Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -141.47 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -198.36 | kJ/mol | Joback Calculated Property |
ΔfusH° | 9.07 | kJ/mol | Joback Calculated Property |
ΔvapH° | 43.46 | kJ/mol | Joback Calculated Property |
IE | [9.10; 9.65] | eV |
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IE | 9.10 | eV | NIST |
IE | 9.65 | eV | NIST |
log10WS | 4.71e-03 | Crippen Calculated Property | |
logPoct/wat | -0.092 | Crippen Calculated Property | |
McVol | 61.260 | ml/mol | McGowan Calculated Property |
Pc | 6359.24 | kPa | Joback Calculated Property |
Inp | [717.00; 725.00] |
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|
Inp | 725.00 | NIST | |
Inp | 722.00 | NIST | |
Inp | 717.00 | NIST | |
Inp | 717.00 | NIST | |
Inp | 724.00 | NIST | |
Inp | 724.00 | NIST | |
I | [1498.00; 1538.00] |
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|
I | 1498.00 | NIST | |
I | 1498.00 | NIST | |
I | Outlier 1538.00 | NIST | |
I | 1501.00 | NIST | |
I | 1501.00 | NIST | |
I | 1498.00 | NIST | |
Tboil | [430.05; 430.20] | K |
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Tboil | 430.20 | K | NIST |
Tboil | 430.05 | K | NIST |
Tc | 587.02 | K | Joback Calculated Property |
Tfus | 209.58 | K | Joback Calculated Property |
Vc | 0.221 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [103.07; 129.18] | J/mol×K | [400.20; 587.02] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 105 110 115 120 125 130 400 450 500 550 | ||||
Cp,gas | 103.07 | J/mol×K | 400.20 | Joback Calculated Property |
Cp,gas | 107.90 | J/mol×K | 431.34 | Joback Calculated Property |
Cp,gas | 112.53 | J/mol×K | 462.47 | Joback Calculated Property |
Cp,gas | 116.96 | J/mol×K | 493.61 | Joback Calculated Property |
Cp,gas | 121.22 | J/mol×K | 524.75 | Joback Calculated Property |
Cp,gas | 125.29 | J/mol×K | 555.88 | Joback Calculated Property |
Cp,gas | 129.18 | J/mol×K | 587.02 | Joback Calculated Property |
ΔvapH | 54.10 | kJ/mol | 366.50 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 430.70 | K | 98.90 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 207.58] | kPa | [326.59; 456.19] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.51420e+01 | |||
Coefficient B | -3.73991e+03 | |||
Coefficient C | -7.48200e+01 | |||
Temperature range, min. | 326.59 | |||
Temperature range, max. | 456.19 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
Pvap | 1.33 | kPa | 326.59 | Calculated Property |
Pvap | 2.98 | kPa | 340.99 | Calculated Property |
Pvap | 6.12 | kPa | 355.39 | Calculated Property |
Pvap | 11.74 | kPa | 369.79 | Calculated Property |
Pvap | 21.18 | kPa | 384.19 | Calculated Property |
Pvap | 36.27 | kPa | 398.59 | Calculated Property |
Pvap | 59.31 | kPa | 412.99 | Calculated Property |
Pvap | 93.17 | kPa | 427.39 | Calculated Property |
Pvap | 141.27 | kPa | 441.79 | Calculated Property |
Pvap | 207.58 | kPa | 456.19 | Calculated Property |
Pvap | [0.14; 131.69] | kPa | [293.15; 440.15] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.59021e+02 | |||
Coefficient B | -1.21287e+04 | |||
Coefficient C | -2.12966e+01 | |||
Coefficient D | 1.57448e-05 | |||
Temperature range, min. | 293.15 | |||
Temperature range, max. | 440.15 | |||
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 120 140 300 350 400 | ||||
Pvap | 0.14 | kPa | 293.15 | Calculated Property |
Pvap | 0.45 | kPa | 309.48 | Calculated Property |
Pvap | 1.27 | kPa | 325.82 | Calculated Property |
Pvap | 3.14 | kPa | 342.15 | Calculated Property |
Pvap | 7.01 | kPa | 358.48 | Calculated Property |
Pvap | 14.31 | kPa | 374.82 | Calculated Property |
Pvap | 27.13 | kPa | 391.15 | Calculated Property |
Pvap | 48.31 | kPa | 407.48 | Calculated Property |
Pvap | 81.58 | kPa | 423.82 | Calculated Property |
Pvap | 131.69 | kPa | 440.15 | Calculated Property |
Find more compounds similar to Ethanol, 2-mercapto-.
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