| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3054 | Relay (1.0) Calculated Property | |
| PAff | 758.80 | kJ/mol | NIST |
| BasG | 727.90 | kJ/mol | NIST |
| ΔfG° | -909.16 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -1027.57 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 12.31 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 34.12 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [11.00; 11.60] | eV |
|
| IE | 11.00 | eV | NIST |
| IE | 11.60 | eV | NIST |
| log10WS | -0.27 | Relay (1.0) Calculated Property | |
| logPoct/wat | 1.112 | Crippen Calculated Property | |
| McVol | 79.970 | ml/mol | McGowan Calculated Property |
| Pc | 3407.89 | kPa | Joback Calculated Property |
| Inp | [473.80; 474.00] |
|
|
| Inp | 474.00 | NIST | |
| Inp | 473.80 | NIST | |
| Tboil | [334.00; 335.65] | K |
|
| Tboil | 335.65 | K | Isobaric vapor-liquid equilibrium of trifluoroacetic acid + water, trifluoroacetic acid + ethyl trifluoroacetate and ethyl trifluoroacetate + ethanol binary mixtures |
| Tboil | 334.00 ± 1.00 | K | NIST |
| Tboil | 334.20 | K | NIST |
| Tc | 455.85 | K | Relay (1.0) Calculated Property |
| Tfus | 203.74 | K | Relay (1.0) Calculated Property |
| Vc | 0.303 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 34.70 | kJ/mol | 335.00 | NIST |
| n0 | 1.30860 | 293.15 | Density, viscosity, and saturated vapor pressure of ethyl trifluoroacetate |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [129.81; 256.48] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 1.84610e+01 | |||
| Coefficient B | 4.90220e-01 | |||
| Coefficient C | -3.20200e-04 | |||
| Coefficient D | 6.80000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 129.81 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 154.83 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 176.60 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 195.36 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 211.31 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 224.67 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 235.65 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 244.47 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 251.34 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 256.48 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.62] | kPa | [247.99; 353.82] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.70839e+01 | |||
| Coefficient B | -4.16538e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Temperature range, min. | 247.99 | |||
| Temperature range, max. | 353.82 | |||
| Pvap | 1.33 | kPa | 247.99 | Calculated Property |
| Pvap | 2.85 | kPa | 259.75 | Calculated Property |
| Pvap | 5.71 | kPa | 271.51 | Calculated Property |
| Pvap | 10.80 | kPa | 283.27 | Calculated Property |
| Pvap | 19.40 | kPa | 295.03 | Calculated Property |
| Pvap | 33.33 | kPa | 306.78 | Calculated Property |
| Pvap | 55.01 | kPa | 318.54 | Calculated Property |
| Pvap | 87.63 | kPa | 330.30 | Calculated Property |
| Pvap | 135.18 | kPa | 342.06 | Calculated Property |
| Pvap | 202.62 | kPa | 353.82 | Calculated Property |
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