Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -465.70 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -557.29 | kJ/mol | Joback Calculated Property |
ΔfusH° | 9.06 | kJ/mol | Joback Calculated Property |
ΔvapH° | [32.70; 34.80] | kJ/mol |
![]() |
ΔvapH° | 34.80 ± 0.40 | kJ/mol | NIST |
ΔvapH° | 32.70 | kJ/mol | NIST |
IE | [11.30; 11.60] | eV |
![]() |
IE | 11.30 | eV | NIST |
IE | 11.60 | eV | NIST |
log10WS | -3.18 | Crippen Calculated Property | |
logPoct/wat | 3.188 | Crippen Calculated Property | |
McVol | 91.540 | ml/mol | McGowan Calculated Property |
Pc | 3857.88 | kPa | Joback Calculated Property |
Inp | [681.00; 709.00] |
![]() |
|
Inp | 709.00 | NIST | |
Inp | Outlier 681.00 | NIST | |
Inp | 691.00 | NIST | |
Inp | 702.10 | NIST | |
Inp | 704.00 | NIST | |
Inp | 694.00 | NIST | |
Inp | 704.00 | NIST | |
Inp | 702.10 | NIST | |
I | [870.00; 888.00] |
![]() |
|
I | 888.00 | NIST | |
I | 870.00 | NIST | |
I | 870.00 | NIST | |
S°liquid | [273.84; 283.43] | J/mol×K |
![]() |
S°liquid | 283.43 | J/mol×K | NIST |
S°liquid | 273.84 | J/mol×K | NIST |
Tboil | [364.70; 366.20] | K |
![]() |
Tboil | 365.95 | K | KDB |
Tboil | 365.90 | K | NIST |
Tboil | 366.20 | K | NIST |
Tboil | 365.75 ± 0.40 | K | NIST |
Tboil | 364.70 ± 4.00 | K | NIST |
Tc | 592.71 | K | Joback Calculated Property |
Tfus | 238.00 | K | Joback Calculated Property |
Ttriple | [297.91; 299.70] | K |
![]() |
Ttriple | 297.91 | K | KDB |
Ttriple | 297.91 ± 0.01 | K | NIST |
Ttriple | 299.70 ± 0.02 | K | NIST |
Vc | 0.357 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [138.37; 161.61] | J/mol×K | [386.96; 592.71] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 140 145 150 155 160 400 450 500 550 | ||||
Cp,gas | 138.37 | J/mol×K | 386.96 | Joback Calculated Property |
Cp,gas | 143.76 | J/mol×K | 421.25 | Joback Calculated Property |
Cp,gas | 148.47 | J/mol×K | 455.54 | Joback Calculated Property |
Cp,gas | 152.57 | J/mol×K | 489.84 | Joback Calculated Property |
Cp,gas | 156.09 | J/mol×K | 524.13 | Joback Calculated Property |
Cp,gas | 159.09 | J/mol×K | 558.42 | Joback Calculated Property |
Cp,gas | 161.61 | J/mol×K | 592.71 | Joback Calculated Property |
Cp,liquid | [173.60; 178.59] | J/mol×K | [298.00; 300.00] | ![]() |
Cp,liquid | 173.60 | J/mol×K | 298.00 | NIST |
Cp,liquid | 175.52 | J/mol×K | 298.15 | NIST |
Cp,liquid | 178.59 | J/mol×K | 300.00 | NIST |
ΔfusH | [0.79; 3.70] | kJ/mol | [130.00; 299.70] | ![]() |
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 0.5 1 1.5 2 2.5 3 3.5 150 200 250 300 | ||||
ΔfusH | 0.79 | kJ/mol | 130.00 | NIST |
ΔfusH | 3.67 | kJ/mol | 297.91 | NIST |
ΔfusH | 3.70 | kJ/mol | 299.70 | NIST |
ΔfusH | 3.70 | kJ/mol | 299.70 | NIST |
ΔfusH | 3.70 | kJ/mol | 299.70 | NIST |
ΔsubH | [36.40; 38.20] | kJ/mol | [264.00; 265.00] | ![]() |
ΔsubH | 36.40 | kJ/mol | 264.00 | NIST |
ΔsubH | 38.20 | kJ/mol | 265.00 | NIST |
ΔvapH | [32.60; 36.60] | kJ/mol | [264.00; 366.20] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 33 34 35 36 300 350 | ||||
ΔvapH | 36.40 | kJ/mol | 264.00 | NIST |
ΔvapH | 34.60 ± 0.10 | kJ/mol | 308.00 | NIST |
ΔvapH | 34.10 ± 0.10 | kJ/mol | 315.00 | NIST |
ΔvapH | 33.60 ± 0.10 | kJ/mol | 323.00 | NIST |
ΔvapH | 33.10 ± 0.10 | kJ/mol | 330.00 | NIST |
ΔvapH | 36.60 | kJ/mol | 333.00 | NIST |
ΔvapH | 34.00 | kJ/mol | 337.00 | NIST |
ΔvapH | 32.60 ± 0.10 | kJ/mol | 338.00 | NIST |
ΔvapH | 35.17 | kJ/mol | 366.20 | NIST |
ΔfusS | [6.08; 12.35] | J/mol×K | [130.00; 299.70] | ![]() |
ΔfusS | 6.08 | J/mol×K | 130.00 | NIST |
ΔfusS | 12.31 | J/mol×K | 297.91 | NIST |
ΔfusS | 12.33 | J/mol×K | 299.70 | NIST |
ΔfusS | 12.35 | J/mol×K | 299.70 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [267.59; 390.86] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.40018e+01 | |||
Coefficient B | -2.92421e+03 | |||
Coefficient C | -5.43650e+01 | |||
Temperature range, min. | 267.59 | |||
Temperature range, max. | 390.86 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
Pvap | 1.33 | kPa | 267.59 | Calculated Property |
Pvap | 3.05 | kPa | 281.29 | Calculated Property |
Pvap | 6.35 | kPa | 294.98 | Calculated Property |
Pvap | 12.22 | kPa | 308.68 | Calculated Property |
Pvap | 22.00 | kPa | 322.38 | Calculated Property |
Pvap | 37.39 | kPa | 336.07 | Calculated Property |
Pvap | 60.51 | kPa | 349.77 | Calculated Property |
Pvap | 93.83 | kPa | 363.47 | Calculated Property |
Pvap | 140.17 | kPa | 377.16 | Calculated Property |
Pvap | 202.67 | kPa | 390.86 | Calculated Property |
Pvap | [3.39; 3303.03] | kPa | [283.00; 551.00] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 2.86377e+01 | |||
Coefficient B | -4.85447e+03 | |||
Coefficient C | -1.80130e+00 | |||
Coefficient D | -1.17110e-06 | |||
Temperature range, min. | 283.00 | |||
Temperature range, max. | 551.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 300 400 500 | ||||
Pvap | 3.39 | kPa | 283.00 | Calculated Property |
Pvap | 14.20 | kPa | 312.78 | Calculated Property |
Pvap | 45.41 | kPa | 342.56 | Calculated Property |
Pvap | 118.41 | kPa | 372.33 | Calculated Property |
Pvap | 263.50 | kPa | 402.11 | Calculated Property |
Pvap | 517.31 | kPa | 431.89 | Calculated Property |
Pvap | 918.15 | kPa | 461.67 | Calculated Property |
Pvap | 1500.68 | kPa | 491.44 | Calculated Property |
Pvap | 2290.96 | kPa | 521.22 | Calculated Property |
Pvap | 3303.03 | kPa | 551.00 | Calculated Property |
Find more compounds similar to Ethane, 1,1,2,2-tetrachloro-1,2-difluoro-.
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.