Property | Value | Unit | Source |
---|---|---|---|
PAff | 784.50 | kJ/mol | NIST |
BasG | 752.00 | kJ/mol | NIST |
ΔcH°liquid | [-3761.00; -3751.50] | kJ/mol |
![]() |
ΔcH°liquid | -3752.39 ± 0.49 | kJ/mol | NIST |
ΔcH°liquid | -3752.00 ± 0.50 | kJ/mol | NIST |
ΔcH°liquid | -3751.50 ± 0.50 | kJ/mol | NIST |
ΔcH°liquid | -3761.00 | kJ/mol | NIST |
ΔfG° | 61.76 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-7.10; -4.32] | kJ/mol |
![]() |
ΔfH°gas | -4.32 ± 0.98 | kJ/mol | NIST |
ΔfH°gas | -4.70 | kJ/mol | NIST |
ΔfH°gas | -5.30 | kJ/mol | NIST |
ΔfH°gas | -7.10 | kJ/mol | NIST |
ΔfH°liquid | [-40.60; -37.80] | kJ/mol |
![]() |
ΔfH°liquid | -37.80 ± 8.20 | kJ/mol | NIST |
ΔfH°liquid | -38.20 ± 0.59 | kJ/mol | NIST |
ΔfH°liquid | -38.80 ± 0.59 | kJ/mol | NIST |
ΔfH°liquid | -40.60 ± 0.79 | kJ/mol | NIST |
ΔfusH° | 3.28 | kJ/mol | Joback Calculated Property |
ΔvapH° | [30.50; 33.57] | kJ/mol |
![]() |
ΔvapH° | 33.57 | kJ/mol | NIST |
ΔvapH° | 33.50 ± 0.53 | kJ/mol | NIST |
ΔvapH° | 33.50 | kJ/mol | NIST |
ΔvapH° | 33.50 ± 0.50 | kJ/mol | NIST |
ΔvapH° | 30.50 ± 0.30 | kJ/mol | NIST |
IE | [8.92; 9.57] | eV |
![]() |
IE | 8.95 ± 0.01 | eV | NIST |
IE | 8.94 | eV | NIST |
IE | 8.94 ± 0.02 | eV | NIST |
IE | 8.95 | eV | NIST |
IE | 8.94 ± 0.01 | eV | NIST |
IE | Outlier 9.57 ± 0.05 | eV | NIST |
IE | 8.99 | eV | NIST |
IE | 8.92 | eV | NIST |
IE | 8.95 ± 0.01 | eV | NIST |
IE | 8.94 | eV | NIST |
IE | 8.92 ± 0.02 | eV | NIST |
IE | 8.95 ± 0.01 | eV | NIST |
IE | 9.09 | eV | NIST |
IE | 9.12 | eV | NIST |
IE | 9.12 | eV | NIST |
IE | 9.12 | eV | NIST |
IE | 9.11 | eV | NIST |
log10WS | [-2.59; -2.59] |
![]() |
|
log10WS | -2.59 | Aq. Sol... | |
log10WS | -2.59 | Estimat... | |
logPoct/wat | 2.117 | Crippen Calculated Property | |
McVol | 80.240 | ml/mol | McGowan Calculated Property |
NFPA Fire | 3 | KDB | |
NFPA Health | 1 | KDB | |
Pc | 4328.25 | kPa | Joback Calculated Property |
Inp | [643.00; 714.00] |
![]() |
|
Inp | Outlier 705.00 | NIST | |
Inp | 685.00 | NIST | |
Inp | 689.00 | NIST | |
Inp | 671.00 | NIST | |
Inp | Outlier 704.40 | NIST | |
Inp | 688.00 | NIST | |
Inp | 683.00 | NIST | |
Inp | 680.50 | NIST | |
Inp | 676.80 | NIST | |
Inp | 698.00 | NIST | |
Inp | 693.00 | NIST | |
Inp | 688.00 | NIST | |
Inp | 684.00 | NIST | |
Inp | 688.00 | NIST | |
Inp | 683.00 | NIST | |
Inp | 687.50 | NIST | |
Inp | 674.00 | NIST | |
Inp | 674.00 | NIST | |
Inp | 700.00 | NIST | |
Inp | 690.00 | NIST | |
Inp | 694.00 | NIST | |
Inp | 681.00 | NIST | |
Inp | 685.10 | NIST | |
Inp | 675.90 | NIST | |
Inp | Outlier 704.00 | NIST | |
Inp | 682.00 | NIST | |
Inp | 671.00 | NIST | |
Inp | 675.70 | NIST | |
Inp | 667.00 | NIST | |
Inp | 669.00 | NIST | |
Inp | 673.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 683.00 | NIST | |
Inp | 670.50 | NIST | |
Inp | 670.40 | NIST | |
Inp | 672.40 | NIST | |
Inp | 672.40 | NIST | |
Inp | 669.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 685.00 | NIST | |
Inp | 687.00 | NIST | |
Inp | 666.00 | NIST | |
Inp | 683.00 | NIST | |
Inp | 702.00 | NIST | |
Inp | 687.00 | NIST | |
Inp | 666.00 | NIST | |
Inp | 685.00 | NIST | |
Inp | 668.30 | NIST | |
Inp | 674.40 | NIST | |
Inp | 679.00 | NIST | |
Inp | 668.00 | NIST | |
Inp | 674.00 | NIST | |
Inp | 679.00 | NIST | |
Inp | 679.00 | NIST | |
Inp | 680.00 | NIST | |
Inp | Outlier 707.00 | NIST | |
Inp | 667.00 | NIST | |
Inp | 673.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 681.00 | NIST | |
Inp | 689.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 681.00 | NIST | |
Inp | 695.00 | NIST | |
Inp | 667.00 | NIST | |
Inp | 673.60 | NIST | |
Inp | 673.00 | NIST | |
Inp | 667.00 | NIST | |
Inp | 687.40 | NIST | |
Inp | 701.10 | NIST | |
Inp | 677.10 | NIST | |
Inp | 676.70 | NIST | |
Inp | 678.80 | NIST | |
Inp | 677.10 | NIST | |
Inp | 676.70 | NIST | |
Inp | 678.80 | NIST | |
Inp | 667.76 | NIST | |
Inp | 667.80 | NIST | |
Inp | 667.00 | NIST | |
Inp | 667.00 | NIST | |
Inp | 667.00 | NIST | |
Inp | 667.00 | NIST | |
Inp | Outlier 643.00 | NIST | |
Inp | 683.00 | NIST | |
Inp | 674.00 | NIST | |
Inp | 666.00 | NIST | |
Inp | 675.00 | NIST | |
Inp | 673.00 | NIST | |
Inp | 678.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 675.00 | NIST | |
Inp | 673.00 | NIST | |
Inp | 675.00 | NIST | |
Inp | 667.00 | NIST | |
Inp | 681.00 | NIST | |
Inp | 683.00 | NIST | |
Inp | 700.00 | NIST | |
Inp | 700.00 | NIST | |
Inp | Outlier 714.00 | NIST | |
Inp | 687.00 | NIST | |
Inp | 657.00 | NIST | |
Inp | 681.00 | NIST | |
Inp | 675.00 | NIST | |
Inp | 665.00 | NIST | |
Inp | 681.00 | NIST | |
Inp | 703.00 | NIST | |
Inp | 661.00 | NIST | |
Inp | 667.00 | NIST | |
Inp | 681.00 | NIST | |
Inp | Outlier 705.00 | NIST | |
Inp | 689.00 | NIST | |
Inp | 679.00 | NIST | |
Inp | 689.00 | NIST | |
Inp | 679.00 | NIST | |
I | [808.00; 850.00] |
![]() |
|
I | 822.00 | NIST | |
I | 850.00 | NIST | |
I | 832.00 | NIST | |
I | 841.00 | NIST | |
I | 825.00 | NIST | |
I | 850.00 | NIST | |
I | 849.70 | NIST | |
I | 832.40 | NIST | |
I | 840.90 | NIST | |
I | 849.70 | NIST | |
I | 832.40 | NIST | |
I | 840.90 | NIST | |
I | 808.00 | NIST | |
I | 808.00 | NIST | |
I | 808.00 | NIST | |
I | 811.00 | NIST | |
I | 808.00 | NIST | |
S°gas | 310.45 | J/mol×K | NIST |
S°liquid | [214.60; 216.70] | J/mol×K |
![]() |
S°liquid | 214.60 | J/mol×K | NIST |
S°liquid | 216.19 | J/mol×K | NIST |
S°liquid | 216.70 | J/mol×K | NIST |
Tboil | [355.97; 356.15] | K |
![]() |
Tboil | 356.13 | K | KDB |
Tboil | 355.97 | K | Isobari... |
Tboil | 356.15 | K | Vapor L... |
Tboil | 355.97 | K | Isobari... |
Tboil | 355.97 | K | Isobari... |
Tc | [553.50; 560.42] | K |
![]() |
Tc | 560.40 | K | KDB |
Tc | 560.40 ± 0.10 | K | NIST |
Tc | 560.40 | K | NIST |
Tc | 560.40 ± 0.30 | K | NIST |
Tc | 560.42 ± 0.02 | K | NIST |
Tc | Outlier 553.50 ± 0.15 | K | NIST |
Tfus | [168.00; 169.80] | K |
![]() |
Tfus | 169.60 | K | KDB |
Tfus | 169.27 | K | Aq. Sol... |
Tfus | 169.64 ± 0.06 | K | NIST |
Tfus | 169.45 ± 0.50 | K | NIST |
Tfus | 169.49 ± 0.20 | K | NIST |
Tfus | Outlier 168.00 ± 3.00 | K | NIST |
Tfus | 169.80 ± 0.30 | K | NIST |
Tfus | 169.00 ± 1.50 | K | NIST |
Tfus | 169.05 ± 0.20 | K | NIST |
Tfus | 169.10 ± 1.00 | K | NIST |
Tfus | 169.00 ± 0.30 | K | NIST |
Ttriple | [169.00; 169.67] | K |
![]() |
Ttriple | 169.66 ± 0.02 | K | NIST |
Ttriple | 169.67 ± 0.05 | K | NIST |
Ttriple | 169.00 ± 0.20 | K | NIST |
Vc | 0.291 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [133.47; 148.53] | J/mol×K | [370.00; 410.00] | ![]() |
Cp,gas | 133.47 | J/mol×K | 370.00 | NIST |
Cp,gas | 141.42 | J/mol×K | 390.00 | NIST |
Cp,gas | 148.53 | J/mol×K | 410.00 | NIST |
Cp,liquid | [145.60; 152.90] | J/mol×K | [293.20; 298.15] | ![]() |
Cp,liquid | 145.60 | J/mol×K | 293.20 | NIST |
Cp,liquid | 152.90 | J/mol×K | 298.12 | NIST |
Cp,liquid | 148.80 | J/mol×K | 298.15 | NIST |
Cp,liquid | 148.35 | J/mol×K | 298.15 | NIST |
Cp,liquid | 149.16 | J/mol×K | 298.15 | NIST |
η | [0.0002771; 0.0099936] | Pa×s | [169.76; 360.06] | ![]() |
η | 0.0099936 | Pa×s | 169.76 | Joback Calculated Property |
η | 0.0034351 | Pa×s | 201.48 | Joback Calculated Property |
η | 0.0015788 | Pa×s | 233.19 | Joback Calculated Property |
η | 0.0008741 | Pa×s | 264.91 | Joback Calculated Property |
η | 0.0005491 | Pa×s | 296.63 | Joback Calculated Property |
η | 0.0003774 | Pa×s | 328.34 | Joback Calculated Property |
η | 0.0002771 | Pa×s | 360.06 | Joback Calculated Property |
ΔfusH | [3.28; 4.23] | kJ/mol | [138.70; 169.70] | ![]() |
ΔfusH | 4.23 | kJ/mol | 138.70 | NIST |
ΔfusH | 3.28 | kJ/mol | 169.70 | NIST |
ΔfusH | 3.28 | kJ/mol | 169.70 | NIST |
ΔvapH | [30.46; 33.70] | kJ/mol | [260.50; 356.20] | ![]() |
ΔvapH | 32.60 | kJ/mol | 260.50 | NIST |
ΔvapH | 32.59 | kJ/mol | 300.00 | NIST |
ΔvapH | 32.70 ± 0.10 | kJ/mol | 313.00 | NIST |
ΔvapH | 33.10 | kJ/mol | 313.50 | NIST |
ΔvapH | 33.70 | kJ/mol | 321.00 | NIST |
ΔvapH | 32.20 ± 0.10 | kJ/mol | 323.00 | NIST |
ΔvapH | 31.70 ± 0.10 | kJ/mol | 333.00 | NIST |
ΔvapH | 32.90 | kJ/mol | 333.00 | NIST |
ΔvapH | 32.60 | kJ/mol | 334.00 | NIST |
ΔvapH | 32.80 | kJ/mol | 335.50 | NIST |
ΔvapH | 32.70 | kJ/mol | 337.00 | NIST |
ΔvapH | 31.20 ± 0.10 | kJ/mol | 343.00 | NIST |
ΔvapH | 30.70 ± 0.10 | kJ/mol | 353.00 | NIST |
ΔvapH | 30.46 | kJ/mol | 356.20 | NIST |
Pvap | [19.80; 101.80] | kPa | [310.15; 356.35] | ![]() |
Pvap | 19.80 | kPa | 310.15 | VLE and... |
Pvap | 24.94 | kPa | 315.56 | Isobari... |
Pvap | 27.43 | kPa | 318.01 | Isobari... |
Pvap | 29.98 | kPa | 320.26 | Isobari... |
Pvap | 29.70 | kPa | 320.35 | VLE and... |
Pvap | 32.47 | kPa | 322.34 | Isobari... |
Pvap | 34.95 | kPa | 324.31 | Isobari... |
Pvap | 37.52 | kPa | 326.23 | Isobari... |
Pvap | 39.98 | kPa | 327.96 | Isobari... |
Pvap | 39.70 | kPa | 328.05 | VLE and... |
Pvap | 42.45 | kPa | 329.61 | Isobari... |
Pvap | 45.01 | kPa | 331.23 | Isobari... |
Pvap | 47.48 | kPa | 332.73 | Isobari... |
Pvap | 49.60 | kPa | 334.20 | VLE and... |
Pvap | 50.02 | kPa | 334.22 | Isobari... |
Pvap | 52.51 | kPa | 335.62 | Isobari... |
Pvap | 55.02 | kPa | 336.98 | Isobari... |
Pvap | 57.52 | kPa | 338.27 | Isobari... |
Pvap | 59.98 | kPa | 339.52 | Isobari... |
Pvap | 59.60 | kPa | 339.55 | VLE and... |
Pvap | 62.46 | kPa | 340.73 | Isobari... |
Pvap | 65.02 | kPa | 341.94 | Isobari... |
Pvap | 67.51 | kPa | 343.07 | Isobari... |
Pvap | 69.97 | kPa | 344.16 | Isobari... |
Pvap | 69.70 | kPa | 344.25 | VLE and... |
Pvap | 72.51 | kPa | 345.27 | Isobari... |
Pvap | 74.96 | kPa | 346.30 | Isobari... |
Pvap | 77.48 | kPa | 347.33 | Isobari... |
Pvap | 80.02 | kPa | 348.35 | Isobari... |
Pvap | 79.80 | kPa | 348.45 | VLE and... |
Pvap | 82.52 | kPa | 349.31 | Isobari... |
Pvap | 84.99 | kPa | 350.26 | Isobari... |
Pvap | 87.45 | kPa | 351.18 | Isobari... |
Pvap | 89.96 | kPa | 352.09 | Isobari... |
Pvap | 89.80 | kPa | 352.20 | VLE and... |
Pvap | 92.46 | kPa | 352.97 | Isobari... |
Pvap | 95.01 | kPa | 353.85 | Isobari... |
Pvap | 97.52 | kPa | 354.71 | Isobari... |
Pvap | 101.33 | kPa | 355.97 | Isobari... |
Pvap | 101.33 | kPa | 356.15 | Vapor L... |
Pvap | 101.80 | kPa | 356.35 | VLE and... |
n0 | [1.44378; 1.44378] | [298.15; 298.15] | ![]() |
|
n0 | 1.44378 | 298.15 | Experim... | |
n0 | 1.44378 | 298.15 | Separat... | |
ρl | 805.69 | kg/m3 | 298.15 | Phase b... |
ΔfusS | [19.35; 30.50] | J/mol×K | [138.70; 169.70] | ![]() |
ΔfusS | 30.50 | J/mol×K | 138.70 | NIST |
ΔfusS | 19.35 | J/mol×K | 169.70 | NIST |
csound,fluid | [1169.60; 1252.10] | m/s | [303.15; 318.15] | ![]() |
csound,fluid | 1252.10 | m/s | 303.15 | Densiti... |
csound,fluid | 1224.80 | m/s | 308.15 | Densiti... |
csound,fluid | 1196.60 | m/s | 313.15 | Densiti... |
csound,fluid | 1169.60 | m/s | 318.15 | Densiti... |
λ | [0.12; 0.14] | W/m×K | [257.22; 328.22] | ![]() |
λ | 0.14 | W/m×K | 257.22 | Thermal... |
λ | 0.14 | W/m×K | 257.42 | Thermal... |
λ | 0.14 | W/m×K | 257.57 | Thermal... |
λ | 0.13 | W/m×K | 275.37 | Thermal... |
λ | 0.13 | W/m×K | 275.58 | Thermal... |
λ | 0.13 | W/m×K | 275.73 | Thermal... |
λ | 0.13 | W/m×K | 295.57 | Thermal... |
λ | 0.13 | W/m×K | 295.77 | Thermal... |
λ | 0.13 | W/m×K | 295.92 | Thermal... |
λ | 0.13 | W/m×K | 296.28 | Thermal... |
λ | 0.13 | W/m×K | 296.49 | Thermal... |
λ | 0.13 | W/m×K | 296.65 | Thermal... |
λ | 0.12 | W/m×K | 311.67 | Thermal... |
λ | 0.12 | W/m×K | 311.89 | Thermal... |
λ | 0.12 | W/m×K | 312.04 | Thermal... |
λ | 0.12 | W/m×K | 327.85 | Thermal... |
λ | 0.12 | W/m×K | 328.07 | Thermal... |
λ | 0.12 | W/m×K | 328.22 | Thermal... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [258.08; 380.72] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.41558e+01 | |||
Coefficient B | -2.99426e+03 | |||
Coefficient C | -4.21740e+01 | |||
Temperature range, min. | 258.08 | |||
Temperature range, max. | 380.72 | |||
Pvap | 1.33 | kPa | 258.08 | Calculated Property |
Pvap | 3.04 | kPa | 271.71 | Calculated Property |
Pvap | 6.31 | kPa | 285.33 | Calculated Property |
Pvap | 12.13 | kPa | 298.96 | Calculated Property |
Pvap | 21.82 | kPa | 312.59 | Calculated Property |
Pvap | 37.12 | kPa | 326.21 | Calculated Property |
Pvap | 60.14 | kPa | 339.84 | Calculated Property |
Pvap | 93.42 | kPa | 353.47 | Calculated Property |
Pvap | 139.83 | kPa | 367.09 | Calculated Property |
Pvap | 202.63 | kPa | 380.72 | Calculated Property |
Pvap | [9.03e-05; 4391.33] | kPa | [169.67; 560.40] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.66975e+01 | |||
Coefficient B | -6.84280e+03 | |||
Coefficient C | -1.08968e+01 | |||
Coefficient D | 9.11435e-06 | |||
Temperature range, min. | 169.67 | |||
Temperature range, max. | 560.40 | |||
Pvap | 9.03e-05 | kPa | 169.67 | Calculated Property |
Pvap | 0.03 | kPa | 213.08 | Calculated Property |
Pvap | 1.19 | kPa | 256.50 | Calculated Property |
Pvap | 12.83 | kPa | 299.91 | Calculated Property |
Pvap | 67.91 | kPa | 343.33 | Calculated Property |
Pvap | 232.04 | kPa | 386.74 | Calculated Property |
Pvap | 599.80 | kPa | 430.16 | Calculated Property |
Pvap | 1293.07 | kPa | 473.57 | Calculated Property |
Pvap | 2475.87 | kPa | 516.99 | Calculated Property |
Pvap | 4391.33 | kPa | 560.40 | Calculated Property |
Find more compounds similar to Cyclohexene.
Find more mixtures with Cyclohexene.
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.