Property | Value | Unit | Source |
---|---|---|---|
ω | 0.1380 | KDB | |
PAff | 691.70 | kJ/mol | NIST |
BasG | 665.50 | kJ/mol | NIST |
ΔcH°liquid | -808.60 ± 0.30 | kJ/mol | NIST |
μ | 1.60 | debye | KDB |
EA | [0.11; 0.30] | eV | |
EA | 0.11 ± 0.02 | eV | NIST |
EA | 0.30 ± 0.20 | eV | NIST |
ΔfG° | 15.66 | kJ/mol | KDB |
ΔfH°gas | [13.98; 16.00] | kJ/mol | |
ΔfH°gas | 13.98 | kJ/mol | KDB |
ΔfH°gas | 14.30 ± 1.40 | kJ/mol | NIST |
ΔfH°gas | 14.60 ± 1.00 | kJ/mol | NIST |
ΔfH°gas | 16.00 ± 1.00 | kJ/mol | NIST |
ΔfH°liquid | [-13.60; -12.00] | kJ/mol | |
ΔfH°liquid | -13.60 ± 0.50 | kJ/mol | NIST |
ΔfH°liquid | -12.00 ± 1.00 | kJ/mol | NIST |
ΔfusH° | 2.75 | kJ/mol | Joback Calculated Property |
ΔvapH° | 27.19 | kJ/mol | Joback Calculated Property |
IE | [9.48; 10.86] | eV | |
IE | 9.54 ± 0.02 | eV | NIST |
IE | 9.54 ± 0.05 | eV | NIST |
IE | 9.54 | eV | NIST |
IE | Outlier 10.86 | eV | NIST |
IE | 9.54 | eV | NIST |
IE | 9.54 | eV | NIST |
IE | 9.54 | eV | NIST |
IE | 9.53 ± 0.01 | eV | NIST |
IE | 9.54 | eV | NIST |
IE | 9.54 | eV | NIST |
IE | 9.48 ± 0.03 | eV | NIST |
IE | 9.54 | eV | NIST |
IE | 9.52 | eV | NIST |
IE | 10.14 | eV | NIST |
IE | 9.50 | eV | NIST |
IE | 9.54 | eV | NIST |
IE | 9.53 ± 0.01 | eV | NIST |
IE | 9.54 ± 0.00 | eV | NIST |
IE | 9.53 | eV | NIST |
IE | 9.90 | eV | NIST |
IE | 9.51 | eV | NIST |
log10WS | [-1.00; -1.00] | ||
log10WS | -1.00 | Aq. Sol... | |
log10WS | -1.00 | Estimat... | |
logPoct/wat | 1.051 | Crippen Calculated Property | |
McVol | 50.770 | ml/mol | McGowan Calculated Property |
Pc | 6590.00 | kPa | KDB |
Inp | [502.00; 554.00] | ||
Inp | 523.00 | NIST | |
Inp | 528.00 | NIST | |
Inp | 518.00 | NIST | |
Inp | 528.60 | NIST | |
Inp | 502.00 | NIST | |
Inp | 508.00 | NIST | |
Inp | 513.00 | NIST | |
Inp | 518.00 | NIST | |
Inp | 524.00 | NIST | |
Inp | 516.00 | NIST | |
Inp | Outlier 554.00 | NIST | |
Inp | 506.00 | NIST | |
Inp | 530.00 | NIST | |
Inp | 523.00 | NIST | |
Inp | 515.00 | NIST | |
Inp | 509.00 | NIST | |
Inp | 509.00 | NIST | |
Inp | 515.00 | NIST | |
Inp | 515.00 | NIST | |
I | [802.99; 833.00] | ||
I | 804.33 | NIST | |
I | 802.99 | NIST | |
I | 818.02 | NIST | |
I | 833.00 | NIST | |
I | 806.00 | NIST | |
I | 806.00 | NIST | |
Tboil | 315.70 | K | KDB |
Tc | 528.00 | K | KDB |
Tfus | [206.70; 208.10] | K | |
Tfus | 206.70 | K | KDB |
Tfus | 207.30 | K | Aq. Sol... |
Tfus | 206.70 ± 0.50 | K | NIST |
Tfus | 208.10 ± 0.40 | K | NIST |
Vc | 0.179 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [47.27; 60.89] | J/mol×K | [315.42; 522.45] | |
T(K) Ideal gas heat capacity (J/mol×K) 50 55 60 350 400 450 500 | ||||
Cp,gas | 47.27 | J/mol×K | 315.42 | Joback Calculated Property |
Cp,gas | 49.92 | J/mol×K | 349.93 | Joback Calculated Property |
Cp,gas | 52.41 | J/mol×K | 384.43 | Joback Calculated Property |
Cp,gas | 54.74 | J/mol×K | 418.94 | Joback Calculated Property |
Cp,gas | 56.92 | J/mol×K | 453.44 | Joback Calculated Property |
Cp,gas | 58.97 | J/mol×K | 487.95 | Joback Calculated Property |
Cp,gas | 60.89 | J/mol×K | 522.45 | Joback Calculated Property |
Cp,liquid | [82.00; 148.10] | J/mol×K | [298.00; 300.00] | |
T(K) Liquid phase heat capacity (J/mol×K) 80 90 100 110 120 130 140 150 298 299 300 | ||||
Cp,liquid | 148.10 | J/mol×K | 298.00 | NIST |
Cp,liquid | 82.75 | J/mol×K | 298.15 | NIST |
Cp,liquid | 82.00 | J/mol×K | 298.15 | NIST |
Cp,liquid | 82.76 | J/mol×K | 298.20 | NIST |
Cp,liquid | 82.68 | J/mol×K | 300.00 | NIST |
η | [0.0004180; 0.0044613] | Pa×s | [159.09; 315.42] | |
T(K) Dynamic viscosity (Pa×s) 1.00e-3 2.00e-3 3.00e-3 4.00e-3 200 250 300 | ||||
η | 0.0044613 | Pa×s | 159.09 | Joback Calculated Property |
η | 0.0022777 | Pa×s | 185.15 | Joback Calculated Property |
η | 0.0013726 | Pa×s | 211.20 | Joback Calculated Property |
η | 0.0009245 | Pa×s | 237.25 | Joback Calculated Property |
η | 0.0006734 | Pa×s | 263.31 | Joback Calculated Property |
η | 0.0005193 | Pa×s | 289.37 | Joback Calculated Property |
η | 0.0004180 | Pa×s | 315.42 | Joback Calculated Property |
ΔfusH | [9.10; 9.12] | kJ/mol | [206.80; 206.80] | |
ΔfusH | 9.12 | kJ/mol | 206.80 | NIST |
ΔfusH | 9.10 | kJ/mol | 206.80 | NIST |
ΔsubH | 40.20 ± 0.40 | kJ/mol | 201.50 | NIST |
ΔvapH | [26.50; 31.10] | kJ/mol | [217.50; 408.50] | |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 27 28 29 30 31 250 300 350 400 | ||||
ΔvapH | 31.10 | kJ/mol | 217.50 | NIST |
ΔvapH | 30.40 | kJ/mol | 266.50 | NIST |
ΔvapH | 30.40 | kJ/mol | 282.50 | NIST |
ΔvapH | 29.20 | kJ/mol | 286.50 | NIST |
ΔvapH | 28.20 | kJ/mol | 290.00 | NIST |
ΔvapH | 27.20 | kJ/mol | 315.60 | KDB |
ΔvapH | 28.41 | kJ/mol | 315.80 | NIST |
ΔvapH | 26.50 | kJ/mol | 408.50 | NIST |
Pvap | [30.00; 129.00] | kPa | [283.15; 323.15] | |
T(K) Vapor pressure (kPa) 40 60 80 100 120 290 300 310 320 | ||||
Pvap | 30.00 | kPa | 283.15 | Isother... |
Pvap | 47.50 | kPa | 293.15 | Isother... |
Pvap | 69.90 | kPa | 303.15 | Isother... |
Pvap | 95.00 | kPa | 313.15 | Isother... |
Pvap | 129.00 | kPa | 323.15 | Isother... |
ρl | 2279.00 | kg/m3 | 293.00 | KDB |
γ | 0.03 | N/m | 293.20 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [0.26; 202.68] | kPa | [206.70; 337.18] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.48574e+01 | |||
Coefficient B | -3.02828e+03 | |||
Coefficient C | -1.99430e+01 | |||
Temperature range, min. | 206.70 | |||
Temperature range, max. | 337.18 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 | ||||
Pvap | 0.26 | kPa | 206.70 | Calculated Property |
Pvap | 0.83 | kPa | 221.20 | Calculated Property |
Pvap | 2.27 | kPa | 235.70 | Calculated Property |
Pvap | 5.50 | kPa | 250.19 | Calculated Property |
Pvap | 11.99 | kPa | 264.69 | Calculated Property |
Pvap | 23.96 | kPa | 279.19 | Calculated Property |
Pvap | 44.48 | kPa | 293.69 | Calculated Property |
Pvap | 77.58 | kPa | 308.18 | Calculated Property |
Pvap | 128.32 | kPa | 322.68 | Calculated Property |
Pvap | 202.68 | kPa | 337.18 | Calculated Property |
Pvap | [0.25; 6876.91] | kPa | [206.70; 528.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 5.75767e+01 | |||
Coefficient B | -5.02586e+03 | |||
Coefficient C | -6.54993e+00 | |||
Coefficient D | 6.60013e-06 | |||
Temperature range, min. | 206.70 | |||
Temperature range, max. | 528.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 7000 200 300 400 500 | ||||
Pvap | 0.25 | kPa | 206.70 | Calculated Property |
Pvap | 3.55 | kPa | 242.40 | Calculated Property |
Pvap | 23.39 | kPa | 278.10 | Calculated Property |
Pvap | 95.26 | kPa | 313.80 | Calculated Property |
Pvap | 282.34 | kPa | 349.50 | Calculated Property |
Pvap | 673.11 | kPa | 385.20 | Calculated Property |
Pvap | 1377.43 | kPa | 420.90 | Calculated Property |
Pvap | 2527.78 | kPa | 456.60 | Calculated Property |
Pvap | 4288.96 | kPa | 492.30 | Calculated Property |
Pvap | 6876.91 | kPa | 528.00 | Calculated Property |
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