| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.2430 | KDB | |
| AP | 316.950 | K | KDB |
| ΔcH°liquid | -5222.60 ± 1.50 | kJ/mol | NIST |
| μ | 0.00 | debye | KDB |
| ΔfG° | 39.27 | kJ/mol | KDB |
| Δc,grossH | 5222.59 | kJ/mol | KDB |
| Δc,netH | 4870.511 | kJ/mol | KDB |
| ΔfH°gas | [-172.60; -171.80] | kJ/mol |
|
| ΔfH°gas | -171.90 | kJ/mol | KDB |
| ΔfH°gas | -172.60 | kJ/mol | NIST |
| ΔfH°gas | -171.80 ± 1.50 | kJ/mol | NIST |
| ΔfH°liquid | [-213.00; -212.20] | kJ/mol |
|
| ΔfH°liquid | -213.00 | kJ/mol | NIST |
| ΔfH°liquid | -212.20 ± 1.50 | kJ/mol | NIST |
| ΔfusH° | 8.31 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 38.76 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [9.54; 9.67] | eV |
|
| IE | 9.54 | eV | NIST |
| IE | 9.67 ± 0.02 | eV | NIST |
| log10WS | [-4.25; -4.25] |
|
|
| log10WS | -4.25 | Aq. Solubility Prediction | |
| log10WS | -4.25 | Estimated Solubility | |
| logPoct/wat | 2.977 | Crippen Calculated Property | |
| McVol | 112.720 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [3000.00; 3250.00] | kPa |
|
| Pc | 3000.00 | kPa | KDB |
| Pc | 3250.00 | kPa | Critical Point Measurements for Five n-Alkylcyclohexanes (C6 to C10) by the Pulse-Heating Method |
| Inp | [818.00; 867.90] |
|
|
| Inp | 846.00 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 842.20 | NIST | |
| Inp | Outlier 859.70 | NIST | |
| Inp | Outlier 867.90 | NIST | |
| Inp | 828.00 | NIST | |
| Inp | 833.60 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | 834.30 | NIST | |
| Inp | 842.80 | NIST | |
| Inp | 831.30 | NIST | |
| Inp | 831.70 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 838.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 842.00 | NIST | |
| Inp | 842.00 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 840.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 840.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 836.00 | NIST | |
| Inp | 838.00 | NIST | |
| Inp | 841.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 834.30 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | Outlier 856.00 | NIST | |
| Inp | 842.00 | NIST | |
| Inp | 825.00 | NIST | |
| Inp | 828.00 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 842.00 | NIST | |
| Inp | 835.92 | NIST | |
| Inp | 824.00 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | Outlier 854.00 | NIST | |
| Inp | 840.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 841.00 | NIST | |
| Inp | 832.20 | NIST | |
| Inp | 829.10 | NIST | |
| Inp | 828.40 | NIST | |
| Inp | 826.90 | NIST | |
| Inp | 829.10 | NIST | |
| Inp | 830.90 | NIST | |
| Inp | 838.10 | NIST | |
| Inp | 830.10 | NIST | |
| Inp | Outlier 818.00 | NIST | |
| Inp | 826.90 | NIST | |
| Inp | 829.10 | NIST | |
| Inp | 830.90 | NIST | |
| Inp | 829.10 | NIST | |
| Inp | 828.40 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 821.60 | NIST | |
| Inp | 824.96 | NIST | |
| Inp | 827.15 | NIST | |
| Inp | 827.11 | NIST | |
| Inp | 830.63 | NIST | |
| Inp | 832.99 | NIST | |
| Inp | 841.00 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 828.00 | NIST | |
| Inp | 833.00 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | 833.00 | NIST | |
| Inp | 836.00 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 831.70 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 825.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 837.90 | NIST | |
| Inp | 841.40 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 846.20 | NIST | |
| Inp | 825.00 | NIST | |
| Inp | 824.00 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 831.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 840.00 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 840.00 | NIST | |
| Inp | 834.00 | NIST | |
| I | [885.00; 925.20] |
|
|
| I | 920.00 | NIST | |
| I | 915.00 | NIST | |
| I | 920.00 | NIST | |
| I | 925.20 | NIST | |
| I | 905.50 | NIST | |
| I | 910.10 | NIST | |
| I | 920.00 | NIST | |
| I | Outlier 885.00 | NIST | |
| I | 920.00 | NIST | |
| I | 910.10 | NIST | |
| S°gas | 382.67 | J/mol×K | NIST |
| S°liquid | [280.91; 281.60] | J/mol×K |
|
| S°liquid | 280.91 | J/mol×K | NIST |
| S°liquid | 281.60 | J/mol×K | NIST |
| Tboil | 404.90 | K | KDB |
| Tc | [606.90; 609.00] | K |
|
| Tc | 609.00 | K | KDB |
| Tc | 606.90 | K | Gas-Liquid Critical Temperatures of Some Alkenes, Amines, and Cyclic Hydrocarbons |
| Tc | 609.00 | K | NIST |
| Tfus | [161.80; 162.00] | K |
|
| Tfus | 161.80 | K | KDB |
| Tfus | 162.00 | K | Aq. Solubility Prediction |
| Ttriple | [161.40; 161.84] | K |
|
| Ttriple | 161.84 ± 0.05 | K | NIST |
| Ttriple | 161.40 ± 0.20 | K | NIST |
| Vc | 0.450 | m3/kmol | KDB |
| Zc | 0.2666120 | KDB |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [291.27; 433.70] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.40223e+01 | |||
| Coefficient B | -3.39182e+03 | |||
| Coefficient C | -4.43220e+01 | |||
| Temperature range, min. | 291.27 | |||
| Temperature range, max. | 433.70 | |||
| Pvap | 1.33 | kPa | 291.27 | Calculated Property |
| Pvap | 3.05 | kPa | 307.10 | Calculated Property |
| Pvap | 6.35 | kPa | 322.92 | Calculated Property |
| Pvap | 12.21 | kPa | 338.75 | Calculated Property |
| Pvap | 21.97 | kPa | 354.57 | Calculated Property |
| Pvap | 37.35 | kPa | 370.40 | Calculated Property |
| Pvap | 60.45 | kPa | 386.22 | Calculated Property |
| Pvap | 93.76 | kPa | 402.05 | Calculated Property |
| Pvap | 140.11 | kPa | 417.87 | Calculated Property |
| Pvap | 202.64 | kPa | 433.70 | Calculated Property |
| Pvap | [3.59e-07; 3033.23] | kPa | [161.84; 609.15] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.23704e+01 | |||
| Coefficient B | -7.17302e+03 | |||
| Coefficient C | -8.45462e+00 | |||
| Coefficient D | 4.40351e-06 | |||
| Temperature range, min. | 161.84 | |||
| Temperature range, max. | 609.15 | |||
| Pvap | 3.59e-07 | kPa | 161.84 | Calculated Property |
| Pvap | 1.35e-03 | kPa | 211.54 | Calculated Property |
| Pvap | 0.16 | kPa | 261.24 | Calculated Property |
| Pvap | 3.32 | kPa | 310.94 | Calculated Property |
| Pvap | 26.41 | kPa | 360.64 | Calculated Property |
| Pvap | 116.75 | kPa | 410.35 | Calculated Property |
| Pvap | 355.10 | kPa | 460.05 | Calculated Property |
| Pvap | 843.49 | kPa | 509.75 | Calculated Property |
| Pvap | 1694.41 | kPa | 559.45 | Calculated Property |
| Pvap | 3033.23 | kPa | 609.15 | Calculated Property |
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