Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -423.66 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -476.83 | kJ/mol | Joback Calculated Property |
ΔfusH° | 7.10 | kJ/mol | Joback Calculated Property |
ΔvapH° | 18.41 | kJ/mol | Joback Calculated Property |
log10WS | -0.37 | Crippen Calculated Property | |
logPoct/wat | 0.925 | Crippen Calculated Property | |
McVol | 42.580 | ml/mol | McGowan Calculated Property |
Pc | 4444.44 | kPa | Joback Calculated Property |
Inp | [368.00; 368.00] |
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|
Inp | 368.00 | NIST | |
Inp | 368.00 | NIST | |
Tboil | 283.65 ± 1.00 | K | NIST |
Tc | 381.80 | K | Joback Calculated Property |
Tfus | 113.48 | K | Joback Calculated Property |
Vc | 0.183 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [59.58; 80.41] | J/mol×K | [243.70; 381.80] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 60 65 70 75 80 250 300 350 | ||||
Cp,gas | 59.58 | J/mol×K | 243.70 | Joback Calculated Property |
Cp,gas | 63.31 | J/mol×K | 266.72 | Joback Calculated Property |
Cp,gas | 66.93 | J/mol×K | 289.73 | Joback Calculated Property |
Cp,gas | 70.45 | J/mol×K | 312.75 | Joback Calculated Property |
Cp,gas | 73.87 | J/mol×K | 335.76 | Joback Calculated Property |
Cp,gas | 77.19 | J/mol×K | 358.78 | Joback Calculated Property |
Cp,gas | 80.41 | J/mol×K | 381.80 | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [210.40; 301.44] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.50142e+01 | |||
Coefficient B | -2.58932e+03 | |||
Coefficient C | -3.45780e+01 | |||
Temperature range, min. | 210.40 | |||
Temperature range, max. | 301.44 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 | ||||
Pvap | 1.33 | kPa | 210.40 | Calculated Property |
Pvap | 2.97 | kPa | 220.52 | Calculated Property |
Pvap | 6.09 | kPa | 230.63 | Calculated Property |
Pvap | 11.65 | kPa | 240.75 | Calculated Property |
Pvap | 20.96 | kPa | 250.86 | Calculated Property |
Pvap | 35.78 | kPa | 260.98 | Calculated Property |
Pvap | 58.35 | kPa | 271.09 | Calculated Property |
Pvap | 91.42 | kPa | 281.21 | Calculated Property |
Pvap | 138.26 | kPa | 291.32 | Calculated Property |
Pvap | 202.63 | kPa | 301.44 | Calculated Property |
Pvap | [0.89; 4304.69] | kPa | [215.00; 476.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 6.09008e+01 | |||
Coefficient B | -5.04105e+03 | |||
Coefficient C | -7.05486e+00 | |||
Coefficient D | 6.85539e-06 | |||
Temperature range, min. | 215.00 | |||
Temperature range, max. | 476.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 300 400 | ||||
Pvap | 0.89 | kPa | 215.00 | Calculated Property |
Pvap | 6.47 | kPa | 244.00 | Calculated Property |
Pvap | 29.15 | kPa | 273.00 | Calculated Property |
Pvap | 94.40 | kPa | 302.00 | Calculated Property |
Pvap | 242.01 | kPa | 331.00 | Calculated Property |
Pvap | 523.59 | kPa | 360.00 | Calculated Property |
Pvap | 999.19 | kPa | 389.00 | Calculated Property |
Pvap | 1735.75 | kPa | 418.00 | Calculated Property |
Pvap | 2808.35 | kPa | 447.00 | Calculated Property |
Pvap | 4304.69 | kPa | 476.00 | Calculated Property |
Find more compounds similar to 1,2-Difluoroethane.
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