Chemical Properties of Cycloheptane (CAS 291-64-5)

Cycloheptane

InChI
InChI=1S/C7H14/c1-2-4-6-7-5-3-1/h1-7H2
InChI Key
DMEGYFMYUHOHGS-UHFFFAOYSA-N
Formula
C7H14
SMILES
C1CCCCCC1
Molecular Weight1
98.19
CAS
291-64-5
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Physical Properties

Property Value Unit Source
ω [0.2370; 0.3359]   Show Hide
ω 0.2384 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω 0.3359 Passut and Danner (1973), critical constants and acentric factors Compiled value
ω 0.2370 KDB
ΔcH°liquid [-4598.90; -4586.50] kJ/mol Show Hide
ΔcH°liquid -4597.00 ± 0.80 kJ/mol NIST
ΔcH°liquid -4597.60 ± 0.60 kJ/mol NIST
ΔcH°liquid -4598.90 ± 1.70 kJ/mol NIST
ΔcH°liquid -4586.50 kJ/mol NIST
ΔfG° 63.05 kJ/mol KDB
Δc,grossH 4597.80 kJ/mol KDB
Δc,netH 4289.856 kJ/mol KDB
ΔfH°gas -119.40 kJ/mol KDB
ΔfH°liquid -156.40 ± 1.70 kJ/mol NIST
ΔfusH° 2.55 kJ/mol Joback Calculated Property
ΔvapH° [37.00; 39.40] kJ/mol Show Hide
ΔvapH° 38.50 kJ/mol NIST
ΔvapH° 38.50 ± 2.10 kJ/mol NIST
ΔvapH° 38.50 ± 0.20 kJ/mol NIST
ΔvapH° 39.40 kJ/mol NIST
ΔvapH° Outlier 37.00 kJ/mol NIST
ΔvapH° 38.50 ± 2.10 kJ/mol NIST
ΔvapH° 38.50 ± 0.20 kJ/mol NIST
IE [9.82; 9.97] eV Show Hide
IE 9.90 ± 0.10 eV NIST
IE 9.82 ± 0.05 eV NIST
IE 9.96 eV NIST
IE 9.97 eV NIST
IE 9.88 ± 0.05 eV NIST
log10WS [-3.52; -3.51]   Show Hide
log10WS -3.52 Aq. Solubility Prediction
log10WS -3.51 Estimated Solubility
logPoct/wat 2.731 Crippen Calculated Property
McVol 98.630 ml/mol McGowan Calculated Property
Pc [3723.17; 3826.00] kPa Show Hide
Pc 3820.00 kPa IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Pc 3819.95 kPa PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc Outlier 3723.17 kPa Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc 3820.00 kPa KDB
Pc 3820.00 ± 40.00 kPa NIST
Pc 3813.00 ± 50.00 kPa NIST
Pc 3826.00 ± 40.53 kPa NIST
ρc 277.87 ± 3.93 kg/m3 NIST
Inp [784.00; 846.00]   Show Hide
Inp 787.00 NIST
Inp Outlier 837.50 NIST
Inp Outlier 836.00 NIST
Inp Outlier 837.00 NIST
Inp 794.20 NIST
Inp 800.00 NIST
Inp 806.90 NIST
Inp 819.00 NIST
Inp 800.00 NIST
Inp 789.00 NIST
Inp 788.00 NIST
Inp 789.00 NIST
Inp 815.00 NIST
Inp 811.60 NIST
Inp 791.00 NIST
Inp 804.00 NIST
Inp 811.00 NIST
Inp 829.00 NIST
Inp 807.00 NIST
Inp 803.00 NIST
Inp 784.00 NIST
Inp 812.00 NIST
Inp 786.00 NIST
Inp 795.00 NIST
Inp 800.00 NIST
Inp 806.00 NIST
Inp 816.00 NIST
Inp 804.00 NIST
Inp 824.00 NIST
Inp 819.00 NIST
Inp 787.00 NIST
Inp 794.00 NIST
Inp 786.00 NIST
Inp 796.00 NIST
Inp 796.00 NIST
Inp 790.00 NIST
Inp 800.00 NIST
Inp Outlier 846.00 NIST
Inp 803.00 NIST
Inp 797.00 NIST
Inp 807.00 NIST
Inp 800.00 NIST
Inp 800.00 NIST
Inp 786.00 NIST
Inp Outlier 837.50 NIST
Inp 806.90 NIST
Inp 789.00 NIST
Inp 811.00 NIST
Inp 812.00 NIST
Inp 816.00 NIST
Inp 800.00 NIST
Inp 819.00 NIST
Inp 796.00 NIST
Ip [878.00; 899.00]   Show Hide
Ip 899.00 NIST
Ip 878.00 NIST
Ip 892.00 NIST
Ip 883.00 NIST
Ip 899.00 NIST
Ip 883.00 NIST
S°gas 342.30 ± 1.30 J/mol×K NIST
S°liquid 242.55 J/mol×K NIST
Tboil [391.25; 393.00] K Show Hide
Tboil 391.63 K KDB
Tboil 391.70 K NIST
Tboil Outlier 393.00 ± 2.00 K NIST
Tboil 391.99 ± 0.20 K NIST
Tboil 391.99 ± 0.30 K NIST
Tboil 391.99 ± 0.30 K NIST
Tboil 391.63 ± 0.30 K NIST
Tboil 391.25 ± 0.60 K NIST
Tboil 392.15 ± 2.00 K NIST
Tc [589.26; 604.20] K Show Hide
Tc 604.20 K IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Tc 604.20 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc Outlier 589.26 K Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc 604.20 K KDB
Tc 604.20 ± 0.50 K NIST
Tc 604.20 ± 0.50 K NIST
Tfus [260.95; 265.20] K Show Hide
Tfus 265.15 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 265.12 K KDB
Tfus 264.69 ± 0.25 K NIST
Tfus 265.20 ± 2.00 K NIST
Tfus 265.02 ± 0.06 K NIST
Tfus 265.02 ± 0.04 K NIST
Tfus 265.05 ± 0.02 K NIST
Tfus Outlier 260.95 ± 0.30 K NIST
Ttriple [265.00; 265.12] K Show Hide
Ttriple 265.00 ± 0.07 K NIST
Ttriple 265.12 ± 0.05 K NIST
Ttriple 265.10 ± 3.00 K NIST
Ttriple 265.00 ± 0.07 K NIST
Ttriple 265.12 ± 0.05 K NIST
Vc [0.353; 0.354] m3/kmol Show Hide
Vc 0.353 m3/kmol IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Vc 0.353 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc 0.353 m3/kmol KDB
Vc 0.353 m3/kmol NIST
Vc 0.354 ± 0.007 m3/kmol NIST
Zc [0.2680000; 0.2684240]   Show Hide
Zc 0.2680000 IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Zc 0.2684240 KDB

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,liquid [170.00; 181.40] J/mol×K [270.00; 300.00] Show Hide
Cp,liquid 170.00 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
Cp,liquid 171.20 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
Cp,liquid 173.80 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
Cp,liquid 177.60 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
Cp,liquid 180.70 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
Cp,liquid 180.61 J/mol×K 298.15 NIST
Cp,liquid 180.47 J/mol×K 298.15 NIST
Cp,liquid 180.75 J/mol×K 298.15 NIST
Cp,liquid 181.40 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
ΔfusH [0.29; 4.98] kJ/mol [134.80; 265.10] Show Hide
ΔfusH 4.98 kJ/mol 134.80 NIST
ΔfusH 0.29 kJ/mol 198.20 NIST
ΔfusH 0.45 kJ/mol 212.40 NIST
ΔfusH 1.88 kJ/mol 265.10 NIST
ΔfusH 1.88 kJ/mol 265.10 NIST
ΔsubH 53.50 kJ/mol 134.00 NIST
ΔvapH [31.70; 38.60] kJ/mol [307.50; 540.00] Show Hide
ΔvapH 38.60 kJ/mol 307.50 NIST
ΔvapH 36.40 kJ/mol 365.50 NIST
ΔvapH 36.10 kJ/mol 387.00 NIST
ΔvapH 36.10 kJ/mol 387.00 NIST
ΔvapH 31.70 kJ/mol 540.00 NIST
n0 1.44240 298.15 KDB
ρl 810.00 kg/m3 293.00 KDB
ΔfusS [1.46; 36.94] J/mol×K [134.80; 265.10] Show Hide
ΔfusS 36.94 J/mol×K 134.80 NIST
ΔfusS 1.46 J/mol×K 198.20 NIST
ΔfusS 2.11 J/mol×K 212.40 NIST
ΔfusS 7.10 J/mol×K 265.10 NIST
γ 0.03 N/m 298.20 KDB
λliquid [0.11; 0.13] W/m×K [262.18; 320.36] Show Hide
λliquid 0.13 W/m×K 262.18 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.13 W/m×K 262.37 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.13 W/m×K 262.50 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.12 W/m×K 280.17 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.12 W/m×K 280.35 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.12 W/m×K 280.48 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.12 W/m×K 297.01 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.12 W/m×K 297.20 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.12 W/m×K 297.33 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.11 W/m×K 320.05 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.11 W/m×K 320.23 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.11 W/m×K 320.36 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [108.70; 360.66] J/mol×K [273.00; 1000.00] Joback Predicted correlation Show Hide
EquationY = A + B·T + C·T² + D·T³ + E·T⁴
Y is Cp,gas in J/mol×K, T in K
Coefficient A-8.01400e+01
Coefficient B8.07800e-01
Coefficient C-4.47000e-04
Coefficient D8.00000e-08
Coefficient E0.00000e+00
Temperature range, min.273.00
Temperature range, max.1000.00
Cp,gas 108.70 J/mol×K 273.00 Calculated Property
Cp,gas 153.24 J/mol×K 353.78 Calculated Property
Cp,gas 193.05 J/mol×K 434.56 Calculated Property
Cp,gas 228.39 J/mol×K 515.33 Calculated Property
Cp,gas 259.50 J/mol×K 596.11 Calculated Property
Cp,gas 286.66 J/mol×K 676.89 Calculated Property
Cp,gas 310.09 J/mol×K 757.67 Calculated Property
Cp,gas 330.07 J/mol×K 838.44 Calculated Property
Cp,gas 346.84 J/mol×K 919.22 Calculated Property
Cp,gas 360.66 J/mol×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0017742; 0.0001985] Pa×s [265.04; 422.94] Joback Predicted correlation Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is η in Pa×s, T in K
Coefficient A-1.22011e+01
Coefficient B1.55489e+03
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
CommentLiquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc.
Temperature range, min.265.04
Temperature range, max.422.94
η 0.0017742 Pa×s 265.04 Calculated Property
η 0.0012326 Pa×s 282.58 Calculated Property
η 0.0008936 Pa×s 300.13 Calculated Property
η 0.0006712 Pa×s 317.67 Calculated Property
η 0.0005195 Pa×s 335.22 Calculated Property
η 0.0004125 Pa×s 352.76 Calculated Property
η 0.0003347 Pa×s 370.31 Calculated Property
η 0.0002768 Pa×s 387.85 Calculated Property
η 0.0002327 Pa×s 405.40 Calculated Property
η 0.0001985 Pa×s 422.94 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [0.39; 202.67] kPa [265.12; 418.93] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.41291e+01
Coefficient B-3.26491e+03
Coefficient C-4.86550e+01
Temperature range, min.265.12
Temperature range, max.418.93
Pvap 0.39 kPa 265.12 Calculated Property
Pvap 1.16 kPa 282.21 Calculated Property
Pvap 3.01 kPa 299.30 Calculated Property
Pvap 6.92 kPa 316.39 Calculated Property
Pvap 14.39 kPa 333.48 Calculated Property
Pvap 27.53 kPa 350.57 Calculated Property
Pvap 49.13 kPa 367.66 Calculated Property
Pvap 82.67 kPa 384.75 Calculated Property
Pvap 132.28 kPa 401.84 Calculated Property
Pvap 202.67 kPa 418.93 Calculated Property
Pvap [0.39; 3831.50] kPa [265.12; 604.30] 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 A8.37466e+01
Coefficient B-7.38221e+03
Coefficient C-1.02752e+01
Coefficient D6.91167e-06
Coefficient E0.00000e+00
Temperature range, min.265.12
Temperature range, max.604.30
Pvap 0.39 kPa 265.12 Calculated Property
Pvap 3.66 kPa 302.81 Calculated Property
Pvap 19.26 kPa 340.49 Calculated Property
Pvap 68.53 kPa 378.18 Calculated Property
Pvap 186.24 kPa 415.87 Calculated Property
Pvap 418.69 kPa 453.55 Calculated Property
Pvap 822.00 kPa 491.24 Calculated Property
Pvap 1463.67 kPa 528.93 Calculated Property
Pvap 2428.81 kPa 566.61 Calculated Property
Pvap 3831.50 kPa 604.30 Calculated Property
Pvap [19.88; 270.07] kPa [341.30; 432.17] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.37628e+01
Coefficient B-3.06336e+03
Coefficient C-5.69460e+01
ReferenceFinke, Scott, et al., 1956
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.341.30
Temperature range, max.432.17
Pvap 19.88 kPa 341.30 Calculated Property
Pvap 28.76 kPa 351.40 Calculated Property
Pvap 40.61 kPa 361.49 Calculated Property
Pvap 56.08 kPa 371.59 Calculated Property
Pvap 75.91 kPa 381.69 Calculated Property
Pvap 100.88 kPa 391.78 Calculated Property
Pvap 131.86 kPa 401.88 Calculated Property
Pvap 169.75 kPa 411.98 Calculated Property
Pvap 215.49 kPa 422.07 Calculated Property
Pvap 270.07 kPa 432.17 Calculated Property
Pvap [19.88; 270.07] kPa [341.30; 432.17] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.37628e+01
Coefficient B-3.06336e+03
Coefficient C-5.69460e+01
ReferenceFinke, Scott, et al., 1956, 3
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.341.30
Temperature range, max.432.17
Pvap 19.88 kPa 341.30 Calculated Property
Pvap 28.76 kPa 351.40 Calculated Property
Pvap 40.61 kPa 361.49 Calculated Property
Pvap 56.08 kPa 371.59 Calculated Property
Pvap 75.91 kPa 381.69 Calculated Property
Pvap 100.88 kPa 391.78 Calculated Property
Pvap 131.86 kPa 401.88 Calculated Property
Pvap 169.75 kPa 411.98 Calculated Property
Pvap 215.49 kPa 422.07 Calculated Property
Pvap 270.07 kPa 432.17 Calculated Property

Similar Compounds

Cyclooctane. Cyclotetracosane. Cyclotriacontane. CYCLOEICOSANE. Cycloundecane. Cyclooctadecane. Cyclotetradecane. Cyclohexadecane. Cyclopentadecane. Cyclodecane. Cyclononane. Cyclododecane. Cyclotridecane. Cyclooctacosane. Cyclohexyl radical.

Find more compounds similar to Cycloheptane.

Mixtures

Sources

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. Take the time to validate and double check the source of the data.
Outlier This icon means that the value is more than 2 standard deviations away from the property mean.
Calculated This icon marks a calculated value or equation: a prediction, not a measurement.
Compiled This icon marks a compiled value or equation: taken from a data compilation such as ChemSep, not from an original measurement report.
These property values are available through the Cheméo API. A free account gives you an access key.