Chemical Properties of BUTYLCYCLOHEXANE (CAS 1678-93-9)

BUTYLCYCLOHEXANE

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-
  • Cyclohexane, n-butyl-
  • cyclohexane, butyl-
  • n-butylcyclohexane
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Physical Properties

Property Value Unit Source
ω [0.2743; 0.3620]   Show Hide
ω 0.3524 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω 0.3618 Passut and Danner (1973), critical constants and acentric factors Compiled value
ω 0.2743 ChemSep v8.3 pure component data Compiled value
ω 0.3620 KDB
ΔcH°liquid -6530.30 ± 1.20 kJ/mol NIST
μ 0.00 debye ChemSep v8.3 pure component data Compiled value
ΔfG° [56.48; 56.54] kJ/mol Show Hide
ΔfG° 56.54 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfG° 56.48 kJ/mol KDB
ΔfH°gas [-213.30; -213.17] kJ/mol Show Hide
ΔfH°gas -213.17 kJ/mol ChemSep v8.3 pure component data Compiled value
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 Show Hide
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 Show Hide
IE 9.41 eV NIST
IE 9.57 ± 0.03 eV NIST
log10WS -5.42 Relay (1.0) Calculated Property
logPoct/wat 3.757 Crippen Calculated Property
McVol 140.900 ml/mol McGowan Calculated Property
Pc [2560.00; 3151.21] kPa Show Hide
Pc 2560.00 kPa Critical Point Measurements for Five n-Alkylcyclohexanes (C6 to C10) by the Pulse-Heating Method
Pc 3151.21 kPa PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc 3150.90 kPa Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc 2570.00 kPa ChemSep v8.3 pure component data Compiled value
Pc 3150.00 kPa KDB
Ptriple 3.66e-06 kPa ChemSep v8.3 pure component data Compiled value
Inp [1022.00; 1061.00]   Show Hide
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
Ip [1075.00; 1123.30]   Show Hide
Ip 1116.00 NIST
Ip 1094.00 NIST
Ip 1100.00 NIST
Ip 1105.00 NIST
Ip 1101.70 NIST
Ip 1107.60 NIST
Ip 1113.20 NIST
Ip 1118.10 NIST
Ip 1123.30 NIST
Ip 1091.20 NIST
Ip 1096.70 NIST
Ip 1116.00 NIST
Ip 1075.00 NIST
Ip 1082.00 NIST
Ip 1082.00 NIST
Ip 1116.00 NIST
Ip 1107.60 NIST
Ip 1096.70 NIST
Ip 1075.00 NIST
S°gas 459.78 J/mol×K NIST
S°liquid 344.97 J/mol×K NIST
Tboil [446.65; 454.50] K Show Hide
Tboil 454.13 K ChemSep v8.3 pure component data Compiled value
Tboil 454.10 K KDB
Tboil 452.20 K NIST
Tboil 454.20 K NIST
Tboil Outlier 446.65 ± 5.00 K NIST
Tboil 454.10 ± 0.20 K NIST
Tboil 454.09 ± 0.30 K NIST
Tboil 454.09 ± 0.03 K NIST
Tboil 454.09 ± 0.30 K NIST
Tboil 454.09 ± 0.30 K NIST
Tboil 454.09 ± 0.20 K NIST
Tboil 454.09 ± 0.30 K NIST
Tboil 454.50 ± 0.30 K NIST
Tboil 453.90 ± 0.40 K NIST
Tboil 453.65 ± 0.50 K NIST
Tboil 453.80 ± 1.50 K NIST
Tboil 450.65 ± 2.00 K NIST
Tboil 450.15 ± 2.00 K NIST
Tboil 453.15 ± 3.00 K NIST
Tc [649.30; 667.04] K Show Hide
Tc 649.30 K DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
Tc 653.10 K Gas-Liquid Critical Temperatures of Some Alkenes, Amines, and Cyclic Hydrocarbons
Tc 667.00 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc 667.04 K Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc 667.00 K ChemSep v8.3 pure component data Compiled value
Tc 667.00 K KDB
Tfus [196.85; 198.42] K Show Hide
Tfus 198.15 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 198.42 K ChemSep v8.3 pure component data Compiled value
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 Outlier 196.85 ± 0.50 K NIST
Ttriple [198.42; 198.42] K Show Hide
Ttriple 198.42 K ChemSep v8.3 pure component data Compiled value
Ttriple 198.42 ± 0.02 K NIST
UQi 5.40 ChemSep v8.3 pure component data Compiled value
URi 6.74 ChemSep v8.3 pure component data Compiled value
Vc [0.530; 0.534] m3/kmol Show Hide
Vc 0.530 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc 0.534 m3/kmol ChemSep v8.3 pure component data Compiled value
Zc 0.2470000 ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,liquid 271.04 J/mol×K 298.15 NIST
Csat [228.40; 314.00] J/mol×K [210.00; 370.00] Show Hide
Csat 228.40 J/mol×K 210.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 232.20 J/mol×K 220.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 236.30 J/mol×K 230.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 240.70 J/mol×K 240.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 245.40 J/mol×K 250.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 250.30 J/mol×K 260.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 255.50 J/mol×K 270.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 257.20 J/mol×K 273.15 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 260.90 J/mol×K 280.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 266.40 J/mol×K 290.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 271.00 J/mol×K 298.15 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 272.10 J/mol×K 300.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 277.90 J/mol×K 310.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 283.80 J/mol×K 320.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 289.80 J/mol×K 330.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 295.80 J/mol×K 340.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 301.90 J/mol×K 350.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 308.00 J/mol×K 360.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat 314.00 J/mol×K 370.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
ΔfusH [14.14; 14.20] kJ/mol [198.00; 198.42] Show Hide
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] Show Hide
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, Viscosity, Refractive Index, and Freezing Point for Binary Mixtures of 1,1'-Bicyclohexyl with Alkylcyclohexane
ρl [746.38; 829.90] kg/m3 [253.15; 363.15] Show Hide
ρl 829.90 kg/m3 253.15 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
ρl 803.07 kg/m3 288.15 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
ρl 799.00 kg/m3 293.00 KDB
ρl 799.37 kg/m3 293.15 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
ρl 799.47 kg/m3 293.15 Density, Viscosity, Surface Tension, and Refractive Index for Binary Mixtures of 1,3-Dimethyladamantane with Four C10 Alkanes
ρl 799.34 kg/m3 293.15 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
ρl 799.44 kg/m3 293.15 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
ρl 799.33 kg/m3 293.15 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
ρl 799.33 kg/m3 293.15 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)
ρl 799.33 kg/m3 293.15 Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
ρl 799.47 kg/m3 293.15 Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
ρl 795.59 kg/m3 298.15 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
ρl 795.71 kg/m3 298.15 Density, Viscosity, Surface Tension, and Refractive Index for Binary Mixtures of 1,3-Dimethyladamantane with Four C10 Alkanes
ρl 795.63 kg/m3 298.15 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
ρl 795.71 kg/m3 298.15 Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
ρl 795.70 kg/m3 298.15 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
ρl 795.57 kg/m3 298.15 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
ρl 791.82 kg/m3 303.15 Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
ρl 791.82 kg/m3 303.15 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)
ρl 791.88 kg/m3 303.15 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
ρl 791.81 kg/m3 303.15 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
ρl 791.96 kg/m3 303.15 Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
ρl 791.95 kg/m3 303.15 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
ρl 791.84 kg/m3 303.15 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
ρl 791.96 kg/m3 303.15 Density, Viscosity, Surface Tension, and Refractive Index for Binary Mixtures of 1,3-Dimethyladamantane with Four C10 Alkanes
ρl 788.19 kg/m3 308.15 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
ρl 788.20 kg/m3 308.15 Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
ρl 788.07 kg/m3 308.15 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
ρl 788.12 kg/m3 308.15 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
ρl 784.35 kg/m3 313.15 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
ρl 784.41 kg/m3 313.15 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
ρl 784.28 kg/m3 313.15 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)
ρl 784.43 kg/m3 313.15 Density, Viscosity, Surface Tension, and Refractive Index for Binary Mixtures of 1,3-Dimethyladamantane with Four C10 Alkanes
ρl 784.43 kg/m3 313.15 Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
ρl 784.30 kg/m3 313.15 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
ρl 784.27 kg/m3 313.15 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
ρl 784.28 kg/m3 313.15 Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
ρl 780.52 kg/m3 318.15 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
ρl 780.49 kg/m3 318.15 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
ρl 780.65 kg/m3 318.15 Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
ρl 776.70 kg/m3 323.15 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)
ρl 776.70 kg/m3 323.15 Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
ρl 776.71 kg/m3 323.15 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
ρl 776.70 kg/m3 323.15 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
ρl 776.74 kg/m3 323.15 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
ρl 777.16 kg/m3 323.15 Density, Viscosity, Surface Tension, and Refractive Index for Binary Mixtures of 1,3-Dimethyladamantane with Four C10 Alkanes
ρl 772.93 kg/m3 328.15 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
ρl 769.09 kg/m3 333.15 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)
ρl 769.55 kg/m3 333.15 Density, Viscosity, Surface Tension, and Refractive Index for Binary Mixtures of 1,3-Dimethyladamantane with Four C10 Alkanes
ρl 769.10 kg/m3 333.15 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
ρl 769.13 kg/m3 333.15 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
ρl 769.09 kg/m3 333.15 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
ρl 769.09 kg/m3 333.15 Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
ρl 765.30 kg/m3 338.15 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
ρl 761.43 kg/m3 343.15 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
ρl 761.40 kg/m3 343.15 Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
ρl 761.47 kg/m3 343.15 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
ρl 761.88 kg/m3 343.15 Density, Viscosity, Surface Tension, and Refractive Index for Binary Mixtures of 1,3-Dimethyladamantane with Four C10 Alkanes
ρl 761.40 kg/m3 343.15 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)
ρl 753.70 kg/m3 353.15 Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylcyclohexane with Toluene or n-Hexadecane
ρl 754.16 kg/m3 353.15 Density, Viscosity, Surface Tension, and Refractive Index for Binary Mixtures of 1,3-Dimethyladamantane with Four C10 Alkanes
ρl 746.38 kg/m3 363.15 Density, Viscosity, Surface Tension, and Refractive Index for Binary Mixtures of 1,3-Dimethyladamantane with Four C10 Alkanes
ΔfusS 71.36 J/mol×K 198.42 NIST
γ 0.03 N/m 293.20 KDB

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [149.10; 614.04] J/mol×K [150.00; 1500.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,gas in J/mol×K, T in K
Coefficient A1.45450e+02
Coefficient B-8.90370e+02
Coefficient C7.33324e+00
Coefficient D-7.09800e-04
Coefficient E2.11010e-07
Temperature range, min.150.00
Temperature range, max.1500.00
Cp,gas 149.10 J/mol×K 150.00 Calculated Property
Cp,gas 210.26 J/mol×K 300.00 Calculated Property
Cp,gas 305.90 J/mol×K 450.00 Calculated Property
Cp,gas 389.99 J/mol×K 600.00 Calculated Property
Cp,gas 454.17 J/mol×K 750.00 Calculated Property
Cp,gas 501.85 J/mol×K 900.00 Calculated Property
Cp,gas 537.98 J/mol×K 1050.00 Calculated Property
Cp,gas 566.76 J/mol×K 1200.00 Calculated Property
Cp,gas 591.33 J/mol×K 1350.00 Calculated Property
Cp,gas 614.04 J/mol×K 1500.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [224.04; 618.00] J/mol×K [198.42; 667.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,liquid in J/mol×K, T in K
Coefficient A1.17850e+02
Coefficient B4.48610e+01
Coefficient C3.44824e+00
Coefficient D5.39470e-03
Coefficient E-2.02040e-06
Temperature range, min.198.42
Temperature range, max.667.00
Cp,liquid 224.04 J/mol×K 198.42 Calculated Property
Cp,liquid 245.83 J/mol×K 250.48 Calculated Property
Cp,liquid 272.90 J/mol×K 302.55 Calculated Property
Cp,liquid 305.34 J/mol×K 354.61 Calculated Property
Cp,liquid 343.35 J/mol×K 406.68 Calculated Property
Cp,liquid 387.10 J/mol×K 458.74 Calculated Property
Cp,liquid 436.64 J/mol×K 510.81 Calculated Property
Cp,liquid 491.89 J/mol×K 562.87 Calculated Property
Cp,liquid 552.52 J/mol×K 614.94 Calculated Property
Cp,liquid 618.00 J/mol×K 667.00 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0215556; 0.0001449] Pa×s [198.42; 600.30] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is η in Pa×s, T in K
Coefficient A-6.61512e+01
Coefficient B3.53644e+03
Coefficient C8.46644e+00
Coefficient D-7.61222e-06
Coefficient E2.00000e+00
Temperature range, min.198.42
Temperature range, max.600.30
η 0.0215556 Pa×s 198.42 Calculated Property
η 0.0039154 Pa×s 243.07 Calculated Property
η 0.0014254 Pa×s 287.73 Calculated Property
η 0.0007512 Pa×s 332.38 Calculated Property
η 0.0004867 Pa×s 377.03 Calculated Property
η 0.0003544 Pa×s 421.69 Calculated Property
η 0.0002753 Pa×s 466.34 Calculated Property
η 0.0002208 Pa×s 510.99 Calculated Property
η 0.0001791 Pa×s 555.65 Calculated Property
η 0.0001449 Pa×s 600.30 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [55.86; 14.22] kJ/mol [198.42; 642.34] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc
Y is ΔvapH in kJ/mol, T in K
Coefficient A7.76560e+01
Coefficient B1.63700e+00
Coefficient C-3.32690e+00
Coefficient D3.66980e+00
Coefficient E-1.48000e+00
Critical temperature, Tc (K)6.67000e+02
Temperature range, min.198.42
Temperature range, max.642.34
ΔvapH 55.86 kJ/mol 198.42 Calculated Property
ΔvapH 52.78 kJ/mol 247.74 Calculated Property
ΔvapH 49.84 kJ/mol 297.07 Calculated Property
ΔvapH 46.79 kJ/mol 346.39 Calculated Property
ΔvapH 43.43 kJ/mol 395.72 Calculated Property
ΔvapH 39.63 kJ/mol 445.04 Calculated Property
ΔvapH 35.24 kJ/mol 494.37 Calculated Property
ΔvapH 30.08 kJ/mol 543.69 Calculated Property
ΔvapH 23.69 kJ/mol 593.02 Calculated Property
ΔvapH 14.22 kJ/mol 642.34 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.65] kPa [328.36; 484.61] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.39050e+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 [3.62e-06; 2574.63] kPa [198.42; 667.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is Pvap in kPa, T in K
Coefficient A7.57942e+01
Coefficient B-8.41770e+03
Coefficient C-8.69680e+00
Coefficient D2.77130e-06
Coefficient E2.00000e+00
Temperature range, min.198.42
Temperature range, max.667.00
Pvap 3.62e-06 kPa 198.42 Calculated Property
Pvap 3.44e-03 kPa 250.48 Calculated Property
Pvap 0.23 kPa 302.55 Calculated Property
Pvap 3.84 kPa 354.61 Calculated Property
Pvap 27.20 kPa 406.68 Calculated Property
Pvap 113.26 kPa 458.74 Calculated Property
Pvap 331.94 kPa 510.81 Calculated Property
Pvap 765.13 kPa 562.87 Calculated Property
Pvap 1490.39 kPa 614.94 Calculated Property
Pvap 2574.63 kPa 667.00 Calculated Property
Pvap [3.66e-06; 2575.39] kPa [198.42; 667.00] KDB Vapor Pressure Data Show Hide
Equationln(Y) = A + B/T + C·ln(T) + D·T² + E/T²
Y is Pvap in kPa, T in K
Coefficient A7.54321e+01
Coefficient B-8.39938e+03
Coefficient C-8.64335e+00
Coefficient D2.74293e-06
Coefficient E0.00000e+00
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
Property Value Unit Temperature (K) Source
ρl [864.76; 428.42] kg/m3 [198.42; 642.34] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A / B^(1 + (1 − T/C)^D)
Y is ρl in kg/m3, T in K
Coefficient A6.98327e+01
Coefficient B2.65720e-01
Coefficient C6.67000e+02
Coefficient D3.02540e-01
Temperature range, min.198.42
Temperature range, max.642.34
ρl 864.76 kg/m3 198.42 Calculated Property
ρl 831.34 kg/m3 247.74 Calculated Property
ρl 796.52 kg/m3 297.07 Calculated Property
ρl 759.96 kg/m3 346.39 Calculated Property
ρl 721.21 kg/m3 395.72 Calculated Property
ρl 679.58 kg/m3 445.04 Calculated Property
ρl 633.91 kg/m3 494.37 Calculated Property
ρl 582.13 kg/m3 543.69 Calculated Property
ρl 519.47 kg/m3 593.02 Calculated Property
ρl 428.42 kg/m3 642.34 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.04; 5.86e-04] N/m [198.42; 642.34] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is γ in N/m, T in K
Coefficient A-7.88250e-03
Coefficient B3.92210e+01
Coefficient C-3.18480e+00
Coefficient D2.42340e-04
Coefficient E-4.37060e-06
Temperature range, min.198.42
Temperature range, max.642.34
γ 0.04 N/m 198.42 Calculated Property
γ 0.03 N/m 247.74 Calculated Property
γ 0.03 N/m 297.07 Calculated Property
γ 0.02 N/m 346.39 Calculated Property
γ 0.02 N/m 395.72 Calculated Property
γ 0.01 N/m 445.04 Calculated Property
γ 0.01 N/m 494.37 Calculated Property
γ 0.01 N/m 543.69 Calculated Property
γ 0.00 N/m 593.02 Calculated Property
γ 5.86e-04 N/m 642.34 Calculated Property
Property Value Unit Temperature (K) Source
λgas [0.00; 0.09] W/m×K [198.42; 1000.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·T^B / (1 + C/T + D/T²)
Y is λgas in W/m×K, T in K
Coefficient A6.35090e-05
Coefficient B1.10320e+00
Coefficient C4.70220e+02
Coefficient D4.29220e+04
Temperature range, min.198.42
Temperature range, max.1000.00
λgas 0.00 W/m×K 198.42 Calculated Property
λgas 0.01 W/m×K 287.48 Calculated Property
λgas 0.02 W/m×K 376.55 Calculated Property
λgas 0.03 W/m×K 465.61 Calculated Property
λgas 0.03 W/m×K 554.68 Calculated Property
λgas 0.04 W/m×K 643.74 Calculated Property
λgas 0.05 W/m×K 732.81 Calculated Property
λgas 0.06 W/m×K 821.87 Calculated Property
λgas 0.07 W/m×K 910.94 Calculated Property
λgas 0.09 W/m×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
λliquid [0.13; 0.09] W/m×K [198.42; 454.43] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is λliquid in W/m×K, T in K
Coefficient A-4.07530e-02
Coefficient B3.94480e+00
Coefficient C-1.65880e+00
Coefficient D-4.59870e-04
Coefficient E-1.02150e-06
Temperature range, min.198.42
Temperature range, max.454.43
λliquid 0.13 W/m×K 198.42 Calculated Property
λliquid 0.12 W/m×K 226.87 Calculated Property
λliquid 0.12 W/m×K 255.31 Calculated Property
λliquid 0.12 W/m×K 283.76 Calculated Property
λliquid 0.11 W/m×K 312.20 Calculated Property
λliquid 0.11 W/m×K 340.65 Calculated Property
λliquid 0.10 W/m×K 369.09 Calculated Property
λliquid 0.10 W/m×K 397.54 Calculated Property
λliquid 0.09 W/m×K 425.98 Calculated Property
λliquid 0.09 W/m×K 454.43 Calculated Property

Similar Compounds

Cyclohexane, propyl-. Cyclohexane, decyl-. n-Nonylcyclohexane. Cyclohexane, octyl-. TETRADECYLCYCLOHEXANE. Cyclohexane, eicosyl-. Cyclohexane, hexadecyl-. n-Pentadecylcyclohexane. Cyclohexane, octadecyl-. Heptylcyclohexane. N-heptadecylcyclohexane. Dodecylcyclohexane. Cyclohexane, hexyl-. Cyclohexane, undecyl-. Cyclohexane, pentyl-.

Find more compounds similar to BUTYLCYCLOHEXANE.

Mixtures

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Sources

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