| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.6032 | Relay (1.0) Calculated Property | |
| Cp,liquid | 306.77 | J/mol×K | Vapour pressures and heat capacity measurements on the C7 C9 secondary aliphatic alcohols |
| ΔfG° | -131.20 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -354.80 ± 2.10 | kJ/mol | NIST |
| ΔfH°liquid | -416.30 ± 0.67 | kJ/mol | NIST |
| ΔfusH° | 14.45 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 62.40 ± 0.30 | kJ/mol | NIST |
| IE | [9.61; 10.03] | eV |
|
| IE | 9.61 ± 0.03 | eV | NIST |
| IE | 10.03 | eV | NIST |
| log10WS | [-1.40; -1.40] |
|
|
| log10WS | -1.40 | Aq. Solubility Prediction | |
| log10WS | -1.40 | Estimated Solubility | |
| logPoct/wat | 1.948 | Crippen Calculated Property | |
| McVol | 115.360 | ml/mol | McGowan Calculated Property |
| Pc | 3121.00 | kPa | Joback Calculated Property |
| ρc | [268.43; 268.43] | kg/m3 |
|
| ρc | 268.43 | kg/m3 | NIST |
| ρc | 268.43 ± 19.75 | kg/m3 | NIST |
| Inp | [865.00; 881.00] |
|
|
| Inp | Outlier 865.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 881.00 | NIST | |
| I | [1250.00; 1308.00] |
|
|
| I | 1290.00 | NIST | |
| I | 1281.00 | NIST | |
| I | 1272.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1308.00 | NIST | |
| I | 1285.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1288.00 | NIST | |
| I | 1308.00 | NIST | |
| I | 1290.00 | NIST | |
| Tboil | [425.15; 429.10] | K |
|
| Tboil | 426.65 ± 1.50 | K | NIST |
| Tboil | 428.15 ± 2.00 | K | NIST |
| Tboil | 428.15 ± 3.00 | K | NIST |
| Tboil | 428.25 ± 0.50 | K | NIST |
| Tboil | 428.45 ± 1.00 | K | NIST |
| Tboil | 427.40 ± 2.00 | K | NIST |
| Tboil | Outlier 425.15 ± 3.00 | K | NIST |
| Tboil | 428.55 ± 2.00 | K | NIST |
| Tboil | 428.15 ± 3.00 | K | NIST |
| Tboil | 429.10 ± 1.00 | K | NIST |
| Tboil | 427.65 ± 2.00 | K | NIST |
| Tboil | 426.15 ± 3.00 | K | NIST |
| Tc | [602.60; 602.60] | K |
|
| Tc | 602.60 ± 0.50 | K | NIST |
| Tc | 602.60 | K | NIST |
| Tc | 602.60 ± 0.25 | K | NIST |
| Tfus | [231.55; 235.10] | K |
|
| Tfus | 235.10 | K | Calorimetric and FTIR study of selected aliphatic heptanols |
| Tfus | 231.55 | K | Aq. Solubility Prediction |
| Vc | 0.432 | m3/kmol | NIST |
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 337.00 | K | 2.10 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [166.17; 399.67] | 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 | 1.34000e-01 | |||
| Coefficient B | 7.08740e-01 | |||
| Coefficient C | -3.90600e-04 | |||
| Coefficient D | 8.14000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 166.17 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 205.59 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 241.04 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 272.78 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 301.07 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 326.15 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 348.30 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 367.76 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 384.80 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 399.67 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0570846; 0.0003079] | Pa×s | [233.32; 421.82] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.45507e+01 | |||
| Coefficient B | 2.72697e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 233.32 | |||
| Temperature range, max. | 421.82 | |||
| η | 0.0570846 | Pa×s | 233.32 | Calculated Property |
| η | 0.0217987 | Pa×s | 254.27 | Calculated Property |
| η | 0.0096378 | Pa×s | 275.21 | Calculated Property |
| η | 0.0047825 | Pa×s | 296.16 | Calculated Property |
| η | 0.0026034 | Pa×s | 317.10 | Calculated Property |
| η | 0.0015281 | Pa×s | 338.04 | Calculated Property |
| η | 0.0009544 | Pa×s | 358.99 | Calculated Property |
| η | 0.0006279 | Pa×s | 379.93 | Calculated Property |
| η | 0.0004316 | Pa×s | 400.88 | Calculated Property |
| η | 0.0003079 | Pa×s | 421.82 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [332.99; 450.86] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.52932e+01 | |||
| Coefficient B | -3.51406e+03 | |||
| Coefficient C | -9.88080e+01 | |||
| Temperature range, min. | 332.99 | |||
| Temperature range, max. | 450.86 | |||
| Pvap | 1.33 | kPa | 332.99 | Calculated Property |
| Pvap | 2.95 | kPa | 346.09 | Calculated Property |
| Pvap | 6.03 | kPa | 359.18 | Calculated Property |
| Pvap | 11.51 | kPa | 372.28 | Calculated Property |
| Pvap | 20.71 | kPa | 385.38 | Calculated Property |
| Pvap | 35.39 | kPa | 398.47 | Calculated Property |
| Pvap | 57.83 | kPa | 411.57 | Calculated Property |
| Pvap | 90.85 | kPa | 424.67 | Calculated Property |
| Pvap | 137.80 | kPa | 437.76 | Calculated Property |
| Pvap | 202.66 | kPa | 450.86 | Calculated Property |
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