Property | Value | Unit | Source |
---|---|---|---|
PAff | 834.80 | kJ/mol | NIST |
BasG | 805.00 | kJ/mol | NIST |
ΔcH°liquid | [-2665.20; -2664.30] | kJ/mol |
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ΔcH°liquid | -2664.30 | kJ/mol | NIST |
ΔcH°liquid | -2665.20 ± 0.84 | kJ/mol | NIST |
ΔfG° | 70.60 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [59.90; 61.10] | kJ/mol |
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ΔfH°gas | 59.90 | kJ/mol | NIST |
ΔfH°gas | 61.10 ± 1.30 | kJ/mol | NIST |
ΔfH°liquid | [24.00; 25.20] | kJ/mol |
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ΔfH°liquid | 24.00 ± 2.00 | kJ/mol | NIST |
ΔfH°liquid | 25.20 ± 1.20 | kJ/mol | NIST |
ΔfusH° | 2.15 | kJ/mol | Joback Calculated Property |
ΔvapH° | [35.80; 36.01] | kJ/mol |
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ΔvapH° | 36.01 | kJ/mol | NIST |
ΔvapH° | 35.80 | kJ/mol | NIST |
ΔvapH° | 35.90 | kJ/mol | NIST |
ΔvapH° | 35.90 ± 0.20 | kJ/mol | NIST |
IE | [8.50; 8.65] | eV |
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IE | 8.61 | eV | NIST |
IE | 8.61 | eV | NIST |
IE | 8.50 | eV | NIST |
IE | 8.65 ± 0.01 | eV | NIST |
IE | 8.65 | eV | NIST |
log10WS | -0.86 | Crippen Calculated Property | |
logPoct/wat | 1.123 | Crippen Calculated Property | |
McVol | 58.620 | ml/mol | McGowan Calculated Property |
Pc | 5704.58 | kPa | Joback Calculated Property |
Inp | [743.00; 744.00] |
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|
Inp | 744.00 | NIST | |
Inp | 743.00 | NIST | |
Inp | 744.00 | NIST | |
Inp | 743.00 | NIST | |
S°liquid | 184.93 | J/mol×K | NIST |
Tboil | [367.00; 368.10] | K |
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Tboil | 367.90 | K | NIST |
Tboil | 368.10 | K | NIST |
Tboil | 367.00 ± 3.00 | K | NIST |
Tc | 540.19 | K | Joback Calculated Property |
Tfus | 225.68 | K | Joback Calculated Property |
Ttriple | 199.91 ± 0.01 | K | NIST |
Vc | 0.200 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [79.04; 122.73] | J/mol×K | [331.55; 540.19] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 80 90 100 110 120 350 400 450 500 | ||||
Cp,gas | 79.04 | J/mol×K | 331.55 | Joback Calculated Property |
Cp,gas | 87.68 | J/mol×K | 366.32 | Joback Calculated Property |
Cp,gas | 95.74 | J/mol×K | 401.10 | Joback Calculated Property |
Cp,gas | 103.24 | J/mol×K | 435.87 | Joback Calculated Property |
Cp,gas | 110.22 | J/mol×K | 470.64 | Joback Calculated Property |
Cp,gas | 116.70 | J/mol×K | 505.42 | Joback Calculated Property |
Cp,gas | 122.73 | J/mol×K | 540.19 | Joback Calculated Property |
Cp,liquid | 112.59 | J/mol×K | 294.37 | NIST |
ΔfusH | [0.67; 8.24] | kJ/mol | [176.70; 199.90] | ![]() |
ΔfusH | 0.67 | kJ/mol | 176.70 | NIST |
ΔfusH | 8.24 | kJ/mol | 199.90 | NIST |
ΔfusH | 8.24 | kJ/mol | 199.90 | NIST |
ΔvapH | [32.32; 36.50] | kJ/mol | [334.00; 368.10] | ![]() |
ΔvapH | 36.50 | kJ/mol | 334.00 | NIST |
ΔvapH | 34.60 | kJ/mol | 362.50 | NIST |
ΔvapH | 32.32 | kJ/mol | 368.10 | NIST |
ΔfusS | [3.77; 41.25] | J/mol×K | [176.70; 199.90] | ![]() |
ΔfusS | 3.77 | J/mol×K | 176.70 | NIST |
ΔfusS | 41.25 | J/mol×K | 199.90 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 204.20] | kPa | [268.65; 392.95] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.43057e+01 | |||
Coefficient B | -3.11206e+03 | |||
Coefficient C | -4.66510e+01 | |||
Temperature range, min. | 268.65 | |||
Temperature range, max. | 392.95 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
Pvap | 1.33 | kPa | 268.65 | Calculated Property |
Pvap | 3.03 | kPa | 282.46 | Calculated Property |
Pvap | 6.29 | kPa | 296.27 | Calculated Property |
Pvap | 12.09 | kPa | 310.08 | Calculated Property |
Pvap | 21.77 | kPa | 323.89 | Calculated Property |
Pvap | 37.09 | kPa | 337.71 | Calculated Property |
Pvap | 60.21 | kPa | 351.52 | Calculated Property |
Pvap | 93.71 | kPa | 365.33 | Calculated Property |
Pvap | 140.58 | kPa | 379.14 | Calculated Property |
Pvap | 204.20 | kPa | 392.95 | Calculated Property |
Pvap | [1.33; 6130.28] | kPa | [268.15; 603.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 7.13704e+01 | |||
Coefficient B | -6.54879e+03 | |||
Coefficient C | -8.42079e+00 | |||
Coefficient D | 5.83091e-06 | |||
Temperature range, min. | 268.15 | |||
Temperature range, max. | 603.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 300 400 500 600 | ||||
Pvap | 1.33 | kPa | 268.15 | Calculated Property |
Pvap | 9.86 | kPa | 305.36 | Calculated Property |
Pvap | 44.25 | kPa | 342.56 | Calculated Property |
Pvap | 141.36 | kPa | 379.77 | Calculated Property |
Pvap | 356.31 | kPa | 416.97 | Calculated Property |
Pvap | 758.73 | kPa | 454.18 | Calculated Property |
Pvap | 1430.11 | kPa | 491.38 | Calculated Property |
Pvap | 2465.73 | kPa | 528.59 | Calculated Property |
Pvap | 3982.11 | kPa | 565.79 | Calculated Property |
Pvap | 6130.28 | kPa | 603.00 | Calculated Property |
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