 | |||
| Temperature range, max. | 586.20 | |||
| Pvap | 9.61e-05 | kPa | 223.00 | Calculated Property |
| Pvap | 0.01 | kPa | 263.36 | Calculated Property |
| Pvap | 0.48 | kPa | 303.71 | Calculated Property |
| Pvap | 5.80 | kPa | 344.07 | Calculated Property |
| Pvap | 36.42 | kPa | 384.42 | Calculated Property |
| Pvap | 146.08 | kPa | 424.78 | Calculated Property |
| Pvap | 426.73 | kPa | 465.13 | Calculated Property |
| Pvap | 990.25 | kPa | 505.49 | Calculated Property |
| Pvap | 1938.28 | kPa | 545.84 | Calculated Property |
| Pvap | 3339.22 | kPa | 586.20 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Hexanol.
Mixtures
- Toluene + 2-Hexanol
- 2-Hexanol + Cyclohexane, methyl-
- Decane + 2-Hexanol
- 2-Hexanol + Formamide
- Cyclohexanamine, N-methyl- + 2-Hexanol
- Acetonitrile + 2-Hexanol
- 2-Hexanol + Ethane, 1,2-dichloro-
- 2-Butanone + 2-Hexanol
- 1-Butanamine + 2-Hexanol
- Cyclohexanone + 2-Hexanol
- N,N-Dimethylacetamide + 2-Hexanol
- Acetophenone + 2-Hexanol
- Nitrogen + 2-Hexanol
- 2-Hexanol + Ethanol, 2,2'-oxybis-
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Vapor liquid equilibria for nitrogen with 2-hexanol, 2-heptanol, or 2-octanol binary systems
- Densities, viscosities and ultrasonic velocities of binary mixtures of methylbenzene with hexan-2-ol, heptan-2-ol and octan-2-ol at T = 298.15 and 308.15K
- A thermodynamic study of the ketoreductase-catalyzed reduction of 2-alkanones in non-aqueous solvents
- Speeds of sound, isentropic compressibilities, viscosities and excess molar volumes of binary mixtures of methylcyclohexane + 2-alkanols or ethanol at T = 298.15 K
- Study of thermodynamic and transport properties of binary liquid mixtures of n-decane with hexan-2-ol, heptan-2-ol and octan-2-ol at T = 298.15 K. Experimental results and application of the Prigogine-Flory-Patterson theory
- Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
- The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K
- 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
- Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
- Density and Viscosity Measurement of n-Butylamine with Hexyl Alcohol Isomer Binary Systems
- Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
- Densities and Viscosities of Binary Mixtures Containing Diethylene Glycol and 2-Alkanol
- Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
- 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
- Densities, Viscosities, and Refractive Indices of Binary Mixtures of Acetophenone and 2-Alkanols
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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