Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -641.60 ± 1.90 | kJ/mol | NIST |
ΔfG° | -648.58 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -726.80 ± 4.30 | kJ/mol | NIST |
ΔfH°liquid | -755.00 ± 4.30 | kJ/mol | NIST |
ΔfusH° | 7.94 | kJ/mol | Joback Calculated Property |
ΔvapH° | [28.20; 28.70] | kJ/mol |
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ΔvapH° | 28.61 | kJ/mol | NIST |
ΔvapH° | 28.20 ± 0.40 | kJ/mol | NIST |
ΔvapH° | 28.40 ± 0.10 | kJ/mol | NIST |
ΔvapH° | 28.20 ± 0.40 | kJ/mol | NIST |
ΔvapH° | 28.70 | kJ/mol | NIST |
IE | [11.99; 12.05] | eV |
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IE | 11.99 ± 0.02 | eV | NIST |
IE | 12.05 | eV | NIST |
log10WS | [-3.04; -3.04] |
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|
log10WS | -3.04 | Aq. Sol... | |
log10WS | -3.04 | Estimat... | |
logPoct/wat | 2.919 | Crippen Calculated Property | |
McVol | 81.070 | ml/mol | McGowan Calculated Property |
Pc | [3379.00; 3420.00] | kPa |
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Pc | 3420.00 | kPa | KDB |
Pc | 3379.00 ± 5.00 | kPa | NIST |
Pc | 3410.82 ± 6.89 | kPa | NIST |
Pc | 3412.89 | kPa | NIST |
ρc | [569.62; 575.24] | kg/m3 |
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ρc | 569.62 ± 5.70 | kg/m3 | NIST |
ρc | 569.92 ± 9.61 | kg/m3 | NIST |
ρc | 575.24 ± 1.87 | kg/m3 | NIST |
Inp | [522.00; 555.00] |
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|
Inp | 528.00 | NIST | |
Inp | 540.00 | NIST | |
Inp | 524.00 | NIST | |
Inp | 532.00 | NIST | |
Inp | 526.00 | NIST | |
Inp | 522.00 | NIST | |
Inp | 522.00 | NIST | |
Inp | 527.00 | NIST | |
Inp | Outlier 555.00 | NIST | |
Inp | 530.00 | NIST | |
Inp | 530.00 | NIST | |
I | [660.00; 660.00] |
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|
I | 660.00 | NIST | |
I | 660.00 | NIST | |
S°liquid | 289.50 | J/mol×K | NIST |
Tboil | [320.42; 321.00] | K |
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Tboil | 320.80 | K | KDB |
Tboil | 321.00 | K | NIST |
Tboil | 320.42 ± 0.10 | K | NIST |
Tboil | 320.90 | K | NIST |
Tboil | 320.70 | K | NIST |
Tboil | 320.70 | K | NIST |
Tc | 487.30 | K | KDB |
Tfus | [238.00; 238.15] | K |
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Tfus | 238.00 | K | KDB |
Tfus | 238.15 | K | NIST |
Ttriple | [236.55; 237.93] | K |
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Ttriple | 236.55 ± 0.10 | K | NIST |
Ttriple | 237.93 ± 0.02 | K | NIST |
Ttriple | 236.92 ± 0.02 | K | NIST |
Vc | 0.325 | m3/kmol | KDB |
Zc | 0.2743320 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [126.81; 153.48] | J/mol×K | [348.80; 533.87] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 125 130 135 140 145 150 155 350 400 450 500 | ||||
Cp,gas | 126.81 | J/mol×K | 348.80 | Joback Calculated Property |
Cp,gas | 132.62 | J/mol×K | 379.64 | Joback Calculated Property |
Cp,gas | 137.83 | J/mol×K | 410.49 | Joback Calculated Property |
Cp,gas | 142.49 | J/mol×K | 441.33 | Joback Calculated Property |
Cp,gas | 146.63 | J/mol×K | 472.18 | Joback Calculated Property |
Cp,gas | 150.28 | J/mol×K | 503.02 | Joback Calculated Property |
Cp,gas | 153.48 | J/mol×K | 533.87 | Joback Calculated Property |
Cp,liquid | [172.50; 179.80] | J/mol×K | [298.15; 303.15] | ![]() |
T(K) Liquid phase heat capacity (J/mol×K) 172 174 176 178 180 300 302 | ||||
Cp,liquid | 172.90 | J/mol×K | 298.15 | NIST |
Cp,liquid | 172.80 | J/mol×K | 298.15 | NIST |
Cp,liquid | 179.80 | J/mol×K | 298.15 | NIST |
Cp,liquid | 177.00 | J/mol×K | 298.20 | NIST |
Cp,liquid | 177.00 | J/mol×K | 298.20 | NIST |
Cp,liquid | 172.50 | J/mol×K | 303.15 | NIST |
ΔfusH | [0.83; 2.47] | kJ/mol | [82.50; 273.93] | ![]() |
ΔfusH | 0.83 | kJ/mol | 82.50 | NIST |
ΔfusH | 2.47 | kJ/mol | 236.90 | NIST |
ΔfusH | 2.47 | kJ/mol | 236.90 | NIST |
ΔfusH | 2.33 | kJ/mol | 273.93 | NIST |
ΔsubH | 32.90 | kJ/mol | 219.00 | NIST |
ΔvapH | [26.60; 30.90] | kJ/mol | [295.50; 416.50] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 27 28 29 30 31 300 350 400 | ||||
ΔvapH | 28.20 | kJ/mol | 295.50 | NIST |
ΔvapH | 28.30 | kJ/mol | 296.00 | NIST |
ΔvapH | 30.90 | kJ/mol | 301.00 | NIST |
ΔvapH | 30.80 | kJ/mol | 302.00 | NIST |
ΔvapH | 28.80 | kJ/mol | 307.00 | NIST |
ΔvapH | 27.50 ± 0.10 | kJ/mol | 313.00 | NIST |
ΔvapH | 27.04 | kJ/mol | 320.70 | NIST |
ΔvapH | 26.60 ± 0.10 | kJ/mol | 328.00 | NIST |
ΔvapH | 26.90 | kJ/mol | 416.50 | NIST |
ΔfusS | [8.49; 10.42] | J/mol×K | [82.50; 273.93] | ![]() |
ΔfusS | 10.08 | J/mol×K | 82.50 | NIST |
ΔfusS | 10.42 | J/mol×K | 236.90 | NIST |
ΔfusS | 8.49 | J/mol×K | 273.93 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 3358.42] | kPa | [232.76; 487.21] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.40069e+01 | |||
Coefficient B | -2.62436e+03 | |||
Coefficient C | -4.14730e+01 | |||
Temperature range, min. | 232.76 | |||
Temperature range, max. | 487.21 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 300 400 | ||||
Pvap | 1.33 | kPa | 232.76 | Calculated Property |
Pvap | 7.80 | kPa | 261.03 | Calculated Property |
Pvap | 30.50 | kPa | 289.30 | Calculated Property |
Pvap | 90.19 | kPa | 317.58 | Calculated Property |
Pvap | 218.07 | kPa | 345.85 | Calculated Property |
Pvap | 453.78 | kPa | 374.12 | Calculated Property |
Pvap | 841.86 | kPa | 402.39 | Calculated Property |
Pvap | 1427.71 | kPa | 430.67 | Calculated Property |
Pvap | 2254.06 | kPa | 458.94 | Calculated Property |
Pvap | 3358.42 | kPa | 487.21 | Calculated Property |
Pvap | [1.95; 3548.42] | kPa | [238.15; 487.25] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.11463e+02 | |||
Coefficient B | -7.08030e+03 | |||
Coefficient C | -1.49859e+01 | |||
Coefficient D | 1.67919e-05 | |||
Temperature range, min. | 238.15 | |||
Temperature range, max. | 487.25 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 300 400 | ||||
Pvap | 1.95 | kPa | 238.15 | Calculated Property |
Pvap | 10.49 | kPa | 265.83 | Calculated Property |
Pvap | 38.02 | kPa | 293.51 | Calculated Property |
Pvap | 104.82 | kPa | 321.18 | Calculated Property |
Pvap | 238.37 | kPa | 348.86 | Calculated Property |
Pvap | 472.79 | kPa | 376.54 | Calculated Property |
Pvap | 850.73 | kPa | 404.22 | Calculated Property |
Pvap | 1428.93 | kPa | 431.89 | Calculated Property |
Pvap | 2288.07 | kPa | 459.57 | Calculated Property |
Pvap | 3548.42 | kPa | 487.25 | Calculated Property |
Find more compounds similar to Ethane, 1,1,2-trichloro-1,2,2-trifluoro-.
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