| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 1.4141 | Relay (1.0) Calculated Property | |
| ΔfG° | 363.02 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -736.06 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 92.02 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 166.57 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.30 | eV | Relay (1.0) Calculated Property |
| log10WS | -11.19 | Relay (1.0) Calculated Property | |
| logPoct/wat | 13.051 | Crippen Calculated Property | |
| McVol | 528.080 | ml/mol | McGowan Calculated Property |
| Pc | 457.35 | kPa | Joback Calculated Property |
| Tboil | 689.17 | K | Relay (1.0) Calculated Property |
| Tc | 849.14 | K | Relay (1.0) Calculated Property |
| Tfus | [288.85; 289.20] | K |
|
| Tfus | 289.20 | K | Solid-liquid equilibrium, excess molar volume, and deviations in the molar refractivity for the binary and ternary mixtures of Alamine 304-1 with 1-octanol, 2-octanol, and 1-decanol |
| Tfus | 288.85 ± 1.00 | K | NIST |
| Vc | 2.062 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 82.10 | kJ/mol | 693.00 | NIST |
| ρl | 819.23 | kg/m3 | 298.15 | Solid Liquid Equilibria, Excess Molar Volumes, and Deviations in the Molar Refractivity for the Binary Systems of Alamine 304-1 + Decane, Dodecane, or Dodecanol |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [784.69; 1914.63] | 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 | -4.05270e+01 | |||
| Coefficient B | 3.54776e+00 | |||
| Coefficient C | -2.04720e-03 | |||
| Coefficient D | 4.54600e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 784.69 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 978.50 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 1151.89 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 1306.30 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 1443.16 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 1563.92 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 1670.01 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 1762.86 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 1843.93 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 1914.63 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [558.92; 836.24] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.28712e+01 | |||
| Coefficient B | -5.25100e+03 | |||
| Coefficient C | -1.41630e+02 | |||
| Temperature range, min. | 558.92 | |||
| Temperature range, max. | 836.24 | |||
| Pvap | 1.33 | kPa | 558.92 | Calculated Property |
| Pvap | 3.17 | kPa | 589.73 | Calculated Property |
| Pvap | 6.73 | kPa | 620.55 | Calculated Property |
| Pvap | 13.06 | kPa | 651.36 | Calculated Property |
| Pvap | 23.50 | kPa | 682.17 | Calculated Property |
| Pvap | 39.68 | kPa | 712.99 | Calculated Property |
| Pvap | 63.50 | kPa | 743.80 | Calculated Property |
| Pvap | 97.08 | kPa | 774.61 | Calculated Property |
| Pvap | 142.68 | kPa | 805.43 | Calculated Property |
| Pvap | 202.66 | kPa | 836.24 | Calculated Property |
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