- InChI
- InChI=1S/C10H20/c1-2-3-7-10-8-5-4-6-9-10/h10H,2-9H2,1H3
- InChI Key
- GGBJHURWWWLEQH-UHFFFAOYSA-N
- Formula
- C10H20
- SMILES
- CCCCC1CCCCC1
- Molecular Weight1
- 140.27
- CAS
- 1678-93-9
- Other Names
-
- 1-CYCLOHEXYLBUTANE
- Butane, 1-cyclohexyl-
- Butylcyclohexane
- Cyclohexane, n-butyl-
- n-Butylcyclohexane
- ω : Acentric Factor.
- 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).
- 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.
- 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).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (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 |
|---|---|---|---|
| ω | 0.3620 | KDB | |
| ΔcH°liquid | -6530.30 ± 1.20 | kJ/mol | NIST |
| ΔfG° | 56.48 | kJ/mol | KDB |
| ΔfH°gas | [-213.30; -213.20] | kJ/mol |
|
| ΔfH°gas | -213.30 | kJ/mol | KDB |
| ΔfH°gas | -213.20 ± 1.40 | kJ/mol | NIST |
| ΔfH°liquid | -263.20 ± 1.30 | kJ/mol | NIST |
| ΔfusH° | 13.49 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [47.00; 50.03] | kJ/mol |
|
| ΔvapH° | 49.37 | kJ/mol | NIST |
| ΔvapH° | Outlier 47.00 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 48.90 ± 0.50 | kJ/mol | NIST |
| ΔvapH° | 49.40 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 49.40 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 49.40 | kJ/mol | NIST |
| ΔvapH° | 50.00 | kJ/mol | NIST |
| ΔvapH° | 50.03 | kJ/mol | NIST |
| ΔvapH° | 50.00 | kJ/mol | NIST |
| ΔvapH° | 50.00 | kJ/mol | NIST |
| IE | [9.41; 9.57] | eV |
|
| IE | 9.41 | eV | NIST |
| IE | 9.57 ± 0.03 | eV | NIST |
| log10WS | -3.66 | Crippen Calculated Property | |
| logPoct/wat | 3.757 | Crippen Calculated Property | |
| McVol | 140.900 | ml/mol | McGowan Calculated Property |
| Pc | [2560.00; 3150.00] | kPa |
|
| Pc | 3150.00 | kPa | KDB |
| Pc | 2560.00 | kPa | Critica... |
| Inp | [1022.00; 1061.00] |
|
|
| Inp | 1047.00 | NIST | |
| Inp | 1024.00 | NIST | |
| Inp | 1051.30 | NIST | |
| Inp | Outlier 1060.90 | NIST | |
| Inp | 1024.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1045.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | Outlier 1061.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | Outlier 1061.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1026.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1033.80 | NIST | |
| Inp | 1030.20 | NIST | |
| Inp | 1028.90 | NIST | |
| Inp | 1026.60 | NIST | |
| Inp | 1030.20 | NIST | |
| Inp | 1031.60 | NIST | |
| Inp | 1026.60 | NIST | |
| Inp | 1030.20 | NIST | |
| Inp | 1031.60 | NIST | |
| Inp | 1030.20 | NIST | |
| Inp | 1028.90 | NIST | |
| Inp | 1028.46 | NIST | |
| Inp | 1023.13 | NIST | |
| Inp | 1026.83 | NIST | |
| Inp | 1029.30 | NIST | |
| Inp | 1028.77 | NIST | |
| Inp | 1032.57 | NIST | |
| Inp | 1035.27 | NIST | |
| Inp | 1026.00 | NIST | |
| Inp | 1027.00 | NIST | |
| Inp | 1033.10 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1033.80 | NIST | |
| Inp | 1031.60 | NIST | |
| Inp | 1028.90 | NIST | |
| Inp | 1028.77 | NIST | |
| I | [1075.00; 1123.30] |
|
|
| I | 1116.00 | NIST | |
| I | 1094.00 | NIST | |
| I | 1100.00 | NIST | |
| I | 1105.00 | NIST | |
| I | 1101.70 | NIST | |
| I | 1107.60 | NIST | |
| I | 1113.20 | NIST | |
| I | 1118.10 | NIST | |
| I | 1123.30 | NIST | |
| I | 1091.20 | NIST | |
| I | 1096.70 | NIST | |
| I | 1116.00 | NIST | |
| I | 1075.00 | NIST | |
| I | 1082.00 | NIST | |
| I | 1082.00 | NIST | |
| I | 1075.00 | NIST | |
| S°gas | 459.78 | J/mol×K | NIST |
| S°liquid | 344.97 | J/mol×K | NIST |
| Tboil | 454.10 | K | KDB |
| Tc | [653.10; 667.00] | K |
|
| Tc | 667.00 | K | KDB |
| Tc | 653.10 | K | Gas-Liq... |
| Tfus | [196.85; 198.40] | K |
|
| Tfus | 198.40 | K | KDB |
| Tfus | 198.30 ± 0.50 | K | NIST |
| Tfus | 198.30 ± 0.20 | K | NIST |
| Tfus | 198.30 ± 0.20 | K | NIST |
| Tfus | 196.85 ± 0.50 | K | NIST |
| Ttriple | 198.42 ± 0.02 | K | NIST |
| Vc | 0.528 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [299.95; 403.35] | J/mol×K | [447.75; 644.56] |
|
| Cp,gas | 299.95 | J/mol×K | 447.75 | Joback Calculated Property |
| Cp,gas | 319.42 | J/mol×K | 480.55 | Joback Calculated Property |
| Cp,gas | 337.97 | J/mol×K | 513.35 | Joback Calculated Property |
| Cp,gas | 355.61 | J/mol×K | 546.16 | Joback Calculated Property |
| Cp,gas | 372.37 | J/mol×K | 578.96 | Joback Calculated Property |
| Cp,gas | 388.28 | J/mol×K | 611.76 | Joback Calculated Property |
| Cp,gas | 403.35 | J/mol×K | 644.56 | Joback Calculated Property |
| Cp,liquid | 271.04 | J/mol×K | 298.15 | NIST |
| η | [0.0002640; 0.0086122] | Pa×s | [209.84; 447.75] |
|
| η | 0.0086122 | Pa×s | 209.84 | Joback Calculated Property |
| η | 0.0030367 | Pa×s | 249.49 | Joback Calculated Property |
| η | 0.0014252 | Pa×s | 289.14 | Joback Calculated Property |
| η | 0.0008027 | Pa×s | 328.79 | Joback Calculated Property |
| η | 0.0005116 | Pa×s | 368.45 | Joback Calculated Property |
| η | 0.0003559 | Pa×s | 408.10 | Joback Calculated Property |
| η | 0.0002640 | Pa×s | 447.75 | Joback Calculated Property |
| ΔfusH | [14.14; 14.20] | kJ/mol | [198.00; 198.42] |
|
| ΔfusH | 14.20 | kJ/mol | 198.00 | NIST |
| ΔfusH | 14.14 | kJ/mol | 198.40 | NIST |
| ΔfusH | 14.14 | kJ/mol | 198.40 | NIST |
| ΔfusH | 14.16 | kJ/mol | 198.42 | NIST |
| ΔvapH | [38.49; 47.40] | kJ/mol | [293.50; 454.10] |
|
| ΔvapH | 47.40 ± 0.20 | kJ/mol | 293.50 | NIST |
| ΔvapH | 44.90 | kJ/mol | 412.00 | NIST |
| ΔvapH | 38.49 | kJ/mol | 454.10 | KDB |
| n0 | 1.43990 | 293.15 | Density... | |
| ρl | [746.38; 829.90] | kg/m3 | [253.15; 363.15] |
|
| ρl | 829.90 | kg/m3 | 253.15 | Densiti... |
| ρl | 803.07 | kg/m3 | 288.15 | Densiti... |
| ρl | 799.00 | kg/m3 | 293.00 | KDB |
| ρl | 799.37 | kg/m3 | 293.15 | Densiti... |
| ρl | 799.33 | kg/m3 | 293.15 | Densiti... |
| ρl | 799.47 | kg/m3 | 293.15 | Excess ... |
| ρl | 799.44 | kg/m3 | 293.15 | Excess ... |
| ρl | 799.47 | kg/m3 | 293.15 | Density... |
| ρl | 799.33 | kg/m3 | 293.15 | Density... |
| ρl | 799.34 | kg/m3 | 293.15 | Densiti... |
| ρl | 795.57 | kg/m3 | 298.15 | Densiti... |
| ρl | 795.59 | kg/m3 | 298.15 | Densiti... |
| ρl | 795.71 | kg/m3 | 298.15 | Excess ... |
| ρl | 795.71 | kg/m3 | 298.15 | Density... |
| ρl | 795.70 | kg/m3 | 298.15 | Excess ... |
| ρl | 795.63 | kg/m3 | 298.15 | Densiti... |
| ρl | 791.96 | kg/m3 | 303.15 | Excess ... |
| ρl | 791.81 | kg/m3 | 303.15 | Densiti... |
| ρl | 791.95 | kg/m3 | 303.15 | Excess ... |
| ρl | 791.88 | kg/m3 | 303.15 | Densiti... |
| ρl | 791.82 | kg/m3 | 303.15 | Density... |
| ρl | 791.84 | kg/m3 | 303.15 | Densiti... |
| ρl | 791.96 | kg/m3 | 303.15 | Density... |
| ρl | 788.07 | kg/m3 | 308.15 | Densiti... |
| ρl | 788.12 | kg/m3 | 308.15 | Densiti... |
| ρl | 788.19 | kg/m3 | 308.15 | Excess ... |
| ρl | 788.20 | kg/m3 | 308.15 | Excess ... |
| ρl | 784.30 | kg/m3 | 313.15 | Densiti... |
| ρl | 784.35 | kg/m3 | 313.15 | Densiti... |
| ρl | 784.41 | kg/m3 | 313.15 | Excess ... |
| ρl | 784.43 | kg/m3 | 313.15 | Excess ... |
| ρl | 784.43 | kg/m3 | 313.15 | Density... |
| ρl | 784.27 | kg/m3 | 313.15 | Densiti... |
| ρl | 784.28 | kg/m3 | 313.15 | Density... |
| ρl | 780.65 | kg/m3 | 318.15 | Excess ... |
| ρl | 780.49 | kg/m3 | 318.15 | Densiti... |
| ρl | 780.52 | kg/m3 | 318.15 | Densiti... |
| ρl | 776.71 | kg/m3 | 323.15 | Densiti... |
| ρl | 776.70 | kg/m3 | 323.15 | Densiti... |
| ρl | 776.74 | kg/m3 | 323.15 | Densiti... |
| ρl | 776.70 | kg/m3 | 323.15 | Density... |
| ρl | 777.16 | kg/m3 | 323.15 | Density... |
| ρl | 772.93 | kg/m3 | 328.15 | Densiti... |
| ρl | 769.09 | kg/m3 | 333.15 | Density... |
| ρl | 769.09 | kg/m3 | 333.15 | Densiti... |
| ρl | 769.10 | kg/m3 | 333.15 | Densiti... |
| ρl | 769.55 | kg/m3 | 333.15 | Density... |
| ρl | 769.13 | kg/m3 | 333.15 | Densiti... |
| ρl | 765.30 | kg/m3 | 338.15 | Densiti... |
| ρl | 761.43 | kg/m3 | 343.15 | Densiti... |
| ρl | 761.88 | kg/m3 | 343.15 | Density... |
| ρl | 761.40 | kg/m3 | 343.15 | Density... |
| ρl | 761.47 | kg/m3 | 343.15 | Densiti... |
| ρl | 754.16 | kg/m3 | 353.15 | Density... |
| ρl | 746.38 | kg/m3 | 363.15 | Density... |
| ΔfusS | 71.36 | J/mol×K | 198.42 | NIST |
| γ | 0.03 | N/m | 293.20 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [328.36; 484.61] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.39050e+01 | |||
| Coefficient B | -3.63952e+03 | |||
| Coefficient C | -6.10930e+01 | |||
| Temperature range, min. | 328.36 | |||
| Temperature range, max. | 484.61 | |||
| Pvap | 1.33 | kPa | 328.36 | Calculated Property |
| Pvap | 3.06 | kPa | 345.72 | Calculated Property |
| Pvap | 6.38 | kPa | 363.08 | Calculated Property |
| Pvap | 12.29 | kPa | 380.44 | Calculated Property |
| Pvap | 22.11 | kPa | 397.80 | Calculated Property |
| Pvap | 37.56 | kPa | 415.17 | Calculated Property |
| Pvap | 60.73 | kPa | 432.53 | Calculated Property |
| Pvap | 94.07 | kPa | 449.89 | Calculated Property |
| Pvap | 140.35 | kPa | 467.25 | Calculated Property |
| Pvap | 202.65 | kPa | 484.61 | Calculated Property |
| Pvap | [3.66e-06; 2575.39] | kPa | [198.42; 667.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.54321e+01 | |||
| Coefficient B | -8.39938e+03 | |||
| Coefficient C | -8.64335e+00 | |||
| Coefficient D | 2.74293e-06 | |||
| Temperature range, min. | 198.42 | |||
| Temperature range, max. | 667.00 | |||
| Pvap | 3.66e-06 | kPa | 198.42 | Calculated Property |
| Pvap | 3.45e-03 | kPa | 250.48 | Calculated Property |
| Pvap | 0.23 | kPa | 302.55 | Calculated Property |
| Pvap | 3.84 | kPa | 354.61 | Calculated Property |
| Pvap | 27.19 | kPa | 406.68 | Calculated Property |
| Pvap | 113.19 | kPa | 458.74 | Calculated Property |
| Pvap | 331.82 | kPa | 510.81 | Calculated Property |
| Pvap | 765.09 | kPa | 562.87 | Calculated Property |
| Pvap | 1490.65 | kPa | 614.94 | Calculated Property |
| Pvap | 2575.39 | kPa | 667.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Cyclohexane, butyl-.
Mixtures
- Pentane, 2,2,4-trimethyl- + Cyclohexane, butyl-
- Cyclohexane, butyl- + Cyclopropyl carbinol
- Dodecane + Cyclohexane, butyl-
- Dodecane + Cyclohexane, butyl- + Cyclopropyl carbinol
- Benzene, n-butyl- + Hexadecane + Cyclohexane, butyl-
- Hexadecane + Benzene, hexyl- + Cyclohexane, butyl-
- Benzene, n-butyl- + Dodecane + Cyclohexane, butyl-
- Dodecane + Benzene, hexyl- + Cyclohexane, butyl-
- Toluene + Hexadecane + Cyclohexane, butyl-
- Hexadecane + Cyclohexane, butyl-
- Benzene, n-butyl- + Cyclohexane, butyl- + Nonane, 2,2,4,4,6,8,8-heptamethyl-
- Dodecane + Cyclohexane, butyl- + Nonane, 2,2,4,4,6,8,8-heptamethyl-
- (3a«alpha»,4«beta»,7«beta»,7a«alpha»)-octahydro-4,7-methano-1H-indene + Cyclohexane, butyl-
- Heptane + Cyclohexane, butyl-
- Octane + Cyclohexane, butyl-
- Cyclohexane, butyl- + Nonane
- Decane + Cyclohexane, butyl-
- Cyclohexane, butyl- + Tetradecane
- Adamantane, 1,3-dimethyl- + Cyclohexane, butyl-
- Cyclohexane, butyl- + 1,1'-Bicyclohexyl
Find more mixtures with Cyclohexane, butyl-.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Phase equilibria of (CO2 + butylbenzene) and (CO2 + butylcyclohexane) at temperatures between (323.15 and 423.15) K and at pressures up to 21MPa
- Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
- Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
- Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
- Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Quaternary Mixtures of n-Dodecane (1), n-Butylcyclohexane (2), n-Butylbenzene (3), and 2,2,4,4,6,8,8-Heptamethylnonane (4) at 0.1 MPa as Potential Surrogate Mixtures for Military Jet Fuel, JP-5
- Critical Point Measurements for Five n-Alkylcyclohexanes (C6 to C10) by the Pulse-Heating Method
- Gas-Liquid Critical Temperatures of Some Alkenes, Amines, and Cyclic Hydrocarbons
- Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
- Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
- Density, Viscosity, Surface Tension, and Refractive Index for Binary Mixtures of 1,3-Dimethyladamantane with Four C10 Alkanes
- Density, Viscosity, Refractive Index, and Freezing Point for Binary Mixtures of 1,1'-Bicyclohexyl with Alkylcyclohexane
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
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that the value is more than 2 standard deviations away from the
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