| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.6689 | Relay (1.0) Calculated Property | |
| ΔcH°solid | -6976.00 ± 3.00 | kJ/mol | NIST |
| ΔfG° | 23.64 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -139.47 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfH°solid | -247.90 | kJ/mol | NIST |
| ΔfusH° | 35.85 | kJ/mol | Solubility of Benzoin in Six Monosolvents and in Some Binary Solvent Mixtures at Various Temperatures |
| ΔvapH° | 91.91 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.73 | eV | Relay (1.0) Calculated Property |
| log10WS | [-3.23; -2.85] |
|
|
| log10WS | -3.23 | Aq. Solubility Prediction | |
| log10WS | -2.85 | Estimated Solubility | |
| logPoct/wat | 2.603 | Crippen Calculated Property | |
| McVol | 168.040 | ml/mol | McGowan Calculated Property |
| Pc | 3314.37 | kPa | Joback Calculated Property |
| Tboil | 579.67 | K | Relay (1.0) Calculated Property |
| Tc | 891.71 | K | Relay (1.0) Calculated Property |
| Tfus | [406.00; 409.15] | K |
|
| Tfus | 409.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 408.75 | K | Aq. Solubility Prediction |
| Tfus | 406.50 ± 0.50 | K | NIST |
| Tfus | 408.00 ± 2.00 | K | NIST |
| Tfus | 406.00 ± 3.00 | K | NIST |
| Tfus | 407.00 ± 3.00 | K | NIST |
| Ttriple | 410.90 | K | Solubility Modeling and Mixing Properties for Benzoin in Different Monosolvents and Solvent Mixtures at the Temperature Range from 273.15 to 313.15 K |
| Vc | 0.605 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [467.00; 617.00] | K | [1.60; 102.00] |
|
| Tboilr | 467.00 | K | 1.60 | NIST |
| Tboilr | 617.00 | K | 102.00 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [201.07; 512.78] | 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 | -6.66800e+01 | |||
| Coefficient B | 1.18790e+00 | |||
| Coefficient C | -8.15100e-04 | |||
| Coefficient D | 2.06660e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 201.07 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 260.71 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 312.56 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 357.30 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 395.57 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 428.03 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 455.32 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 478.11 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 497.05 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 512.78 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0020619; 0.0000618] | Pa×s | [407.57; 664.27] |
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 | -1.52602e+01 | |||
| Coefficient B | 3.69912e+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. | 407.57 | |||
| Temperature range, max. | 664.27 | |||
| η | 0.0020619 | Pa×s | 407.57 | Calculated Property |
| η | 0.0011388 | Pa×s | 436.09 | Calculated Property |
| η | 0.0006766 | Pa×s | 464.61 | Calculated Property |
| η | 0.0004269 | Pa×s | 493.13 | Calculated Property |
| η | 0.0002833 | Pa×s | 521.66 | Calculated Property |
| η | 0.0001961 | Pa×s | 550.18 | Calculated Property |
| η | 0.0001408 | Pa×s | 578.70 | Calculated Property |
| η | 0.0001043 | Pa×s | 607.22 | Calculated Property |
| η | 0.0000793 | Pa×s | 635.74 | Calculated Property |
| η | 0.0000618 | Pa×s | 664.27 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.13; 100.58] | kPa | [408.80; 616.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.63331e+01 | |||
| Coefficient B | -6.73380e+03 | |||
| Coefficient C | -4.15480e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 408.80 | |||
| Temperature range, max. | 616.00 | |||
| Pvap | 0.13 | kPa | 408.80 | Calculated Property |
| Pvap | 0.40 | kPa | 431.82 | Calculated Property |
| Pvap | 1.04 | kPa | 454.84 | Calculated Property |
| Pvap | 2.46 | kPa | 477.87 | Calculated Property |
| Pvap | 5.33 | kPa | 500.89 | Calculated Property |
| Pvap | 10.73 | kPa | 523.91 | Calculated Property |
| Pvap | 20.27 | kPa | 546.93 | Calculated Property |
| Pvap | 36.22 | kPa | 569.96 | Calculated Property |
| Pvap | 61.66 | kPa | 592.98 | Calculated Property |
| Pvap | 100.58 | kPa | 616.00 | Calculated Property |
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