Property | Value | Unit | Source |
---|---|---|---|

ω | 0.1640 | KDB | |

μ | 0.90 | debye | KDB |

Δ_{f}G° |
210.40 | kJ/mol | KDB |

Δ_{c,gross}H |
3226.62 | kJ/mol | KDB |

Δ_{c,net}H |
3050.554 | kJ/mol | KDB |

Δ_{f}H°_{gas} |
[144.30; 144.40] | kJ/mol | |

Δ_{f}H°_{gas} |
144.40 | kJ/mol | KDB |

Δ_{f}H°_{gas} |
144.30 ± 2.10 | kJ/mol | NIST |

Δ_{fus}H° |
11.68 | kJ/mol | Joback Calculated Property |

Δ_{vap}H° |
28.40 | kJ/mol | NIST |

IE | [10.05; 10.10] | eV | |

IE | 10.10 ± 0.01 | eV | NIST |

IE | 10.05 | eV | NIST |

IE | 10.10 ± 0.02 | eV | NIST |

IE | 10.10 ± 0.01 | eV | NIST |

log_{10}WS |
[-1.64; -1.64] | ||

log_{10}WS |
-1.64 | Aq. Sol... | |

log_{10}WS |
-1.64 | Estimat... | |

logP_{oct/wat} |
1.420 | Crippen Calculated Property | |

McVol | 72.710 | ml/mol | McGowan Calculated Property |

P_{c} |
4050.00 | kPa | KDB |

I_{np} |
[484.00; 517.00] | ||

I_{np} |
484.40 | NIST | |

I_{np} |
484.80 | NIST | |

I_{np} |
484.00 | NIST | |

I_{np} |
Outlier 517.00 | NIST | |

I_{np} |
510.00 | NIST | |

I_{np} |
484.50 | NIST | |

I_{np} |
484.00 | NIST | |

I_{np} |
484.00 | NIST | |

I_{np} |
484.00 | NIST | |

I_{np} |
484.00 | NIST | |

I_{np} |
509.00 | NIST | |

I_{np} |
484.00 | NIST | |

I_{np} |
484.00 | NIST | |

I_{np} |
484.40 | NIST | |

I_{np} |
484.50 | NIST | |

I_{np} |
484.00 | NIST | |

I_{np} |
509.00 | NIST | |

T_{boil} |
[312.15; 315.15] | K | |

T_{boil} |
313.33 | K | KDB |

T_{boil} |
313.00 | K | NIST |

T_{boil} |
313.40 | K | NIST |

T_{boil} |
312.80 ± 2.00 | K | NIST |

T_{boil} |
313.38 ± 0.20 | K | NIST |

T_{boil} |
313.33 ± 0.20 | K | NIST |

T_{boil} |
312.20 ± 1.00 | K | NIST |

T_{boil} |
312.85 ± 1.00 | K | NIST |

T_{boil} |
312.65 ± 2.00 | K | NIST |

T_{boil} |
313.35 ± 0.40 | K | NIST |

T_{boil} |
313.40 ± 0.20 | K | NIST |

T_{boil} |
Outlier 315.15 ± 2.00 | K | NIST |

T_{boil} |
313.35 ± 0.30 | K | NIST |

T_{boil} |
312.65 ± 1.50 | K | NIST |

T_{boil} |
312.45 ± 0.50 | K | NIST |

T_{boil} |
313.15 ± 1.00 | K | NIST |

T_{boil} |
312.85 ± 0.60 | K | NIST |

T_{boil} |
312.15 ± 1.00 | K | NIST |

T_{boil} |
313.15 ± 0.70 | K | NIST |

T_{boil} |
312.90 ± 0.80 | K | NIST |

T_{boil} |
312.95 ± 1.00 | K | NIST |

T_{boil} |
313.15 ± 1.50 | K | NIST |

T_{boil} |
313.15 ± 1.00 | K | NIST |

T_{c} |
493.50 | K | KDB |

T_{fus} |
[166.65; 183.00] | K | |

T_{fus} |
183.00 | K | KDB |

T_{fus} |
172.48 | K | Aq. Sol... |

T_{fus} |
166.65 ± 0.30 | K | NIST |

T_{fus} |
167.08 ± 0.20 | K | NIST |

V_{c} |
0.278 | m^{3}/kmol |
KDB |

Z_{c} |
0.2743950 | KDB |

Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|

C_{p,gas} |
[108.43; 147.68] | J/mol×K | [303.92; 478.30] | |

C_{p,gas} |
108.43 | J/mol×K | 303.92 | Joback Calculated Property |

C_{p,gas} |
115.69 | J/mol×K | 332.98 | Joback Calculated Property |

C_{p,gas} |
122.65 | J/mol×K | 362.05 | Joback Calculated Property |

C_{p,gas} |
129.31 | J/mol×K | 391.11 | Joback Calculated Property |

C_{p,gas} |
135.70 | J/mol×K | 420.17 | Joback Calculated Property |

C_{p,gas} |
141.82 | J/mol×K | 449.24 | Joback Calculated Property |

C_{p,gas} |
147.68 | J/mol×K | 478.30 | Joback Calculated Property |

Δ_{vap}H |
[27.74; 31.80] | kJ/mol | [272.00; 313.40] | |

Δ_{vap}H |
31.80 | kJ/mol | 272.00 | NIST |

Δ_{vap}H |
27.74 | kJ/mol | 313.40 | KDB |

n_{0} |
1.38260 | 298.15 | KDB | |

ρ_{l} |
690.00 | kg/m^{3} |
293.00 | KDB |

γ | 0.02 | N/m | 298.20 | KDB |

Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|

P_{vap} |
[1.33; 202.67] | kPa | [233.02; 333.62] | The Yaw... |

Equation | ln(Pvp) = A + B/(T + C) | |||

Coefficient A | 1.39994e+01 | |||

Coefficient B | -2.38534e+03 | |||

Coefficient C | -5.90590e+01 | |||

Temperature range, min. | 233.02 | |||

Temperature range, max. | 333.62 | |||

P_{vap} |
1.33 | kPa | 233.02 | Calculated Property |

P_{vap} |
3.05 | kPa | 244.20 | Calculated Property |

P_{vap} |
6.35 | kPa | 255.38 | Calculated Property |

P_{vap} |
12.23 | kPa | 266.55 | Calculated Property |

P_{vap} |
22.00 | kPa | 277.73 | Calculated Property |

P_{vap} |
37.40 | kPa | 288.91 | Calculated Property |

P_{vap} |
60.51 | kPa | 300.09 | Calculated Property |

P_{vap} |
93.83 | kPa | 311.26 | Calculated Property |

P_{vap} |
140.17 | kPa | 322.44 | Calculated Property |

P_{vap} |
202.67 | kPa | 333.62 | Calculated Property |

P_{vap} |
[2.47e-03; 4064.44] | kPa | [167.45; 481.20] | KDB Vap... |

Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||

Coefficient A | 5.86812e+01 | |||

Coefficient B | -5.16272e+03 | |||

Coefficient C | -6.64398e+00 | |||

Coefficient D | 6.01492e-06 | |||

Temperature range, min. | 167.45 | |||

Temperature range, max. | 481.20 | |||

P_{vap} |
2.47e-03 | kPa | 167.45 | Calculated Property |

P_{vap} |
0.15 | kPa | 202.31 | Calculated Property |

P_{vap} |
2.50 | kPa | 237.17 | Calculated Property |

P_{vap} |
18.22 | kPa | 272.03 | Calculated Property |

P_{vap} |
79.72 | kPa | 306.89 | Calculated Property |

P_{vap} |
248.55 | kPa | 341.76 | Calculated Property |

P_{vap} |
613.54 | kPa | 376.62 | Calculated Property |

P_{vap} |
1283.96 | kPa | 411.48 | Calculated Property |

P_{vap} |
2385.65 | kPa | 446.34 | Calculated Property |

P_{vap} |
4064.44 | kPa | 481.20 | Calculated Property |

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