| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.6808 | Relay (1.0) Calculated Property | |
| ΔcH°liquid | -7486.50 ± 1.30 | kJ/mol | NIST |
| ΔfG° | -260.21 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -604.36 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 36.20 | kJ/mol | Heat Capacity Measurements of 13 Methyl Esters of n-Carboxylic Acids from Methyloctanoate to Methyleicosanoate between 5 K and 350 K |
| ΔvapH° | [70.60; 72.40] | kJ/mol |
|
| ΔvapH° | 70.80 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 70.60 | kJ/mol | NIST |
| ΔvapH° | 71.37 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 71.40 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 72.40 | kJ/mol | NIST |
| IE | 9.67 | eV | Relay (1.0) Calculated Property |
| log10WS | -4.38 | Relay (1.0) Calculated Property | |
| logPoct/wat | 3.690 | Crippen Calculated Property | |
| McVol | 187.380 | ml/mol | McGowan Calculated Property |
| Pc | 1787.88 | kPa | Joback Calculated Property |
| Inp | [1405.00; 1432.00] |
|
|
| Inp | 1411.00 | NIST | |
| Inp | 1422.00 | NIST | |
| Inp | 1407.00 | NIST | |
| Inp | 1406.00 | NIST | |
| Inp | 1419.00 | NIST | |
| Inp | 1420.00 | NIST | |
| Inp | 1427.00 | NIST | |
| Inp | 1410.00 | NIST | |
| Inp | 1421.50 | NIST | |
| Inp | 1422.50 | NIST | |
| Inp | 1410.00 | NIST | |
| Inp | 1407.00 | NIST | |
| Inp | 1407.00 | NIST | |
| Inp | 1432.00 | NIST | |
| Inp | 1427.00 | NIST | |
| Inp | 1430.00 | NIST | |
| Inp | 1405.00 | NIST | |
| Inp | 1405.00 | NIST | |
| Inp | 1429.00 | NIST | |
| Inp | 1429.00 | NIST | |
| Inp | 1406.00 | NIST | |
| Inp | 1414.00 | NIST | |
| Inp | 1408.00 | NIST | |
| Inp | 1410.00 | NIST | |
| Inp | 1419.00 | NIST | |
| Inp | 1407.00 | NIST | |
| Inp | 1405.00 | NIST | |
| I | [1665.00; 1732.00] |
|
|
| I | 1699.00 | NIST | |
| I | 1732.00 | NIST | |
| I | 1672.00 | NIST | |
| I | 1696.60 | NIST | |
| I | 1704.60 | NIST | |
| I | 1705.70 | NIST | |
| I | 1728.70 | NIST | |
| I | 1686.70 | NIST | |
| I | 1701.80 | NIST | |
| I | 1706.60 | NIST | |
| I | 1711.60 | NIST | |
| I | 1710.00 | NIST | |
| I | 1732.00 | NIST | |
| I | 1694.00 | NIST | |
| I | 1703.00 | NIST | |
| I | 1710.00 | NIST | |
| I | Outlier 1665.00 | NIST | |
| I | 1695.00 | NIST | |
| Tboil | 344.15 ± 2.00 | K | NIST |
| Tc | 694.92 | K | Relay (1.0) Calculated Property |
| Tfus | 261.80 ± 0.05 | K | NIST |
| Ttriple | 262.00 | K | Heat capacities of potential organic phase change materials |
| Vc | 0.732 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [276.38; 646.53] | 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 | 1.73890e+01 | |||
| Coefficient B | 1.08904e+00 | |||
| Coefficient C | -5.34400e-04 | |||
| Coefficient D | 7.45000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 276.38 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 339.08 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 395.84 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 446.88 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 492.46 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 532.80 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 568.14 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 598.72 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 624.77 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 646.53 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0060560; 0.0002341] | Pa×s | [261.80; 489.67] |
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 | -1.20971e+01 | |||
| Coefficient B | 1.83008e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 261.80 | |||
| Temperature range, max. | 489.67 | |||
| η | 0.0060560 | Pa×s | 261.80 | Calculated Property |
| η | 0.0032695 | Pa×s | 287.12 | Calculated Property |
| η | 0.0019506 | Pa×s | 312.44 | Calculated Property |
| η | 0.0012574 | Pa×s | 337.76 | Calculated Property |
| η | 0.0008617 | Pa×s | 363.07 | Calculated Property |
| η | 0.0006204 | Pa×s | 388.39 | Calculated Property |
| η | 0.0004650 | Pa×s | 413.71 | Calculated Property |
| η | 0.0003603 | Pa×s | 439.03 | Calculated Property |
| η | 0.0002870 | Pa×s | 464.35 | Calculated Property |
| η | 0.0002341 | Pa×s | 489.67 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [389.72; 540.23] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.55084e+01 | |||
| Coefficient B | -4.64990e+03 | |||
| Coefficient C | -8.42230e+01 | |||
| Temperature range, min. | 389.72 | |||
| Temperature range, max. | 540.23 | |||
| Pvap | 1.33 | kPa | 389.72 | Calculated Property |
| Pvap | 2.94 | kPa | 406.44 | Calculated Property |
| Pvap | 5.99 | kPa | 423.17 | Calculated Property |
| Pvap | 11.41 | kPa | 439.89 | Calculated Property |
| Pvap | 20.53 | kPa | 456.61 | Calculated Property |
| Pvap | 35.11 | kPa | 473.34 | Calculated Property |
| Pvap | 57.44 | kPa | 490.06 | Calculated Property |
| Pvap | 90.40 | kPa | 506.78 | Calculated Property |
| Pvap | 137.44 | kPa | 523.51 | Calculated Property |
| Pvap | 202.63 | kPa | 540.23 | Calculated Property |
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