Chemical Properties of Cyclohexane, propyl- (CAS 1678-92-8)

Cyclohexane, propyl-

InChI
InChI=1S/C9H18/c1-2-6-9-7-4-3-5-8-9/h9H,2-8H2,1H3
InChI Key
DEDZSLCZHWTGOR-UHFFFAOYSA-N
Formula
C9H18
SMILES
CCCC1CCCCC1
Molecular Weight1
126.24
CAS
1678-92-8
Other Names
  • 1-cyclohexylpropane
  • Cyclohexane, n-propyl-
  • n-Propyl cyclohexane
  • n-Propylcyclohexane
  • propylcyclohexane
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Physical Properties

Property Value Unit Source
ω [0.2577; 0.2595]   Show Hide
ω 0.2585 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω 0.2577 Passut and Danner (1973), critical constants and acentric factors Compiled value
ω 0.2595 ChemSep v8.3 pure component data Compiled value
ω 0.2580 KDB
AP 322.950 K KDB
ΔcH°liquid [-5876.60; -5875.80] kJ/mol Show Hide
ΔcH°liquid -5876.60 ± 0.92 kJ/mol NIST
ΔcH°liquid -5875.80 ± 1.10 kJ/mol NIST
μ 0.00 debye ChemSep v8.3 pure component data Compiled value
ΔfG° [47.35; 47.38] kJ/mol Show Hide
ΔfG° 47.38 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfG° 47.35 kJ/mol KDB
Δc,grossH 5875.76 kJ/mol KDB
Δc,netH 5479.660 kJ/mol KDB
ΔfH°gas [-193.40; -192.40] kJ/mol Show Hide
ΔfH°gas -193.30 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas -193.40 kJ/mol KDB
ΔfH°gas -192.40 kJ/mol NIST
ΔfH°gas -193.30 ± 1.30 kJ/mol NIST
ΔfH°liquid [-238.40; -237.50] kJ/mol Show Hide
ΔfH°liquid -237.50 ± 1.10 kJ/mol NIST
ΔfH°liquid -238.40 ± 1.30 kJ/mol NIST
ΔfusH° 10.90 kJ/mol Joback Calculated Property
ΔvapH° [42.80; 45.20] kJ/mol Show Hide
ΔvapH° 45.10 kJ/mol NIST
ΔvapH° Outlier 42.80 ± 0.50 kJ/mol NIST
ΔvapH° 44.70 ± 0.40 kJ/mol NIST
ΔvapH° 44.70 ± 0.40 kJ/mol NIST
ΔvapH° 45.20 kJ/mol NIST
ΔvapH° 45.15 kJ/mol NIST
ΔvapH° 45.10 kJ/mol NIST
ΔvapH° 45.20 kJ/mol NIST
ΔvapH° 45.08 kJ/mol NIST
ΔvapH° 45.10 kJ/mol NIST
IE 9.46 eV NIST
log10WS -5.00 Relay (1.0) Calculated Property
logPoct/wat 3.367 Crippen Calculated Property
McVol 126.810 ml/mol McGowan Calculated Property
Pc [2546.30; 2860.00] kPa Show Hide
Pc 2860.00 kPa Critical Point Measurements for Five n-Alkylcyclohexanes (C6 to C10) by the Pulse-Heating Method
Pc 2546.30 kPa PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc 2806.86 kPa Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc 2807.00 kPa ChemSep v8.3 pure component data Compiled value
Pc 2800.00 kPa KDB
Ptriple 8.59e-07 kPa ChemSep v8.3 pure component data Compiled value
Inp [915.00; 962.10]   Show Hide
Inp 938.00 NIST
Inp 951.00 NIST
Inp 926.00 NIST
Inp Outlier 952.30 NIST
Inp Outlier 962.10 NIST
Inp 936.00 NIST
Inp 936.40 NIST
Inp 947.00 NIST
Inp 931.00 NIST
Inp 937.00 NIST
Inp 940.00 NIST
Inp 934.00 NIST
Inp 938.00 NIST
Inp 942.00 NIST
Inp 945.00 NIST
Inp 943.00 NIST
Inp 946.00 NIST
Inp 948.00 NIST
Inp 950.00 NIST
Inp 952.00 NIST
Inp 944.00 NIST
Inp 932.00 NIST
Inp 925.00 NIST
Inp 928.00 NIST
Inp 930.00 NIST
Inp 933.00 NIST
Inp 937.00 NIST
Inp 925.00 NIST
Inp 944.00 NIST
Inp 931.00 NIST
Inp 944.00 NIST
Inp 925.00 NIST
Inp 926.00 NIST
Inp 923.00 NIST
Inp 931.00 NIST
Inp 935.00 NIST
Inp 923.00 NIST
Inp 950.00 NIST
Inp 928.00 NIST
Inp 938.00 NIST
Inp 934.00 NIST
Inp 941.00 NIST
Inp 930.50 NIST
Inp 927.10 NIST
Inp 926.40 NIST
Inp 924.20 NIST
Inp 927.10 NIST
Inp 929.10 NIST
Inp 936.40 NIST
Inp 926.40 NIST
Inp 916.00 NIST
Inp 924.20 NIST
Inp 927.10 NIST
Inp 929.10 NIST
Inp 927.10 NIST
Inp 926.40 NIST
Inp 925.22 NIST
Inp 920.09 NIST
Inp 923.67 NIST
Inp 925.93 NIST
Inp 925.46 NIST
Inp 929.15 NIST
Inp 931.59 NIST
Inp 923.00 NIST
Inp 933.00 NIST
Inp 950.33 NIST
Inp 927.00 NIST
Inp 936.00 NIST
Inp 935.00 NIST
Inp 930.00 NIST
Inp 944.00 NIST
Inp 938.00 NIST
Inp 939.00 NIST
Inp 922.00 NIST
Inp 915.00 NIST
Inp 931.00 NIST
Inp 937.00 NIST
Inp 937.00 NIST
Inp 933.00 NIST
Inp 921.00 NIST
Inp 923.00 NIST
Inp 935.00 NIST
Inp 922.00 NIST
Ip [982.00; 1019.00]   Show Hide
Ip 1019.00 NIST
Ip 998.00 NIST
Ip 1003.00 NIST
Ip 1008.00 NIST
Ip 1019.00 NIST
Ip 982.00 NIST
Ip 982.00 NIST
S°gas 419.86 J/mol×K NIST
S°liquid 311.88 J/mol×K NIST
Tboil [426.00; 430.30] K Show Hide
Tboil 429.90 K ChemSep v8.3 pure component data Compiled value
Tboil 429.90 K KDB
Tboil 428.20 K NIST
Tboil Outlier 426.00 ± 3.00 K NIST
Tboil 429.00 ± 2.00 K NIST
Tboil 429.87 ± 0.50 K NIST
Tboil 430.30 ± 1.00 K NIST
Tboil 429.70 ± 1.00 K NIST
Tboil 429.87 ± 0.03 K NIST
Tboil 429.80 ± 0.30 K NIST
Tboil 429.82 ± 0.30 K NIST
Tboil 429.86 ± 0.02 K NIST
Tboil 429.90 ± 0.40 K NIST
Tboil 429.86 ± 0.20 K NIST
Tboil 429.87 ± 0.20 K NIST
Tboil 428.85 ± 0.60 K NIST
Tboil 427.00 ± 2.50 K NIST
Tboil 428.10 ± 0.50 K NIST
Tboil 428.85 ± 0.60 K NIST
Tboil 429.00 ± 2.00 K NIST
Tboil 428.00 ± 2.00 K NIST
Tboil 427.00 ± 2.00 K NIST
Tboil 427.00 ± 2.00 K NIST
Tboil 427.00 ± 3.00 K NIST
Tboil 427.00 ± 2.00 K NIST
Tboil 426.65 ± 1.50 K NIST
Tc [630.80; 639.26] K Show Hide
Tc 630.80 K Gas-Liquid Critical Temperatures of Some Alkenes, Amines, and Cyclic Hydrocarbons
Tc 639.00 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc 639.26 K Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc 639.15 K ChemSep v8.3 pure component data Compiled value
Tc 639.00 K KDB
Tfus [178.06; 178.70] K Show Hide
Tfus 178.20 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 178.25 K ChemSep v8.3 pure component data Compiled value
Tfus Outlier 178.70 K KDB
Tfus 178.09 ± 0.20 K NIST
Tfus 178.19 ± 0.02 K NIST
Tfus 178.06 ± 0.10 K NIST
Ttriple [178.25; 178.25] K Show Hide
Ttriple 178.25 K ChemSep v8.3 pure component data Compiled value
Ttriple 178.25 ± 0.02 K NIST
UQi 4.86 ChemSep v8.3 pure component data Compiled value
URi 6.07 ChemSep v8.3 pure component data Compiled value
Vc [0.472; 0.481] m3/kmol Show Hide
Vc 0.481 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc 0.477 m3/kmol ChemSep v8.3 pure component data Compiled value
Vc 0.472 m3/kmol KDB
Zc [0.2490130; 0.2520000]   Show Hide
Zc 0.2520000 ChemSep v8.3 pure component data Compiled value
Zc 0.2490130 KDB

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,liquid 242.04 J/mol×K 298.15 NIST
Csat [195.80; 281.70] J/mol×K [190.00; 370.00] Show Hide
Csat 195.80 J/mol×K 190.00 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 198.90 J/mol×K 200.00 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 202.30 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 206.00 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 209.90 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 214.10 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 218.50 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 223.10 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 227.80 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 229.40 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 232.80 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 237.80 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 242.10 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 243.10 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 248.40 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 253.80 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 259.30 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 264.90 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 270.50 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 276.10 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 281.70 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 [10.37; 13.07] kJ/mol [178.00; 178.30] Show Hide
ΔfusH 10.60 kJ/mol 178.00 NIST
ΔfusH 13.07 kJ/mol 178.25 NIST
ΔfusH 10.37 kJ/mol 178.30 NIST
ΔfusH 10.37 kJ/mol 178.30 NIST
ΔvapH [36.07; 41.70] kJ/mol [388.50; 429.90] Show Hide
ΔvapH 41.70 kJ/mol 388.50 NIST
ΔvapH 36.07 kJ/mol 429.90 KDB
n0 1.43478 298.15 KDB
ρl [738.00; 797.42] kg/m3 [288.15; 363.15] Show Hide
ρl 797.42 kg/m3 288.15 Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl 793.00 kg/m3 293.00 KDB
ρl 793.53 kg/m3 293.15 Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl 793.54 kg/m3 293.15 Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
ρl 790.00 kg/m3 293.15 Volume expansion prediction of supercritical CO 2 + crude oil
ρl 789.63 kg/m3 298.15 Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl 785.73 kg/m3 303.15 Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
ρl 785.72 kg/m3 303.15 Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl 777.90 kg/m3 313.15 Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
ρl 777.88 kg/m3 313.15 Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl 770.04 kg/m3 323.15 Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
ρl 770.00 kg/m3 323.15 Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl 762.09 kg/m3 333.15 Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl 762.12 kg/m3 333.15 Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
ρl 754.20 kg/m3 343.15 Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
ρl 746.10 kg/m3 353.15 Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
ρl 738.00 kg/m3 363.15 Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
ΔfusS 58.19 J/mol×K 178.25 NIST
γ 0.03 N/m 298.20 KDB

Datasets

Thermal conductivity, W/m/K

Fixed Measured
Pressure, kPa - Gas Temperature, K - Gas Thermal conductivity, W/m/K - Gas
83.00 481.25 0.0276
83.00 481.94 0.0281
83.00 482.22 0.0282
84.00 481.45 0.0279
84.00 481.68 0.0280
88.00 453.61 0.0248
89.00 453.38 0.0247
89.00 453.87 0.0249
89.00 454.16 0.0250
90.00 454.48 0.0251
91.00 543.05 0.0361
91.00 543.18 0.0364
91.00 543.33 0.0367
91.00 543.51 0.0367
91.00 543.71 0.0367
120.00 510.63 0.0315
121.00 510.81 0.0317
121.00 511.02 0.0319
121.00 511.26 0.0319
124.00 603.12 0.0448
124.00 603.25 0.0448
125.00 603.40 0.0450
125.00 603.55 0.0448
125.00 603.73 0.0447
131.00 481.93 0.0283
131.00 482.21 0.0283
131.00 573.95 0.0403
132.00 481.23 0.0280
132.00 481.43 0.0282
132.00 481.66 0.0283
132.00 573.62 0.0403
132.00 573.78 0.0403
150.00 453.32 0.0246
150.00 453.55 0.0248
151.00 453.82 0.0249
151.00 603.10 0.0461
151.00 603.16 0.0462
151.00 603.22 0.0461
151.00 603.29 0.0461
151.00 603.36 0.0459
152.00 603.43 0.0459
152.00 603.49 0.0458
153.00 454.11 0.0250
153.00 603.56 0.0461
154.00 454.43 0.0251
154.00 603.63 0.0462
154.00 603.71 0.0463
162.00 453.23 0.0249
163.00 453.47 0.0250
163.00 453.73 0.0251
164.00 454.03 0.0251
164.00 454.35 0.0252
191.00 481.24 0.0289
192.00 481.44 0.0289
193.00 481.65 0.0290
193.00 481.89 0.0290
193.00 482.17 0.0290
213.00 511.24 0.0323
214.00 510.62 0.0318
214.00 510.81 0.0319
214.00 511.02 0.0321
222.00 543.02 0.0365
224.00 543.16 0.0370
226.00 543.32 0.0371
227.00 543.49 0.0371
228.00 543.70 0.0369
248.00 481.29 0.0288
248.00 481.48 0.0288
249.00 481.69 0.0290
250.00 481.92 0.0290
251.00 482.18 0.0291
259.00 573.47 0.0405
260.00 573.61 0.0406
261.00 573.77 0.0408
262.00 573.95 0.0408
287.00 603.17 0.0467
289.00 603.28 0.0470
290.00 603.41 0.0473
291.00 603.57 0.0472
310.00 481.26 0.0290
310.00 481.45 0.0292
310.00 481.65 0.0293
310.00 481.88 0.0295
310.00 482.13 0.0296
312.00 510.40 0.0330
312.00 510.56 0.0331
312.00 510.74 0.0332
312.00 510.96 0.0332
312.00 511.19 0.0331
320.00 543.01 0.0372
321.00 543.15 0.0376
322.00 543.31 0.0376
322.00 543.49 0.0374
322.00 543.70 0.0372
411.00 573.71 0.0420
412.00 510.73 0.0337
412.00 573.43 0.0417
412.00 573.56 0.0420
413.00 510.38 0.0340
413.00 510.55 0.0339
413.00 510.93 0.0338
413.00 511.14 0.0338
413.00 573.30 0.0416
413.00 573.86 0.0420
428.00 542.99 0.0380
428.00 543.65 0.0380
429.00 543.13 0.0383
429.00 543.28 0.0385
429.00 543.46 0.0380
502.00 603.20 0.0457
503.00 603.33 0.0460
504.00 603.46 0.0464
504.00 603.61 0.0466
508.00 510.36 0.0349
508.00 510.51 0.0348
509.00 510.68 0.0348
510.00 510.86 0.0347
511.00 511.07 0.0347
514.00 542.99 0.0387
515.00 543.11 0.0389
516.00 543.24 0.0391
517.00 543.39 0.0390
518.00 543.56 0.0391
562.00 573.29 0.0427
562.00 573.41 0.0426
563.00 573.52 0.0429
565.00 573.64 0.0433
567.00 573.77 0.0437
656.00 542.99 0.0380
656.00 543.13 0.0380
657.00 543.27 0.0382
658.00 543.42 0.0385
659.00 543.58 0.0388
Reference

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [139.89; 553.53] J/mol×K [200.00; 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 A1.23230e+02
Coefficient B-8.35510e+02
Coefficient C7.09524e+00
Coefficient D-5.54510e-04
Coefficient E1.59120e-07
Temperature range, min.200.00
Temperature range, max.1500.00
Cp,gas 139.89 J/mol×K 200.00 Calculated Property
Cp,gas 213.02 J/mol×K 344.44 Calculated Property
Cp,gas 296.21 J/mol×K 488.89 Calculated Property
Cp,gas 365.16 J/mol×K 633.33 Calculated Property
Cp,gas 417.94 J/mol×K 777.78 Calculated Property
Cp,gas 457.92 J/mol×K 922.22 Calculated Property
Cp,gas 488.82 J/mol×K 1066.67 Calculated Property
Cp,gas 513.64 J/mol×K 1211.11 Calculated Property
Cp,gas 534.65 J/mol×K 1355.56 Calculated Property
Cp,gas 553.53 J/mol×K 1500.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [191.63; 321.77] J/mol×K [178.25; 429.90] 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 A4.75690e+01
Coefficient B3.99030e+01
Coefficient C4.10124e+00
Coefficient D3.84360e-03
Coefficient E-1.25830e-06
Temperature range, min.178.25
Temperature range, max.429.90
Cp,liquid 191.63 J/mol×K 178.25 Calculated Property
Cp,liquid 201.09 J/mol×K 206.21 Calculated Property
Cp,liquid 212.04 J/mol×K 234.17 Calculated Property
Cp,liquid 224.28 J/mol×K 262.13 Calculated Property
Cp,liquid 237.74 J/mol×K 290.09 Calculated Property
Cp,liquid 252.34 J/mol×K 318.06 Calculated Property
Cp,liquid 268.06 J/mol×K 346.02 Calculated Property
Cp,liquid 284.88 J/mol×K 373.98 Calculated Property
Cp,liquid 302.79 J/mol×K 401.94 Calculated Property
Cp,liquid 321.77 J/mol×K 429.90 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0023445; 0.0002971] Pa×s [248.15; 429.90] 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-1.89640e+01
Coefficient B1.76830e+03
Coefficient C1.01330e+00
Coefficient D3.16660e-06
Coefficient E2.00000e+00
Temperature range, min.248.15
Temperature range, max.429.90
η 0.0023445 Pa×s 248.15 Calculated Property
η 0.0015343 Pa×s 268.34 Calculated Property
η 0.0010790 Pa×s 288.54 Calculated Property
η 0.0008040 Pa×s 308.73 Calculated Property
η 0.0006283 Pa×s 328.93 Calculated Property
η 0.0005107 Pa×s 349.12 Calculated Property
η 0.0004291 Pa×s 369.32 Calculated Property
η 0.0003709 Pa×s 389.51 Calculated Property
η 0.0003285 Pa×s 409.71 Calculated Property
η 0.0002971 Pa×s 429.90 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [52.16; 0.00] kJ/mol [178.25; 639.15] 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 A6.80860e+01
Coefficient B1.25480e+00
Coefficient C-2.11930e+00
Coefficient D2.18090e+00
Coefficient E-8.44740e-01
Critical temperature, Tc (K)6.39150e+02
Temperature range, min.178.25
Temperature range, max.639.15
ΔvapH 52.16 kJ/mol 178.25 Calculated Property
ΔvapH 49.08 kJ/mol 229.46 Calculated Property
ΔvapH 46.13 kJ/mol 280.67 Calculated Property
ΔvapH 43.11 kJ/mol 331.88 Calculated Property
ΔvapH 39.83 kJ/mol 383.09 Calculated Property
ΔvapH 36.14 kJ/mol 434.31 Calculated Property
ΔvapH 31.84 kJ/mol 485.52 Calculated Property
ΔvapH 26.62 kJ/mol 536.73 Calculated Property
ΔvapH 19.61 kJ/mol 587.94 Calculated Property
ΔvapH 0.00 kJ/mol 639.15 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.64] kPa [310.03; 459.04] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.40078e+01
Coefficient B-3.53909e+03
Coefficient C-5.20770e+01
Temperature range, min.310.03
Temperature range, max.459.04
Pvap 1.33 kPa 310.03 Calculated Property
Pvap 3.05 kPa 326.59 Calculated Property
Pvap 6.35 kPa 343.14 Calculated Property
Pvap 12.22 kPa 359.70 Calculated Property
Pvap 21.99 kPa 376.26 Calculated Property
Pvap 37.38 kPa 392.81 Calculated Property
Pvap 60.49 kPa 409.37 Calculated Property
Pvap 93.80 kPa 425.93 Calculated Property
Pvap 140.14 kPa 442.48 Calculated Property
Pvap 202.64 kPa 459.04 Calculated Property
Pvap [8.35e-07; 2809.33] kPa [178.25; 639.15] 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 A7.60502e+01
Coefficient B-7.87170e+03
Coefficient C-8.87590e+00
Coefficient D3.78420e-06
Coefficient E2.00000e+00
Temperature range, min.178.25
Temperature range, max.639.15
Pvap 8.35e-07 kPa 178.25 Calculated Property
Pvap 1.83e-03 kPa 229.46 Calculated Property
Pvap 0.18 kPa 280.67 Calculated Property
Pvap 3.41 kPa 331.88 Calculated Property
Pvap 26.09 kPa 383.09 Calculated Property
Pvap 113.21 kPa 434.31 Calculated Property
Pvap 340.33 kPa 485.52 Calculated Property
Pvap 800.23 kPa 536.73 Calculated Property
Pvap 1589.91 kPa 587.94 Calculated Property
Pvap 2809.33 kPa 639.15 Calculated Property
Pvap [8.61e-07; 2772.59] kPa [178.28; 639.15] 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 A7.62408e+01
Coefficient B-7.87048e+03
Coefficient C-8.90935e+00
Coefficient D3.80979e-06
Coefficient E0.00000e+00
Temperature range, min.178.28
Temperature range, max.639.15
Pvap 8.61e-07 kPa 178.28 Calculated Property
Pvap 1.87e-03 kPa 229.49 Calculated Property
Pvap 0.18 kPa 280.70 Calculated Property
Pvap 3.42 kPa 331.90 Calculated Property
Pvap 26.07 kPa 383.11 Calculated Property
Pvap 112.69 kPa 434.32 Calculated Property
Pvap 337.75 kPa 485.53 Calculated Property
Pvap 792.32 kPa 536.73 Calculated Property
Pvap 1571.31 kPa 587.94 Calculated Property
Pvap 2772.59 kPa 639.15 Calculated Property
Pvap [6.39; 103.96] kPa [345.84; 430.89] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.38467e+01
Coefficient B-3.36572e+03
Coefficient C-6.51600e+01
ReferenceForziati, Norris, et al., 1949, 2
Temperature range, min.345.84
Temperature range, max.430.89
Pvap 6.39 kPa 345.84 Calculated Property
Pvap 9.45 kPa 355.29 Calculated Property
Pvap 13.63 kPa 364.74 Calculated Property
Pvap 19.21 kPa 374.19 Calculated Property
Pvap 26.54 kPa 383.64 Calculated Property
Pvap 35.99 kPa 393.09 Calculated Property
Pvap 47.97 kPa 402.54 Calculated Property
Pvap 62.96 kPa 411.99 Calculated Property
Pvap 81.44 kPa 421.44 Calculated Property
Pvap 103.96 kPa 430.89 Calculated Property
Pvap [6.39; 103.96] kPa [345.84; 430.89] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.38467e+01
Coefficient B-3.36572e+03
Coefficient C-6.51600e+01
ReferenceForziati, Norris, et al., 1949
Temperature range, min.345.84
Temperature range, max.430.89
Pvap 6.39 kPa 345.84 Calculated Property
Pvap 9.45 kPa 355.29 Calculated Property
Pvap 13.63 kPa 364.74 Calculated Property
Pvap 19.21 kPa 374.19 Calculated Property
Pvap 26.54 kPa 383.64 Calculated Property
Pvap 35.99 kPa 393.09 Calculated Property
Pvap 47.97 kPa 402.54 Calculated Property
Pvap 62.96 kPa 411.99 Calculated Property
Pvap 81.44 kPa 421.44 Calculated Property
Pvap 103.96 kPa 430.89 Calculated Property
Property Value Unit Temperature (K) Source
ρl [876.24; 263.61] kg/m3 [178.25; 639.15] 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 A7.01032e+01
Coefficient B2.65940e-01
Coefficient C6.39150e+02
Coefficient D2.98860e-01
Temperature range, min.178.25
Temperature range, max.639.15
ρl 876.24 kg/m3 178.25 Calculated Property
ρl 840.58 kg/m3 229.46 Calculated Property
ρl 803.30 kg/m3 280.67 Calculated Property
ρl 763.99 kg/m3 331.88 Calculated Property
ρl 722.07 kg/m3 383.09 Calculated Property
ρl 676.62 kg/m3 434.31 Calculated Property
ρl 626.07 kg/m3 485.52 Calculated Property
ρl 567.21 kg/m3 536.73 Calculated Property
ρl 491.45 kg/m3 587.94 Calculated Property
ρl 263.61 kg/m3 639.15 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.04; 1.65e-05] N/m [178.25; 635.46] 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-1.10290e-02
Coefficient B3.12010e+01
Coefficient C-3.10620e+00
Coefficient D1.69420e-04
Coefficient E-3.85400e-06
CommentRange stopped where the equation turns negative; ChemSep gives it to 639.15 K.
Temperature range, min.178.25
Temperature range, max.635.46
γ 0.04 N/m 178.25 Calculated Property
γ 0.03 N/m 229.05 Calculated Property
γ 0.03 N/m 279.85 Calculated Property
γ 0.02 N/m 330.65 Calculated Property
γ 0.02 N/m 381.46 Calculated Property
γ 0.01 N/m 432.26 Calculated Property
γ 0.01 N/m 483.06 Calculated Property
γ 0.01 N/m 533.86 Calculated Property
γ 0.00 N/m 584.66 Calculated Property
γ 1.65e-05 N/m 635.46 Calculated Property
Property Value Unit Temperature (K) Source
λgas [0.00; 0.09] W/m×K [178.25; 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 A1.20500e-06
Coefficient B1.62220e+00
Coefficient C-4.29450e+01
Coefficient D1.57390e+04
Temperature range, min.178.25
Temperature range, max.1000.00
λgas 0.00 W/m×K 178.25 Calculated Property
λgas 0.01 W/m×K 269.56 Calculated Property
λgas 0.02 W/m×K 360.86 Calculated Property
λgas 0.02 W/m×K 452.17 Calculated Property
λgas 0.03 W/m×K 543.47 Calculated Property
λgas 0.04 W/m×K 634.78 Calculated Property
λgas 0.05 W/m×K 726.08 Calculated Property
λgas 0.07 W/m×K 817.39 Calculated Property
λgas 0.08 W/m×K 908.69 Calculated Property
λgas 0.09 W/m×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
λliquid [0.14; 0.09] W/m×K [178.25; 429.90] 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-4.97420e-02
Coefficient B3.30350e+00
Coefficient C-1.58140e+00
Coefficient D-4.85710e-04
Coefficient E-1.01500e-06
Temperature range, min.178.25
Temperature range, max.429.90
λliquid 0.14 W/m×K 178.25 Calculated Property
λliquid 0.13 W/m×K 206.21 Calculated Property
λliquid 0.13 W/m×K 234.17 Calculated Property
λliquid 0.12 W/m×K 262.13 Calculated Property
λliquid 0.12 W/m×K 290.09 Calculated Property
λliquid 0.11 W/m×K 318.06 Calculated Property
λliquid 0.11 W/m×K 346.02 Calculated Property
λliquid 0.10 W/m×K 373.98 Calculated Property
λliquid 0.10 W/m×K 401.94 Calculated Property
λliquid 0.09 W/m×K 429.90 Calculated Property

Similar Compounds

BUTYLCYCLOHEXANE. 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 Cyclohexane, propyl-.

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