- InChI
- InChI=1S/C8H18O/c1-3-5-6-8(4-2)7-9/h8-9H,3-7H2,1-2H3
- InChI Key
- YIWUKEYIRIRTPP-UHFFFAOYSA-N
- Formula
- C8H18O
- SMILES
- CCCCC(CC)CO
- Molecular Weight1
- 130.23
- CAS
- 104-76-7
- Other Names
-
- 2-EH
- 2-Ethyl-1-hexanol
- 2-Ethyl-1-hexyl alcohol
- 2-Ethyl-hexanol-1
- 2-Ethylhexan-1-ol
- 2-Ethylhexanol
- 2-Ethylhexyl alcohol
- Ethyl-1-hexanol,2-
- Ethylhexanol
- Ethylhexyl alcohol
- Hexan-1-ol, 2-ethyl
- Hexanol, 2-ethyl-
- NSC 9300
- OCTYL 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).
- 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).
- 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.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | -5287.78 ± 0.79 | kJ/mol | NIST |
| μ | 1.80 | debye | KDB |
| ΔfG° | -122.78 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-367.50; -365.50] | kJ/mol |
|
| ΔfH°gas | -365.50 | kJ/mol | KDB |
| ΔfH°gas | -367.50 ± 2.20 | kJ/mol | NIST |
| ΔfH°liquid | -432.88 ± 0.79 | kJ/mol | NIST |
| ΔfusH° | 17.04 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 68.50 ± 0.20 | kJ/mol | NIST |
| log10WS | [-2.11; -2.11] |
|
|
| log10WS | -2.11 | Aq. Sol... | |
| log10WS | -2.11 | Estimat... | |
| logPoct/wat | 2.195 | Crippen Calculated Property | |
| McVol | 129.450 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | [2800.00; 2800.00] | kPa |
|
| Pc | 2800.00 | kPa | KDB |
| Pc | 2800.00 ± 100.00 | kPa | NIST |
| Pc | 2800.00 ± 200.00 | kPa | NIST |
| Inp | [164.40; 1064.00] |
|
|
| Inp | 992.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 1015.00 | NIST | |
| Inp | 1017.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 990.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1010.70 | NIST | |
| Inp | 1010.70 | NIST | |
| Inp | 1026.30 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1045.00 | NIST | |
| Inp | 1015.20 | NIST | |
| Inp | 1016.90 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1014.90 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 1038.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1049.00 | NIST | |
| Inp | 1038.00 | NIST | |
| Inp | 1038.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 1016.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1027.00 | NIST | |
| Inp | 1018.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1027.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 980.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1026.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1043.00 | NIST | |
| Inp | 1024.00 | NIST | |
| Inp | 1026.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 998.00 | NIST | |
| Inp | 1014.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1016.10 | NIST | |
| Inp | 1015.00 | NIST | |
| Inp | 1038.00 | NIST | |
| Inp | 1012.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1012.00 | NIST | |
| Inp | 1012.00 | NIST | |
| Inp | 1015.00 | NIST | |
| Inp | 1018.00 | NIST | |
| Inp | 1016.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1015.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1008.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 1015.00 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1043.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1038.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1015.00 | NIST | |
| Inp | 1015.00 | NIST | |
| Inp | 1014.00 | NIST | |
| Inp | 1018.00 | NIST | |
| Inp | 1018.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | Outlier 164.40 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1015.00 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1038.00 | NIST | |
| Inp | 1014.00 | NIST | |
| I | [1441.00; 1522.00] |
|
|
| I | 1484.00 | NIST | |
| I | 1484.00 | NIST | |
| I | 1484.00 | NIST | |
| I | 1488.00 | NIST | |
| I | 1499.00 | NIST | |
| I | 1484.00 | NIST | |
| I | 1480.00 | NIST | |
| I | 1496.00 | NIST | |
| I | 1470.00 | NIST | |
| I | 1481.00 | NIST | |
| I | Outlier 1441.00 | NIST | |
| I | 1484.00 | NIST | |
| I | 1505.00 | NIST | |
| I | 1517.00 | NIST | |
| I | 1491.00 | NIST | |
| I | Outlier 1453.00 | NIST | |
| I | 1484.00 | NIST | |
| I | Outlier 1446.00 | NIST | |
| I | 1491.00 | NIST | |
| I | 1479.00 | NIST | |
| I | 1491.00 | NIST | |
| I | 1474.00 | NIST | |
| I | 1492.00 | NIST | |
| I | Outlier 1522.00 | NIST | |
| I | 1494.00 | NIST | |
| I | 1493.00 | NIST | |
| I | 1502.00 | NIST | |
| I | 1490.00 | NIST | |
| I | 1493.00 | NIST | |
| I | Outlier 1444.00 | NIST | |
| I | 1495.00 | NIST | |
| I | 1473.00 | NIST | |
| I | 1491.00 | NIST | |
| I | 1491.00 | NIST | |
| I | 1494.00 | NIST | |
| I | 1489.00 | NIST | |
| I | 1491.00 | NIST | |
| I | Outlier 1449.00 | NIST | |
| I | 1493.00 | NIST | |
| I | 1492.00 | NIST | |
| I | 1492.00 | NIST | |
| I | 1496.00 | NIST | |
| I | 1483.00 | NIST | |
| I | 1492.00 | NIST | |
| I | 1488.00 | NIST | |
| I | 1518.00 | NIST | |
| I | 1504.00 | NIST | |
| I | 1488.00 | NIST | |
| I | 1490.00 | NIST | |
| I | 1490.00 | NIST | |
| I | 1481.00 | NIST | |
| I | 1474.00 | NIST | |
| I | 1518.00 | NIST | |
| I | 1490.00 | NIST | |
| I | 1489.00 | NIST | |
| I | Outlier 1450.00 | NIST | |
| I | 1502.00 | NIST | |
| I | 1503.00 | NIST | |
| I | 1503.00 | NIST | |
| I | 1490.00 | NIST | |
| I | 1486.00 | NIST | |
| I | 1483.00 | NIST | |
| I | 1462.00 | NIST | |
| I | 1488.00 | NIST | |
| I | 1503.00 | NIST | |
| I | 1484.00 | NIST | |
| I | 1501.00 | NIST | |
| I | 1494.00 | NIST | |
| I | 1474.00 | NIST | |
| I | 1495.00 | NIST | |
| I | 1472.00 | NIST | |
| I | 1515.00 | NIST | |
| I | 1505.00 | NIST | |
| I | 1476.00 | NIST | |
| I | 1476.00 | NIST | |
| I | 1512.00 | NIST | |
| I | 1499.00 | NIST | |
| I | 1484.00 | NIST | |
| I | 1490.00 | NIST | |
| I | 1487.00 | NIST | |
| I | 1495.00 | NIST | |
| I | 1484.00 | NIST | |
| I | 1495.00 | NIST | |
| I | 1496.00 | NIST | |
| I | 1503.00 | NIST | |
| I | 1503.00 | NIST | |
| I | 1502.00 | NIST | |
| I | 1491.00 | NIST | |
| I | 1493.00 | NIST | |
| I | 1509.00 | NIST | |
| I | 1481.00 | NIST | |
| I | 1475.00 | NIST | |
| I | 1509.00 | NIST | |
| I | 1492.00 | NIST | |
| I | 1490.00 | NIST | |
| I | 1492.00 | NIST | |
| I | 1458.00 | NIST | |
| I | 1495.00 | NIST | |
| I | 1490.00 | NIST | |
| I | 1505.00 | NIST | |
| I | 1491.00 | NIST | |
| I | 1483.00 | NIST | |
| I | 1461.00 | NIST | |
| I | 1487.00 | NIST | |
| I | 1491.00 | NIST | |
| I | Outlier 1453.00 | NIST | |
| I | Outlier 1453.00 | NIST | |
| I | Outlier 1453.00 | NIST | |
| I | 1491.00 | NIST | |
| I | 1515.00 | NIST | |
| I | Outlier 1520.00 | NIST | |
| I | 1483.00 | NIST | |
| I | 1491.00 | NIST | |
| I | 1496.00 | NIST | |
| I | 1495.00 | NIST | |
| I | 1492.00 | NIST | |
| I | 1502.00 | NIST | |
| I | 1496.00 | NIST | |
| I | 1504.00 | NIST | |
| I | 1492.00 | NIST | |
| I | 1493.00 | NIST | |
| I | 1494.00 | NIST | |
| I | 1485.00 | NIST | |
| I | 1489.00 | NIST | |
| I | 1491.00 | NIST | |
| I | 1489.00 | NIST | |
| I | 1492.00 | NIST | |
| I | 1492.00 | NIST | |
| I | 1489.00 | NIST | |
| I | 1486.00 | NIST | |
| I | 1495.00 | NIST | |
| I | 1494.00 | NIST | |
| I | 1493.00 | NIST | |
| I | 1489.00 | NIST | |
| I | 1496.00 | NIST | |
| I | 1496.00 | NIST | |
| I | 1496.00 | NIST | |
| I | 1496.00 | NIST | |
| I | 1496.00 | NIST | |
| I | 1480.00 | NIST | |
| I | 1495.00 | NIST | |
| I | 1518.00 | NIST | |
| I | 1476.00 | NIST | |
| I | 1481.00 | NIST | |
| I | 1482.00 | NIST | |
| I | 1470.00 | NIST | |
| I | 1492.00 | NIST | |
| I | 1465.00 | NIST | |
| I | 1502.00 | NIST | |
| I | 1483.00 | NIST | |
| I | 1501.00 | NIST | |
| I | 1515.00 | NIST | |
| I | 1499.00 | NIST | |
| I | 1484.00 | NIST | |
| I | 1475.00 | NIST | |
| I | 1458.00 | NIST | |
| I | Outlier 1453.00 | NIST | |
| S°liquid | 347.00 | J/mol×K | NIST |
| Tboil | [457.77; 458.20] | K |
|
| Tboil | 457.77 | K | KDB |
| Tboil | 458.20 | K | (Liquid... |
| Tc | [640.20; 641.00] | K |
|
| Tc | 640.60 | K | KDB |
| Tc | 641.00 ± 1.00 | K | NIST |
| Tc | 641.00 ± 2.00 | K | NIST |
| Tc | 640.20 ± 0.30 | K | NIST |
| Tfus | 203.00 | K | KDB |
| Vc | 0.496 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [290.23; 354.79] | J/mol×K | [474.18; 637.10] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 290 300 310 320 330 340 350 360 500 550 600 | ||||
| Cp,gas | 290.23 | J/mol×K | 474.18 | Joback Calculated Property |
| Cp,gas | 302.08 | J/mol×K | 501.33 | Joback Calculated Property |
| Cp,gas | 313.47 | J/mol×K | 528.49 | Joback Calculated Property |
| Cp,gas | 324.43 | J/mol×K | 555.64 | Joback Calculated Property |
| Cp,gas | 334.96 | J/mol×K | 582.79 | Joback Calculated Property |
| Cp,gas | 345.08 | J/mol×K | 609.94 | Joback Calculated Property |
| Cp,gas | 354.79 | J/mol×K | 637.10 | Joback Calculated Property |
| Cp,liquid | 317.50 | J/mol×K | 298.15 | NIST |
| η | [0.0001689; 0.1178389] | Pa×s | [225.74; 474.18] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 0.02 0.04 0.06 0.08 0.1 0.12 300 400 | ||||
| η | 0.1178389 | Pa×s | 225.74 | Joback Calculated Property |
| η | 0.0169844 | Pa×s | 267.15 | Joback Calculated Property |
| η | 0.0041171 | Pa×s | 308.55 | Joback Calculated Property |
| η | 0.0013956 | Pa×s | 349.96 | Joback Calculated Property |
| η | 0.0005948 | Pa×s | 391.37 | Joback Calculated Property |
| η | 0.0002984 | Pa×s | 432.77 | Joback Calculated Property |
| η | 0.0001689 | Pa×s | 474.18 | Joback Calculated Property |
| ΔvapH | [52.70; 60.20] | kJ/mol | [385.50; 402.00] |
|
| ΔvapH | 52.70 | kJ/mol | 385.50 | NIST |
| ΔvapH | 60.20 | kJ/mol | 402.00 | NIST |
| Pvap | [0.02; 103.26] | kPa | [293.80; 458.24] |
|
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 300 350 400 450 | ||||
| Pvap | 0.02 | kPa | 293.80 | Measure... |
| Pvap | 0.02 | kPa | 298.70 | Measure... |
| Pvap | 0.03 | kPa | 301.60 | Measure... |
| Pvap | 0.04 | kPa | 304.50 | Measure... |
| Pvap | 0.05 | kPa | 307.40 | Measure... |
| Pvap | 0.07 | kPa | 310.30 | Measure... |
| Pvap | 0.09 | kPa | 313.30 | Measure... |
| Pvap | 0.11 | kPa | 316.30 | Measure... |
| Pvap | 0.14 | kPa | 319.20 | Measure... |
| Pvap | 0.17 | kPa | 322.20 | Measure... |
| Pvap | 0.22 | kPa | 325.20 | Measure... |
| Pvap | 0.28 | kPa | 328.20 | Measure... |
| Pvap | 0.34 | kPa | 331.20 | Measure... |
| Pvap | 9.88 | kPa | 389.76 | Vapor L... |
| Pvap | 19.88 | kPa | 407.11 | Vapor L... |
| Pvap | 30.03 | kPa | 418.24 | Vapor L... |
| Pvap | 39.67 | kPa | 426.95 | Vapor L... |
| Pvap | 40.00 | kPa | 427.20 | Isobari... |
| Pvap | 45.05 | kPa | 430.79 | Vapor L... |
| Pvap | 49.22 | kPa | 433.51 | Vapor L... |
| Pvap | 55.52 | kPa | 437.24 | Vapor L... |
| Pvap | 59.61 | kPa | 439.49 | Vapor L... |
| Pvap | 64.64 | kPa | 442.12 | Vapor L... |
| Pvap | 70.55 | kPa | 445.00 | Vapor L... |
| Pvap | 75.01 | kPa | 447.04 | Vapor L... |
| Pvap | 79.55 | kPa | 449.02 | Vapor L... |
| Pvap | 84.49 | kPa | 451.06 | Vapor L... |
| Pvap | 99.44 | kPa | 456.77 | Vapor L... |
| Pvap | 102.20 | kPa | 457.83 | Vapor L... |
| Pvap | 102.91 | kPa | 458.23 | Vapor L... |
| Pvap | 103.26 | kPa | 458.24 | Vapor L... |
| n0 | [1.42920; 1.43100] | [293.10; 298.20] |
|
|
|
T(K) Refractive Index 1.43 1.43 1.43 1.43 294 296 298 | ||||
| n0 | 1.43100 | 293.10 | Phase E... | |
| n0 | 1.43100 | 293.10 | Vapor-L... | |
| n0 | 1.42920 | 298.15 | Acousti... | |
| n0 | 1.42930 | 298.20 | Solubil... | |
| n0 | 1.42930 | 298.20 | Tie-lin... | |
| ρl | [821.68; 833.00] | kg/m3 | [293.00; 308.15] |
|
| ρl | 833.00 | kg/m3 | 293.00 | KDB |
| ρl | 829.07 | kg/m3 | 298.15 | Densiti... |
| ρl | 825.39 | kg/m3 | 303.15 | Densiti... |
| ρl | 821.68 | kg/m3 | 308.15 | Densiti... |
| csound,fluid | [1318.07; 1318.44] | m/s | [298.15; 298.15] |
|
| csound,fluid | 1318.07 | m/s | 298.15 | Densiti... |
| csound,fluid | 1318.44 | m/s | 298.15 | Densiti... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [349.00; 482.60] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.43882e+01 | |||
| Coefficient B | -3.40352e+03 | |||
| Coefficient C | -1.07630e+02 | |||
| Temperature range, min. | 349.00 | |||
| Temperature range, max. | 482.60 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 349.00 | Calculated Property |
| Pvap | 3.02 | kPa | 363.84 | Calculated Property |
| Pvap | 6.25 | kPa | 378.69 | Calculated Property |
| Pvap | 11.99 | kPa | 393.53 | Calculated Property |
| Pvap | 21.57 | kPa | 408.38 | Calculated Property |
| Pvap | 36.73 | kPa | 423.22 | Calculated Property |
| Pvap | 59.63 | kPa | 438.07 | Calculated Property |
| Pvap | 92.85 | kPa | 452.91 | Calculated Property |
| Pvap | 139.39 | kPa | 467.76 | Calculated Property |
| Pvap | 202.63 | kPa | 482.60 | Calculated Property |
| Pvap | [7.91e-10; 2836.74] | kPa | [203.15; 640.25] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 3.04517e+02 | |||
| Coefficient B | -2.04556e+04 | |||
| Coefficient C | -4.24888e+01 | |||
| Coefficient D | 2.42482e-05 | |||
| Temperature range, min. | 203.15 | |||
| Temperature range, max. | 640.25 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 200 400 600 | ||||
| Pvap | 7.91e-10 | kPa | 203.15 | Calculated Property |
| Pvap | 4.10e-05 | kPa | 251.72 | Calculated Property |
| Pvap | 0.02 | kPa | 300.28 | Calculated Property |
| Pvap | 1.08 | kPa | 348.85 | Calculated Property |
| Pvap | 13.20 | kPa | 397.42 | Calculated Property |
| Pvap | 72.22 | kPa | 445.98 | Calculated Property |
| Pvap | 244.60 | kPa | 494.55 | Calculated Property |
| Pvap | 626.49 | kPa | 543.12 | Calculated Property |
| Pvap | 1378.79 | kPa | 591.68 | Calculated Property |
| Pvap | 2836.74 | kPa | 640.25 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Hexanol, 2-ethyl-.
Mixtures
- Benzene + 1-Hexanol, 2-ethyl-
- Benzene, chloro- + 1-Hexanol, 2-ethyl-
- Benzene, bromo- + 1-Hexanol, 2-ethyl-
- Butanoic acid + 1-Hexanol, 2-ethyl- + Water
- 1-Butanol + 1-Hexanol, 2-ethyl-
- 2-Propanol, 2-methyl- + 1-Hexanol, 2-ethyl-
- 1-Hexanol, 2-ethyl- + Water
- 1-Hexanol, 2-ethyl- + Propanoic acid + Water
- 1-Hexanol, 2-ethyl- + Phenol + Water
- Methyl Isobutyl Ketone + 1-Hexanol, 2-ethyl-
- p-Xylene + 1-Hexanol, 2-ethyl-
- 2-Pyrrolidinone, 1-methyl- + 1-Hexanol, 2-ethyl-
- Heptane, 3-(chloromethyl)- + 1-Hexanol, 2-ethyl-
- Formic acid + 1-Hexanol, 2-ethyl-
- Formamide, N,N-dimethyl- + 1-Hexanol, 2-ethyl-
- Toluene + 1-Hexanol, 2-ethyl-
- 1-Pentanol + 1-Hexanol, 2-ethyl-
- 1,2-Ethanediol + 1-Hexanol, 2-ethyl-
- Carbon dioxide + Hexanoic acid, 2-ethyl- + 1-Hexanol, 2-ethyl-
- Carbon dioxide + 1-Hexanol, 2-ethyl-
Find more mixtures with 1-Hexanol, 2-ethyl-.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Ethyl-1-hexanol with Benzene and Halobenzenes
- Isobaric vapor liquid phase equilibria for the binary systems of tert-butanol + 2-ethyl-1-hexanol and n-butanol + 2-ethyl-1-hexanol
- The co-solubility of 2-ethylhexanoic acid and some liquid alcohols in supercritical carbon dioxide
- Liquid liquid equilibria of (water + 2,3-butanediol + 2-ethyl-1-hexanol) at several temperatures
- Phase equilibria in ternary aqueous mixtures of 1,3-butanediol with 2-ethyl-1-hexanol at T = (298.2, 303.2 and 308.2) K
- Experimental and correlated tie-line data for aqueous mixtures of 2-butanol with 2-ethyl-1-hexanol at various temperatures
- Solubility and tie line data for the aqueous solutions of butyric acid with 1-octanol and 2-ethyl-1-hexanol at various temperatures
- Solubility and dissolution characteristics of capecitabine in pure lower alcohols and water with methanol mixture solvents at atmospheric pressure and different temperatures
- (Liquid + liquid) equilibria for (water + acetic acid + 2-ethyl- 1-hexanol): experimental data and prediction
- (Liquid + liquid) equilibria of (water + propionic acid + 2-ethyl-1-hexanol): Experimental data and correlation
- Phase diagrams for (water + 1, 2-butanediol or 1, 2-propanediol + 2-ethyl-1-hexanol) systems: Experimental data and UNIQUAC
- Tie-line data for the aqueous solutions of phenol with organic solvents at T = 298.2 K
- Measurement and Correlation of the Solubility of Florfenicol Form A in Several Pure and Binary Solvents
- Liquid-Liquid Equilibria for the Ternary Systems of Water + Thioglycolic Acid + 2-Ethyl-1-hexyl Thioglycolate and Water + 2-Ethyl-1-hexyl Thioglycolate + 2-Ethyl-1-hexanol at 293.15, 303.15, and 313.15 K under 101 kPa
- Liquid-Liquid Equilibria for the Ternary and Quaternary Systems of Water + Trimethylolpropane + (2-Ethylhexan-1-ol/Octan-1-ol) + Formaldehyde at 298.15 K
- Solubility of 2-Ethyl-1-hexanol, 2-Ethylhexanoic Acid, and Their Mixtures in Supercritical Carbon Dioxide
- Liquid-Liquid Equilibria of Water + 1-Butanol + 2-Ethyl-1-hexanol System
- 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
- Acoustic and Thermodynamic Properties of 2-Ethyl-1-hexanol by Means of High-Pressure Speed of Sound Measurements at Temperatures from (293 to 318) K and Pressures up to 101 MPa
- Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
- Isobaric Vapor Liquid Equilibria for Binary Systems Comprising 1-Chloro-2-ethylhexane, 2-Ethyl-1-hexanol, p-Xylene, and N-Methylpyrrolidone (NMP) at 40.0 kPa
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Experimental Vapor Liquid Equilibria for the Systems {2-Ethyl-1-hexanol + Glycerol + CO2} and {2-Methyl-2-propanol + Glycerol + CO2}
- Phase Equilibria of Binary Systems Comprising Formic Acid, N,N-Dimethylformamide, 1-Chloro-2-ethylhexane, and 2-Ethyl-1-hexanol
- Vapor-Liquid Equilibria of Binary Systems Comprising 1-Chloro-2-ethylhexane and 2-Ethyl-1-hexanol
- Experimental and Theoretical Study of the Phase Equilibria in Ternary Aqueous Mixtures of 1,4-Butanediol with Alcohols at 298.2 K
- Densities, Speeds of Sound, and Isentropic Compressibilities for Binary Mixtures of 2-Ethyl-1-hexanol with 1-Pentanol, 1-Heptanol, or 1-Nonanol at the Temperature 298.15 K
- Densities, Speeds of Sound, and Isentropic Compressibilities for Binary Mixtures of 1,2-Ethanediol with 2-Ethyl-1-hexanol, 1-Heptanol, or Ethanol at the Temperature 298.15 K and Densities for Mixtures of 1,2-Ethanediol with 1-Nonanol at the Temperatures (293.15 and 298.15) K
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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