Property | Value | Unit | Source |
---|---|---|---|
ω | 0.4910 | KDB | |
ΔcH°liquid | -1844.90 ± 0.46 | kJ/mol | NIST |
EA | [1.02; 1.06] | eV |
![]() |
EA | 1.02 ± 0.06 | eV | NIST |
EA | 1.06 ± 0.13 | eV | NIST |
ΔfG° | -2763.48 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-2898.00; -2897.20] | kJ/mol |
![]() |
ΔfH°gas | -2898.00 | kJ/mol | KDB |
ΔfH°gas | -2897.20 ± 3.80 | kJ/mol | NIST |
ΔfH°liquid | -2931.10 ± 3.80 | kJ/mol | NIST |
ΔfusH° | 8.99 | kJ/mol | Joback Calculated Property |
ΔvapH° | [33.90; 34.10] | kJ/mol |
![]() |
ΔvapH° | 34.00 | kJ/mol | NIST |
ΔvapH° | 34.10 ± 0.30 | kJ/mol | NIST |
ΔvapH° | 33.90 ± 0.20 | kJ/mol | NIST |
log10WS | -4.85 | Crippen Calculated Property | |
logPoct/wat | 4.447 | Crippen Calculated Property | |
McVol | 123.410 | ml/mol | McGowan Calculated Property |
Pc | [2018.71; 2019.00] | kPa |
![]() |
Pc | 2019.00 | kPa | KDB |
Pc | Outlier 2018.71 ± 10.00 | kPa | NIST |
Pc | 2019.00 ± 3.00 | kPa | NIST |
Pc | 2019.00 ± 3.00 | kPa | NIST |
Pc | 2019.00 ± 3.00 | kPa | NIST |
Pc | 2019.00 ± 3.00 | kPa | NIST |
Pc | 2019.00 ± 3.00 | kPa | NIST |
ρc | 612.59 ± 7.00 | kg/m3 | NIST |
Inp | [290.00; 303.00] |
![]() |
|
Inp | 303.00 | NIST | |
Inp | 290.00 | NIST | |
Tboil | [349.00; 349.56] | K |
![]() |
Tboil | 349.50 | K | KDB |
Tboil | 349.00 | K | NIST |
Tboil | 349.30 | K | NIST |
Tboil | 349.56 ± 0.10 | K | NIST |
Tboil | 349.53 ± 0.20 | K | NIST |
Tboil | 349.55 ± 0.40 | K | NIST |
Tboil | 349.20 ± 2.00 | K | NIST |
Tc | 485.91 | K | KDB |
Tfus | 228.40 | K | KDB |
Vc | 0.570 | m3/kmol | KDB |
Zc | 0.2848520 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [282.13; 356.24] | J/mol×K | [343.75; 471.11] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 280 300 320 340 360 350 400 450 | ||||
Cp,gas | 282.13 | J/mol×K | 343.75 | Joback Calculated Property |
Cp,gas | 297.96 | J/mol×K | 364.98 | Joback Calculated Property |
Cp,gas | 312.25 | J/mol×K | 386.20 | Joback Calculated Property |
Cp,gas | 325.11 | J/mol×K | 407.43 | Joback Calculated Property |
Cp,gas | 336.66 | J/mol×K | 428.66 | Joback Calculated Property |
Cp,gas | 347.00 | J/mol×K | 449.88 | Joback Calculated Property |
Cp,gas | 356.24 | J/mol×K | 471.11 | Joback Calculated Property |
Cp,liquid | 353.10 | J/mol×K | 298.00 | NIST |
η | [0.0008074; 0.0010313] | Pa×s | [319.20; 333.11] | ![]() |
T(K) Dynamic viscosity (Pa×s) 8.00e-4 8.50e-4 9.00e-4 9.50e-4 1.00e-3 1.05e-3 320 325 330 | ||||
η | 0.0010313 | Pa×s | 319.20 | Shear V... |
η | 0.0010114 | Pa×s | 320.16 | Shear V... |
η | 0.0009582 | Pa×s | 323.18 | Shear V... |
η | 0.0008787 | Pa×s | 328.13 | Shear V... |
η | 0.0008074 | Pa×s | 333.11 | Shear V... |
ΔsubH | 51.60 | kJ/mol | 234.00 | NIST |
ΔvapH | [30.20; 33.80] | kJ/mol | [310.50; 450.50] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 30 31 32 33 34 350 400 450 | ||||
ΔvapH | 33.30 | kJ/mol | 310.50 | NIST |
ΔvapH | 33.80 | kJ/mol | 325.50 | NIST |
ΔvapH | 33.40 | kJ/mol | 345.00 | NIST |
ΔvapH | 33.30 | kJ/mol | 345.00 | NIST |
ΔvapH | 33.10 | kJ/mol | 359.50 | NIST |
ΔvapH | 30.20 | kJ/mol | 450.50 | NIST |
ν | [0.0000007; 0.0000009] | m2/s | [298.15; 318.15] | ![]() |
T(K) Kinematic viscosity (m2/s) 7.00e-7 7.50e-7 8.00e-7 8.50e-7 9.00e-7 9.50e-7 300 305 310 315 | ||||
ν | 0.0000009 | m2/s | 298.15 | Viscosi... |
ν | 0.0000008 | m2/s | 303.15 | Viscosi... |
ν | 0.0000008 | m2/s | 308.15 | Viscosi... |
ν | 0.0000007 | m2/s | 313.15 | Viscosi... |
ν | 0.0000007 | m2/s | 318.15 | Viscosi... |
ρl | [1656.30; 1841.00] | kg/m3 | [278.15; 343.15] | ![]() |
T(K) Liquid Density (kg/m3) 1650 1700 1750 1800 1850 280 300 320 340 | ||||
ρl | 1841.00 | kg/m3 | 278.15 | Liquid ... |
ρl | 1827.60 | kg/m3 | 283.15 | Liquid ... |
ρl | 1814.00 | kg/m3 | 288.15 | Liquid ... |
ρl | 1800.40 | kg/m3 | 293.15 | Liquid ... |
ρl | 1789.00 | kg/m3 | 298.00 | KDB |
ρl | 1786.60 | kg/m3 | 298.15 | Liquid ... |
ρl | 1772.70 | kg/m3 | 303.15 | Liquid ... |
ρl | 1758.70 | kg/m3 | 308.15 | Liquid ... |
ρl | 1744.50 | kg/m3 | 313.15 | Liquid ... |
ρl | 1730.30 | kg/m3 | 318.15 | Liquid ... |
ρl | 1715.80 | kg/m3 | 323.15 | Liquid ... |
ρl | 1701.20 | kg/m3 | 328.15 | Liquid ... |
ρl | 1686.40 | kg/m3 | 333.15 | Liquid ... |
ρl | 1671.50 | kg/m3 | 338.15 | Liquid ... |
ρl | 1656.30 | kg/m3 | 343.15 | Liquid ... |
γ | [0.01; 0.02] | N/m | [286.75; 313.65] | ![]() |
T(K) Surface Tension (N/m) 0.01 0.01 0.01 0.02 0.02 0.02 0.02 290 300 310 | ||||
γ | 0.02 | N/m | 286.75 | Surface... |
γ | 0.02 | N/m | 293.25 | Surface... |
γ | 0.02 | N/m | 298.35 | Surface... |
γ | 0.01 | N/m | 303.35 | Surface... |
γ | 0.01 | N/m | 308.55 | Surface... |
γ | 0.01 | N/m | 313.65 | Surface... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.05; 202.64] | kPa | [252.15; 414.84] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.17838e+01 | |||
Coefficient B | -2.34793e+03 | |||
Coefficient C | -5.20770e+01 | |||
Temperature range, min. | 252.15 | |||
Temperature range, max. | 414.84 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 350 400 | ||||
Pvap | 1.05 | kPa | 252.15 | Calculated Property |
Pvap | 2.78 | kPa | 270.23 | Calculated Property |
Pvap | 6.32 | kPa | 288.30 | Calculated Property |
Pvap | 12.82 | kPa | 306.38 | Calculated Property |
Pvap | 23.66 | kPa | 324.46 | Calculated Property |
Pvap | 40.45 | kPa | 342.53 | Calculated Property |
Pvap | 64.96 | kPa | 360.61 | Calculated Property |
Pvap | 98.99 | kPa | 378.69 | Calculated Property |
Pvap | 144.31 | kPa | 396.76 | Calculated Property |
Pvap | 202.64 | kPa | 414.84 | Calculated Property |
Pvap | [18.55; 1906.00] | kPa | [306.00; 483.38] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 2.96012e+02 | |||
Coefficient B | -1.49161e+04 | |||
Coefficient C | -4.34642e+01 | |||
Coefficient D | 4.72597e-05 | |||
Temperature range, min. | 306.00 | |||
Temperature range, max. | 483.38 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 350 400 450 | ||||
Pvap | 18.55 | kPa | 306.00 | Calculated Property |
Pvap | 42.33 | kPa | 325.71 | Calculated Property |
Pvap | 83.94 | kPa | 345.42 | Calculated Property |
Pvap | 150.07 | kPa | 365.13 | Calculated Property |
Pvap | 248.85 | kPa | 384.84 | Calculated Property |
Pvap | 391.34 | kPa | 404.54 | Calculated Property |
Pvap | 593.99 | kPa | 424.25 | Calculated Property |
Pvap | 882.45 | kPa | 443.96 | Calculated Property |
Pvap | 1297.64 | kPa | 463.67 | Calculated Property |
Pvap | 1906.00 | kPa | 483.38 | Calculated Property |
Find more compounds similar to Perfluoro(methylcyclohexane).
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.