- InChI
- InChI=1S/C6H12O/c7-6-4-2-1-3-5-6/h6-7H,1-5H2
- InChI Key
- HPXRVTGHNJAIIH-UHFFFAOYSA-N
- Formula
- C6H12O
- SMILES
- OC1CCCCC1
- Molecular Weight1
- 100.16
- CAS
- 108-93-0
- Other Names
-
- 1-Cyclohexanol
- ADRONAL
- ANOL
- Adronol
- CYCLOHEXYL ALCOHOL
- Cicloesanolo
- Cyclohexane, hydroxy-
- Cykloheksanol
- Hexahydrophenol
- Hexalin
- Hydralin
- Hydrophenol
- Hydroxycyclohexane
- NSC 403656
- Naxol
- Phenol, hexahydro-
- ω : Acentric Factor.
- Tig : Autoignition Temperature (K).
- 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).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Rg : Radius of Gyration.
- 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 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.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase 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).
- Tboil : Boiling point at given pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.5280 | KDB | |
| Tig | 573.15 | K | KDB |
| μ | 1.70 | debye | KDB |
| Tflash,cc | 344.26 | K | KDB |
| Tflash,oc | 340.93 | K | KDB |
| ΔfG° | -118.00 | kJ/mol | KDB |
| Rg | 3.4340 | KDB | |
| ΔfH°gas | -294.80 | kJ/mol | KDB |
| ΔfH°liquid | [-359.20; -347.40] | kJ/mol |
|
| ΔfH°liquid | -352.00 ± 0.67 | kJ/mol | NIST |
| ΔfH°liquid | -350.00 ± 2.00 | kJ/mol | NIST |
| ΔfH°liquid | -347.40 ± 2.20 | kJ/mol | NIST |
| ΔfH°liquid | -349.20 ± 0.20 | kJ/mol | NIST |
| ΔfH°liquid | -359.20 | kJ/mol | NIST |
| ΔfusH° | 7.22 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 46.06 | kJ/mol | Joback Calculated Property |
| IE | [9.75; 10.00] | eV |
|
| IE | 9.75 | eV | NIST |
| IE | 10.00 ± 0.20 | eV | NIST |
| IE | 10.00 | eV | NIST |
| log10WS | [-0.44; -0.44] |
|
|
| log10WS | -0.44 | Aq. Sol... | |
| log10WS | -0.44 | Estimat... | |
| logPoct/wat | 1.311 | Crippen Calculated Property | |
| McVol | 90.410 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [3749.02; 4401.00] | kPa |
|
| Pc | 4260.00 | kPa | KDB |
| Pc | 4080.00 ± 150.00 | kPa | NIST |
| Pc | 4401.00 ± 25.00 | kPa | NIST |
| Pc | 4260.00 ± 50.00 | kPa | NIST |
| Pc | 4260.00 ± 50.00 | kPa | NIST |
| Pc | Outlier 3749.02 ± 151.99 | kPa | NIST |
| ρc | 300.48 ± 10.02 | kg/m3 | NIST |
| Inp | [849.00; 928.00] |
|
|
| Inp | 851.10 | NIST | |
| Inp | Outlier 921.10 | NIST | |
| Inp | 852.90 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 891.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 898.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 861.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 891.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | Outlier 928.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 899.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | Outlier 913.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 874.00 | NIST | |
| I | [1375.00; 1430.00] |
|
|
| I | 1377.00 | NIST | |
| I | 1386.00 | NIST | |
| I | 1396.00 | NIST | |
| I | Outlier 1430.00 | NIST | |
| I | 1403.00 | NIST | |
| I | 1386.00 | NIST | |
| I | 1410.00 | NIST | |
| I | 1375.00 | NIST | |
| I | 1376.00 | NIST | |
| I | 1414.00 | NIST | |
| I | 1407.00 | NIST | |
| I | 1408.00 | NIST | |
| I | 1378.00 | NIST | |
| I | 1410.00 | NIST | |
| I | 1403.00 | NIST | |
| I | 1403.00 | NIST | |
| I | 1403.00 | NIST | |
| I | 1393.00 | NIST | |
| I | 1375.00 | NIST | |
| I | 1392.00 | NIST | |
| I | 1375.00 | NIST | |
| I | 1375.00 | NIST | |
| I | 1375.00 | NIST | |
| I | 1375.00 | NIST | |
| I | 1394.00 | NIST | |
| I | 1375.00 | NIST | |
| I | 1392.00 | NIST | |
| I | 1400.00 | NIST | |
| I | 1375.00 | NIST | |
| I | 1375.00 | NIST | |
| S°gas | 353.83 | J/mol×K | NIST |
| S°liquid | [199.60; 203.87] | J/mol×K |
|
| S°liquid | 203.87 | J/mol×K | NIST |
| S°liquid | 199.60 | J/mol×K | NIST |
| Tboil | [433.73; 433.99] | K |
|
| Tboil | 433.99 | K | KDB |
| Tboil | 433.73 | K | A New T... |
| Tboil | 433.89 | K | Isobari... |
| Tc | 650.10 | K | KDB |
| Tfus | [296.62; 298.80] | K |
|
| Tfus | 298.61 | K | KDB |
| Tfus | 296.62 | K | Aq. Sol... |
| Tfus | 297.20 | K | Vapour ... |
| Tfus | 298.80 | K | Vapor P... |
| Ttriple | [297.00; 299.09] | K |
|
| Ttriple | 299.09 ± 0.02 | K | NIST |
| Ttriple | 297.00 ± 0.20 | K | NIST |
| Vc | 0.324 | m3/kmol | Joback Calculated Property |
| Zra | 0.24 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [188.35; 256.55] | J/mol×K | [448.41; 643.39] |
|
| Cp,gas | 188.35 | J/mol×K | 448.41 | Joback Calculated Property |
| Cp,gas | 201.24 | J/mol×K | 480.91 | Joback Calculated Property |
| Cp,gas | 213.50 | J/mol×K | 513.40 | Joback Calculated Property |
| Cp,gas | 225.15 | J/mol×K | 545.90 | Joback Calculated Property |
| Cp,gas | 236.19 | J/mol×K | 578.39 | Joback Calculated Property |
| Cp,gas | 246.66 | J/mol×K | 610.89 | Joback Calculated Property |
| Cp,gas | 256.55 | J/mol×K | 643.39 | Joback Calculated Property |
| Cp,liquid | [174.90; 274.70] | J/mol×K | [290.00; 357.94] |
|
| Cp,liquid | 174.90 | J/mol×K | 290.00 | NIST |
| Cp,liquid | 212.00 | J/mol×K | 297.95 | NIST |
| Cp,liquid | 220.10 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 209.03 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 209.99 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 214.06 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 213.59 | J/mol×K | 300.00 | NIST |
| Cp,liquid | 218.30 | J/mol×K | 305.05 | Heat ca... |
| Cp,liquid | 202.50 | J/mol×K | 305.10 | NIST |
| Cp,liquid | 218.60 | J/mol×K | 305.18 | Heat ca... |
| Cp,liquid | 224.00 | J/mol×K | 310.00 | Heat ca... |
| Cp,liquid | 223.80 | J/mol×K | 310.00 | Heat ca... |
| Cp,liquid | 229.70 | J/mol×K | 315.00 | Heat ca... |
| Cp,liquid | 229.60 | J/mol×K | 315.00 | Heat ca... |
| Cp,liquid | 235.30 | J/mol×K | 320.00 | Heat ca... |
| Cp,liquid | 235.50 | J/mol×K | 320.00 | Heat ca... |
| Cp,liquid | 241.10 | J/mol×K | 325.00 | Heat ca... |
| Cp,liquid | 241.30 | J/mol×K | 325.00 | Heat ca... |
| Cp,liquid | 246.80 | J/mol×K | 330.00 | Heat ca... |
| Cp,liquid | 246.70 | J/mol×K | 330.00 | Heat ca... |
| Cp,liquid | 252.00 | J/mol×K | 335.00 | Heat ca... |
| Cp,liquid | 252.20 | J/mol×K | 335.00 | Heat ca... |
| Cp,liquid | 257.60 | J/mol×K | 340.00 | Heat ca... |
| Cp,liquid | 257.40 | J/mol×K | 340.00 | Heat ca... |
| Cp,liquid | 263.00 | J/mol×K | 345.00 | Heat ca... |
| Cp,liquid | 262.80 | J/mol×K | 345.00 | Heat ca... |
| Cp,liquid | 268.00 | J/mol×K | 350.00 | Heat ca... |
| Cp,liquid | 268.00 | J/mol×K | 350.00 | Heat ca... |
| Cp,liquid | 272.50 | J/mol×K | 355.00 | Heat ca... |
| Cp,liquid | 272.30 | J/mol×K | 355.00 | Heat ca... |
| Cp,liquid | 274.70 | J/mol×K | 357.82 | Heat ca... |
| Cp,liquid | 274.70 | J/mol×K | 357.94 | Heat ca... |
| η | [0.0002419; 0.0966465] | Pa×s | [225.58; 448.41] |
|
| η | 0.0966465 | Pa×s | 225.58 | Joback Calculated Property |
| η | 0.0175844 | Pa×s | 262.72 | Joback Calculated Property |
| η | 0.0048796 | Pa×s | 299.86 | Joback Calculated Property |
| η | 0.0017962 | Pa×s | 337.00 | Joback Calculated Property |
| η | 0.0008063 | Pa×s | 374.13 | Joback Calculated Property |
| η | 0.0004183 | Pa×s | 411.27 | Joback Calculated Property |
| η | 0.0002419 | Pa×s | 448.41 | Joback Calculated Property |
| ΔfusH | [1.70; 8.21] | kJ/mol | [263.50; 298.20] |
|
| ΔfusH | 8.21 | kJ/mol | 263.50 | NIST |
| ΔfusH | 1.70 | kJ/mol | 297.00 | NIST |
| ΔfusH | 1.70 | kJ/mol | 297.00 | NIST |
| ΔfusH | 1.73 | kJ/mol | 298.20 | NIST |
| ΔsubH | 60.70 | kJ/mol | 285.00 | NIST |
| ΔvapH | [45.44; 62.70] | kJ/mol | [308.00; 433.70] |
|
| ΔvapH | 61.20 ± 0.60 | kJ/mol | 308.00 | NIST |
| ΔvapH | 60.40 | kJ/mol | 309.00 | NIST |
| ΔvapH | 58.40 | kJ/mol | 338.00 | NIST |
| ΔvapH | 54.80 | kJ/mol | 364.50 | NIST |
| ΔvapH | 62.70 | kJ/mol | 367.00 | NIST |
| ΔvapH | 59.90 | kJ/mol | 376.00 | NIST |
| ΔvapH | 60.10 | kJ/mol | 377.50 | NIST |
| ΔvapH | 52.60 | kJ/mol | 400.00 | NIST |
| ΔvapH | 55.00 | kJ/mol | 403.00 | NIST |
| ΔvapH | 49.80 | kJ/mol | 410.00 | NIST |
| ΔvapH | 49.30 | kJ/mol | 418.00 | NIST |
| ΔvapH | 45.44 | kJ/mol | 431.70 | NIST |
| ΔvapH | 45.48 | kJ/mol | 433.70 | KDB |
| Pvap | [0.50; 100.05] | kPa | [322.25; 433.38] |
|
| Pvap | 0.50 | kPa | 322.25 | VLE and... |
| Pvap | 1.00 | kPa | 330.95 | VLE and... |
| Pvap | 2.00 | kPa | 341.70 | VLE and... |
| Pvap | 3.95 | kPa | 353.80 | VLE and... |
| Pvap | 7.90 | kPa | 367.25 | VLE and... |
| Pvap | 15.85 | kPa | 382.40 | VLE and... |
| Pvap | 31.75 | kPa | 399.50 | VLE and... |
| Pvap | 63.75 | kPa | 419.05 | VLE and... |
| Pvap | 100.05 | kPa | 433.30 | VLE and... |
| Pvap | 99.00 | kPa | 433.38 | Vapor-L... |
| n0 | [1.46320; 1.46480] | [293.15; 303.15] |
|
|
| n0 | 1.46390 | 293.15 | Phase e... | |
| n0 | 1.46480 | 293.20 | Phase E... | |
| n0 | 1.46320 | 303.15 | Experim... | |
| ρl | [941.40; 961.50] | kg/m3 | [293.10; 303.20] |
|
| ρl | 941.40 | kg/m3 | 293.10 | Vapor-L... |
| ρl | 961.50 | kg/m3 | 298.15 | Determi... |
| ρl | 942.00 | kg/m3 | 303.00 | KDB |
| ρl | 941.42 | kg/m3 | 303.20 | Optimiz... |
| ΔfusS | [5.72; 31.14] | J/mol×K | [263.50; 297.00] |
|
| ΔfusS | 31.14 | J/mol×K | 263.50 | NIST |
| ΔfusS | 5.72 | J/mol×K | 297.00 | NIST |
| csound,fluid | [1370.80; 1443.20] | m/s | [303.15; 318.15] |
|
| csound,fluid | 1443.20 | m/s | 303.15 | Densiti... |
| csound,fluid | 1419.60 | m/s | 308.15 | Densiti... |
| csound,fluid | 1395.20 | m/s | 313.15 | Densiti... |
| csound,fluid | 1370.80 | m/s | 318.15 | Densiti... |
| γ | [0.03; 0.03] | N/m | [293.15; 323.15] |
|
| γ | 0.03 | N/m | 293.15 | Surface... |
| γ | 0.03 | N/m | 298.15 | Surface... |
| γ | 0.03 | N/m | 303.15 | Surface... |
| γ | 0.03 | N/m | 308.15 | Surface... |
| γ | 0.03 | N/m | 313.15 | Surface... |
| γ | 0.03 | N/m | 313.20 | KDB |
| γ | 0.03 | N/m | 318.15 | Surface... |
| γ | 0.03 | N/m | 323.15 | Surface... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | [341.68; 417.16] | K | [2.00; 60.00] |
|
| Tboil | 341.68 | K | 2.00 | A New T... |
| Tboil | 372.00 | K | 10.00 | A New T... |
| Tboil | 387.67 | K | 20.00 | A New T... |
| Tboil | 417.16 | K | 60.00 | A New T... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [333.32; 457.63] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.45470e+01 | |||
| Coefficient B | -3.25877e+03 | |||
| Coefficient C | -1.04780e+02 | |||
| Temperature range, min. | 333.32 | |||
| Temperature range, max. | 457.63 | |||
| Pvap | 1.33 | kPa | 333.32 | Calculated Property |
| Pvap | 3.01 | kPa | 347.13 | Calculated Property |
| Pvap | 6.21 | kPa | 360.94 | Calculated Property |
| Pvap | 11.90 | kPa | 374.76 | Calculated Property |
| Pvap | 21.41 | kPa | 388.57 | Calculated Property |
| Pvap | 36.48 | kPa | 402.38 | Calculated Property |
| Pvap | 59.29 | kPa | 416.19 | Calculated Property |
| Pvap | 92.47 | kPa | 430.01 | Calculated Property |
| Pvap | 139.09 | kPa | 443.82 | Calculated Property |
| Pvap | 202.63 | kPa | 457.63 | Calculated Property |
| Pvap | [0.09; 3779.27] | kPa | [296.60; 625.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.29104e+02 | |||
| Coefficient B | -1.18780e+04 | |||
| Coefficient C | -1.61598e+01 | |||
| Coefficient D | 5.55366e-06 | |||
| Temperature range, min. | 296.60 | |||
| Temperature range, max. | 625.15 | |||
| Pvap | 0.09 | kPa | 296.60 | Calculated Property |
| Pvap | 1.22 | kPa | 333.11 | Calculated Property |
| Pvap | 8.86 | kPa | 369.61 | Calculated Property |
| Pvap | 40.68 | kPa | 406.12 | Calculated Property |
| Pvap | 134.18 | kPa | 442.62 | Calculated Property |
| Pvap | 347.23 | kPa | 479.13 | Calculated Property |
| Pvap | 750.11 | kPa | 515.63 | Calculated Property |
| Pvap | 1414.27 | kPa | 552.14 | Calculated Property |
| Pvap | 2404.74 | kPa | 588.64 | Calculated Property |
| Pvap | 3779.27 | kPa | 625.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Cyclohexanol.
Mixtures
- Cyclohexanol + Water
- Cyclohexanol + 1-Propanol + Water
- Cyclohexanol + Cyclohexanone
- Cyclohexanol + Methyl Alcohol
- Cyclohexanol + 1-Propanol
- Cyclohexanol + 1-Butanol
- Cyclohexanol + Ethanol
- Cyclohexanol + Isopropyl Alcohol
- Cyclohexanol + Butanoic acid, 3-methyl- + Water
- Cyclohexanol + 2-Pyrrolidinone, 1-methyl-
- Cyclohexanol + Hexanedioic acid + Cyclohexanone
- Cyclohexanol + Hexanedioic acid
- Cyclohexanol + Toluene + Water
- Cyclohexanol + p-Xylene + Water
- Cyclohexanol + 3-Penten-2-one, 4-methyl- + Water
- Cyclohexanol + Cyclohexane
- Cyclohexanol + Cyclopentanol
- Cyclohexanol + 2-Hexanone
- Cyclohexanol + 2-Hexanone + Nonane
- Cyclohexanol + 2-Furanmethanol, tetrahydro- + Water
Find more mixtures with Cyclohexanol.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Phase equilibria of water + 1-propanol + solvent (n-amyl acetate, cyclohexanol, and cyclohexyl acetate) at T = 298.2K
- Vapour liquid equilibria, azeotropic data, excess enthalpies, activity coefficients at infinite dilution and solid liquid equilibria for binary alcohol ketone systems
- "Vapor-liquid" equilibrium measurements and modeling for the cyclohexane + cyclohexanol binary system
- Liquid-liquid equilibrium for the system water + 1,4-dioxane + cyclohexanol over the temperature range of 313.2 - 343.2 K
- Measurement on the solubility of adipic acid in various solvents at high temperature and its thermodynamics parameters.
- Distribution of cyclohexanol and cyclohexanone between water and cyclohexane
- Solubilities of adipic acid in binary cyclohexanone + cyclohexanol, cyclohexane + cyclohexanol, and cyclohexane + cyclohexanone solvent mixtures
- Measurement and prediction of liquid-liquid equilibria in ternary systems containing water, an organic component, and cyclohexanol
- Gas solubility of carbon dioxide and of oxygen in cyclohexanol by experiment and molecular simulation
- Experimental study on the calorimetric data of cyclohexanol with alkanols (C1-C4) and correlation with Wilson, NRTL and UNIQUAC models at 300 K
- Phase equilibria of ternary systems (water + pyruvic acid + high boiling alcohol). Thermodynamic modeling and optimization of extraction
- Optimization and modeling of extraction equilibria of the type 2 ternary systems containing (water + isovaleric acid + solvent)
- Densities, Viscosities, Sound Speed, and IR Studies of N-methyl-2- pyrrolidone with Cyclohexylamine, Cyclohexanol, and Cyclohexene at different Temperatures.
- Heat capacities of selected cycloalcohols
- Solubilities of Adipic Acid in Cyclohexanol + Cyclohexanone Mixtures and Cyclohexanone + Cyclohexane Mixtures
- Determination and Correlation for the Solubility of Glutaric Acid in Cyclohexane + Cyclohexanol + Cyclohexanone Solvent Mixtures
- Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
- Measurement and Prediction of Vapor Liquid(-Liquid) Equilibria in Ternary Systems Containing Water, an Organic Component, and Cyclohexanol
- Determination and Correlation of Liquid-Liquid Equilibria Data for Water + Cyclohexanol + (Mesityl Oxide, Toluene, and p-Xylene) Ternary Systems at Different Temperatures
- Liquid-Liquid Equilibria for the Ternary Systems Water + Cyclohexanol + Methyl Isobutyl Carbinol and Water + Cyclohexanol + Methyl Isobutyl Ketone at Different Temperatures
- Measurement and Prediction of Vapor-Liquid Equilibria in Ternary Systems Containing an Organic Component, Cyclohexylamine, and Cyclohexanol
- Determination and Correlation for the Solubilities of Succinic Acid in Cyclohexanol + Cyclohexanone + Cyclohexane Solvent Mixtures
- Vapor-Liquid Phase Equilibrium of a Cyclohexene + Water + Cyclohexanol + Isophorone Quaternary System at 500 kPa
- A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol
- Measurements and Correlation of Liquid-Liquid Equilibria for the Ternary System Cyclohexanol + Water + Cyclohexyl Formate at 298.2-338.2 K
- Thermochemistry of Branched Ethers: Experimental Study of Chemical Equilibrium in the Reacting System of tert-Amyl Alkyl Ether Synthesis
- Isobaric Vapor-Liquid Equilibria of the Ternary System Methylbutyl Ketone + Nonane + Cyclohexanol
- Thermodynamic Properties of Mixtures Containing Ionic Liquids.4.LLE of Binary Mixtures of [C2MIM][NTf2] with Propan-1-ol, Butan-1-ol, and Pentan-1-ol and [C4MIM][NTf2] with Cyclohexanol and 1,2-Hexanediol Including Studies of the Influence of Small Amounts of Water
- Phase Equilibria for the Ternary Liquid Systems of (Water + Tetrahydrofurfuryl Alcohol + Cyclic Solvent) at 298.2 K
- VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
- Vapor-Liquid Equilibrium for Binary Systems of Cyclohexane + Cyclohexanone and + Cyclohexanol at Temperatures from (414.0 to 433.7) K
- Measurements and Correlation of Liquid Liquid Equilibria for the Ternary System Water + Cyclohexanol + Cyclohexanone
- Vapor-Liquid Equilibria of Cyclohexanone + 2-Cyclohexen-1-one and Cyclohexanol + 2-Cyclohexen-1-one, Validated in a Packed Column Distillation.
- Phase Behavior of the Reactant and Products of Cyclohexane Oxidation in Compressed CO2
- Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
- Experimental and Theoretical Study of the Phase Equilibria in Ternary Aqueous Mixtures of 1,4-Butanediol with Alcohols at 298.2 K
- (Liquid + Liquid) Equilibria of (Cyclohexane + Dimethyl Sulfoxide + Cyclohexanone) and (Cyclohexane + Dimethyl Sulfoxide + Cyclohexanol) at T = 303.2 K
- Liquid-Liquid Equilibrium for the System Water + Cyclohexene + Cyclohexanol over the Temperature Range of (303.2 to 403.2) 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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