- InChI
- InChI=1S/C14H12O2/c15-14(13-9-5-2-6-10-13)16-11-12-7-3-1-4-8-12/h1-10H,11H2
- InChI Key
- SESFRYSPDFLNCH-UHFFFAOYSA-N
- Formula
- C14H12O2
- SMILES
- O=C(OCc1ccccc1)c1ccccc1
- Molecular Weight1
- 212.24
- CAS
- 120-51-4
- Other Names
-
- Ascabin
- Ascabiol
- BENYLATE
- BENZYL ALCOHOL BENZOIC ESTER
- BENZYL BENZENECARBOXYLATE
- Benzoic acid, benzyl ester
- Benzoic acid, phenylmethyl ester
- Benzyl phenylformate
- Benzylester kyseliny benzoove
- Benzylets
- Colebenz
- NSC 8081
- Novoscabin
- Peruscabin
- Phenylmethyl (benzyl) ester
- Phenylmethyl benzoate
- Scabagen
- Scabanca
- Scabide
- Scabiozon
- Scabitox
- Scobenol
- Vanzoate
- Venzoate
- Venzonate
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfG° | 57.90 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -104.03 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 22.89 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 60.47 | kJ/mol | Joback Calculated Property |
| log10WS | -3.82 | Crippen Calculated Property | |
| logPoct/wat | 3.044 | Crippen Calculated Property | |
| McVol | 168.040 | ml/mol | McGowan Calculated Property |
| Pc | 2909.25 | kPa | Joback Calculated Property |
| Inp | [1712.00; 1799.00] |
|
|
| Inp | 1736.20 | NIST | |
| Inp | Outlier 1712.00 | NIST | |
| Inp | 1725.00 | NIST | |
| Inp | 1741.00 | NIST | |
| Inp | 1741.00 | NIST | |
| Inp | 1756.00 | NIST | |
| Inp | 1771.00 | NIST | |
| Inp | 1789.00 | NIST | |
| Inp | 1730.00 | NIST | |
| Inp | 1755.00 | NIST | |
| Inp | 1755.00 | NIST | |
| Inp | 1729.00 | NIST | |
| Inp | 1750.00 | NIST | |
| Inp | 1744.00 | NIST | |
| Inp | 1768.00 | NIST | |
| Inp | 1741.00 | NIST | |
| Inp | 1731.00 | NIST | |
| Inp | 1724.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1738.00 | NIST | |
| Inp | 1753.00 | NIST | |
| Inp | 1775.00 | NIST | |
| Inp | 1770.00 | NIST | |
| Inp | 1725.00 | NIST | |
| Inp | 1751.00 | NIST | |
| Inp | 1759.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1765.90 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1766.00 | NIST | |
| Inp | 1765.00 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1758.00 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1763.00 | NIST | |
| Inp | 1764.00 | NIST | |
| Inp | 1749.00 | NIST | |
| Inp | 1769.00 | NIST | |
| Inp | 1758.00 | NIST | |
| Inp | 1763.00 | NIST | |
| Inp | 1763.00 | NIST | |
| Inp | 1757.00 | NIST | |
| Inp | 1765.00 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1765.00 | NIST | |
| Inp | 1763.00 | NIST | |
| Inp | 1714.00 | NIST | |
| Inp | 1720.00 | NIST | |
| Inp | 1749.00 | NIST | |
| Inp | 1763.00 | NIST | |
| Inp | 1764.00 | NIST | |
| Inp | 1733.00 | NIST | |
| Inp | 1765.00 | NIST | |
| Inp | 1737.00 | NIST | |
| Inp | 1739.00 | NIST | |
| Inp | 1716.10 | NIST | |
| Inp | 1714.50 | NIST | |
| Inp | 1734.40 | NIST | |
| Inp | 1746.60 | NIST | |
| Inp | 1719.90 | NIST | |
| Inp | 1731.00 | NIST | |
| Inp | 1724.00 | NIST | |
| Inp | 1736.00 | NIST | |
| Inp | 1765.00 | NIST | |
| Inp | 1765.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1780.00 | NIST | |
| Inp | 1751.00 | NIST | |
| Inp | 1743.00 | NIST | |
| Inp | 1732.00 | NIST | |
| Inp | 1763.00 | NIST | |
| Inp | 1761.00 | NIST | |
| Inp | 1755.00 | NIST | |
| Inp | 1770.00 | NIST | |
| Inp | 1770.00 | NIST | |
| Inp | 1761.00 | NIST | |
| Inp | 1730.00 | NIST | |
| Inp | 1764.00 | NIST | |
| Inp | 1722.00 | NIST | |
| Inp | 1772.00 | NIST | |
| Inp | 1733.00 | NIST | |
| Inp | Outlier 1795.00 | NIST | |
| Inp | Outlier 1794.00 | NIST | |
| Inp | Outlier 1794.00 | NIST | |
| Inp | Outlier 1796.00 | NIST | |
| Inp | Outlier 1799.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1772.00 | NIST | |
| Inp | 1761.00 | NIST | |
| Inp | 1775.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1743.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1731.00 | NIST | |
| Inp | 1774.00 | NIST | |
| Inp | 1769.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1719.00 | NIST | |
| Inp | 1722.00 | NIST | |
| Inp | 1721.00 | NIST | |
| Inp | 1735.00 | NIST | |
| Inp | 1722.00 | NIST | |
| Inp | 1723.00 | NIST | |
| Inp | 1785.00 | NIST | |
| Inp | 1739.00 | NIST | |
| Inp | 1763.00 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1771.00 | NIST | |
| Inp | 1758.00 | NIST | |
| Inp | 1759.00 | NIST | |
| Inp | 1730.00 | NIST | |
| Inp | 1791.00 | NIST | |
| Inp | 1784.00 | NIST | |
| Inp | 1789.00 | NIST | |
| Inp | 1789.00 | NIST | |
| Inp | 1780.00 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1726.00 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1763.00 | NIST | |
| Inp | 1792.00 | NIST | |
| Inp | 1731.00 | NIST | |
| Inp | 1785.00 | NIST | |
| Inp | 1761.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1754.00 | NIST | |
| Inp | 1782.00 | NIST | |
| Inp | 1719.00 | NIST | |
| Inp | 1742.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1748.00 | NIST | |
| Inp | 1729.00 | NIST | |
| Inp | 1766.00 | NIST | |
| Inp | 1766.00 | NIST | |
| Inp | 1723.00 | NIST | |
| Inp | 1723.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1738.00 | NIST | |
| Inp | 1761.00 | NIST | |
| Inp | 1765.00 | NIST | |
| Inp | 1730.00 | NIST | |
| Inp | 1742.00 | NIST | |
| Inp | 1714.00 | NIST | |
| Inp | 1730.00 | NIST | |
| Inp | 1723.00 | NIST | |
| Inp | 1724.00 | NIST | |
| Inp | 1777.00 | NIST | |
| Inp | 1723.70 | NIST | |
| Inp | 1724.20 | NIST | |
| Inp | 1723.80 | NIST | |
| Inp | 1728.90 | NIST | |
| Inp | 1720.00 | NIST | |
| Inp | 1745.00 | NIST | |
| Inp | 1719.00 | NIST | |
| Inp | 1761.00 | NIST | |
| Inp | 1757.00 | NIST | |
| Inp | 1761.00 | NIST | |
| Inp | 1761.00 | NIST | |
| Inp | 1769.00 | NIST | |
| Inp | 1772.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1723.00 | NIST | |
| Inp | 1770.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1771.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1770.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1763.00 | NIST | |
| Inp | 1765.00 | NIST | |
| Inp | 1723.00 | NIST | |
| Inp | 1768.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1761.00 | NIST | |
| Inp | 1741.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1736.00 | NIST | |
| Inp | 1723.00 | NIST | |
| Inp | 1741.00 | NIST | |
| Inp | 1741.00 | NIST | |
| Inp | 1738.00 | NIST | |
| Inp | 1738.00 | NIST | |
| Inp | 1763.00 | NIST | |
| Inp | 1761.00 | NIST | |
| Inp | 1733.00 | NIST | |
| Inp | Outlier 1799.00 | NIST | |
| Inp | 1760.00 | NIST | |
| Inp | 1769.00 | NIST | |
| Inp | 1735.00 | NIST | |
| Inp | 1730.00 | NIST | |
| Inp | 1780.00 | NIST | |
| Inp | 1762.00 | NIST | |
| Inp | 1742.00 | NIST | |
| Inp | 1766.00 | NIST | |
| Inp | 1724.20 | NIST | |
| Inp | 1719.00 | NIST | |
| Inp | 1736.20 | NIST | |
| Inp | 1756.00 | NIST | |
| Inp | 1753.00 | NIST | |
| Inp | 1759.00 | NIST | |
| Inp | 1765.00 | NIST | |
| Inp | 1749.00 | NIST | |
| Inp | 1737.00 | NIST | |
| Inp | 1746.60 | NIST | |
| Inp | 1743.00 | NIST | |
| I | [2566.00; 2655.00] |
|
|
| I | 2569.00 | NIST | |
| I | 2576.00 | NIST | |
| I | 2576.00 | NIST | |
| I | 2607.00 | NIST | |
| I | 2636.00 | NIST | |
| I | 2566.00 | NIST | |
| I | 2618.00 | NIST | |
| I | 2579.00 | NIST | |
| I | 2652.00 | NIST | |
| I | 2583.00 | NIST | |
| I | 2570.00 | NIST | |
| I | 2644.00 | NIST | |
| I | 2636.00 | NIST | |
| I | 2581.00 | NIST | |
| I | 2613.00 | NIST | |
| I | 2571.00 | NIST | |
| I | 2618.00 | NIST | |
| I | 2655.00 | NIST | |
| I | 2655.00 | NIST | |
| I | 2639.00 | NIST | |
| I | 2655.00 | NIST | |
| I | 2607.00 | NIST | |
| I | 2647.00 | NIST | |
| I | 2655.00 | NIST | |
| I | 2655.00 | NIST | |
| I | 2655.00 | NIST | |
| I | 2655.00 | NIST | |
| I | 2655.00 | NIST | |
| I | 2655.00 | NIST | |
| I | 2655.00 | NIST | |
| I | 2655.00 | NIST | |
| I | 2655.00 | NIST | |
| I | 2655.00 | NIST | |
| I | 2655.00 | NIST | |
| I | 2655.00 | NIST | |
| I | 2638.00 | NIST | |
| I | 2633.00 | NIST | |
| I | 2655.00 | NIST | |
| I | 2636.00 | NIST | |
| I | 2647.00 | NIST | |
| I | 2569.00 | NIST | |
| I | 2618.00 | NIST | |
| Tboil | [596.20; 596.70] | K |
|
| Tboil | 596.70 | K | NIST |
| Tboil | 596.50 ± 0.50 | K | NIST |
| Tboil | 596.20 ± 1.00 | K | NIST |
| Tc | 892.14 | K | Joback Calculated Property |
| Tfus | [292.00; 294.99] | K |
|
| Tfus | 294.99 ± 0.20 | K | NIST |
| Tfus | 294.00 | K | NIST |
| Tfus | 292.60 ± 0.50 | K | NIST |
| Tfus | 292.00 ± 0.30 | K | NIST |
| Vc | 0.627 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [415.95; 490.57] | J/mol×K | [649.37; 892.14] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 420 440 460 480 700 800 | ||||
| Cp,gas | 415.95 | J/mol×K | 649.37 | Joback Calculated Property |
| Cp,gas | 431.27 | J/mol×K | 689.83 | Joback Calculated Property |
| Cp,gas | 445.36 | J/mol×K | 730.29 | Joback Calculated Property |
| Cp,gas | 458.28 | J/mol×K | 770.75 | Joback Calculated Property |
| Cp,gas | 470.08 | J/mol×K | 811.21 | Joback Calculated Property |
| Cp,gas | 480.83 | J/mol×K | 851.67 | Joback Calculated Property |
| Cp,gas | 490.57 | J/mol×K | 892.14 | Joback Calculated Property |
| η | [0.0001512; 0.0016037] | Pa×s | [372.54; 649.37] |
|
|
T(K) Dynamic viscosity (Pa×s) 2.00e-4 4.00e-4 6.00e-4 8.00e-4 1.00e-3 1.20e-3 1.40e-3 1.60e-3 400 500 600 | ||||
| η | 0.0016037 | Pa×s | 372.54 | Joback Calculated Property |
| η | 0.0008710 | Pa×s | 418.68 | Joback Calculated Property |
| η | 0.0005339 | Pa×s | 464.82 | Joback Calculated Property |
| η | 0.0003576 | Pa×s | 510.96 | Joback Calculated Property |
| η | 0.0002559 | Pa×s | 557.09 | Joback Calculated Property |
| η | 0.0001928 | Pa×s | 603.23 | Joback Calculated Property |
| η | 0.0001512 | Pa×s | 649.37 | Joback Calculated Property |
| ΔfusH | [20.44; 20.44] | kJ/mol | [293.10; 293.10] |
|
| ΔfusH | 20.44 | kJ/mol | 293.10 | NIST |
| ΔfusH | 20.44 | kJ/mol | 293.10 | NIST |
| ΔvapH | [59.70; 77.70] | kJ/mol | [325.00; 549.50] |
|
| ΔvapH | 77.70 | kJ/mol | 325.00 | NIST |
| ΔvapH | 59.70 | kJ/mol | 549.50 | NIST |
| γ | [0.03; 0.04] | N/m | [353.15; 473.15] |
|
|
T(K) Surface Tension (N/m) 0.03 0.03 0.03 0.03 0.03 0.04 0.04 0.04 400 450 | ||||
| γ | 0.04 | N/m | 353.15 | Measuri... |
| γ | 0.04 | N/m | 373.15 | Measuri... |
| γ | 0.04 | N/m | 393.15 | Measuri... |
| γ | 0.03 | N/m | 413.15 | Measuri... |
| γ | 0.03 | N/m | 433.15 | Measuri... |
| γ | 0.03 | N/m | 453.15 | Measuri... |
| γ | 0.03 | N/m | 473.15 | Measuri... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [448.96; 632.30] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.52484e+01 | |||
| Coefficient B | -5.42518e+03 | |||
| Coefficient C | -8.63370e+01 | |||
| Temperature range, min. | 448.96 | |||
| Temperature range, max. | 632.30 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 600 | ||||
| Pvap | 1.33 | kPa | 448.96 | Calculated Property |
| Pvap | 2.95 | kPa | 469.33 | Calculated Property |
| Pvap | 6.04 | kPa | 489.70 | Calculated Property |
| Pvap | 11.53 | kPa | 510.07 | Calculated Property |
| Pvap | 20.75 | kPa | 530.44 | Calculated Property |
| Pvap | 35.45 | kPa | 550.82 | Calculated Property |
| Pvap | 57.91 | kPa | 571.19 | Calculated Property |
| Pvap | 90.93 | kPa | 591.56 | Calculated Property |
| Pvap | 137.87 | kPa | 611.93 | Calculated Property |
| Pvap | 202.65 | kPa | 632.30 | Calculated Property |
| Pvap | [2.01e-05; 2495.89] | kPa | [292.55; 820.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 9.04348e+01 | |||
| Coefficient B | -1.27055e+04 | |||
| Coefficient C | -1.02137e+01 | |||
| Coefficient D | 2.09556e-06 | |||
| Temperature range, min. | 292.55 | |||
| Temperature range, max. | 820.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 400 600 800 | ||||
| Pvap | 2.01e-05 | kPa | 292.55 | Calculated Property |
| Pvap | 4.73e-03 | kPa | 351.16 | Calculated Property |
| Pvap | 0.19 | kPa | 409.76 | Calculated Property |
| Pvap | 2.61 | kPa | 468.37 | Calculated Property |
| Pvap | 18.09 | kPa | 526.97 | Calculated Property |
| Pvap | 78.89 | kPa | 585.58 | Calculated Property |
| Pvap | 249.34 | kPa | 644.18 | Calculated Property |
| Pvap | 626.18 | kPa | 702.79 | Calculated Property |
| Pvap | 1329.99 | kPa | 761.39 | Calculated Property |
| Pvap | 2495.89 | kPa | 820.00 | Calculated Property |
Similar Compounds
![1,4-Benzenedicarboxylic acid, [4-(methoxycarbonyl)phenyl]methyl methyl ester.](data:image/png;base64,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)
Find more compounds similar to Benzyl Benzoate.
Mixtures
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Effect of Hydrotropes on the Solubility and Mass Transfer Coefficient of Benzyl Benzoate in Water
- Measuring Surface Tension of Liquids at High Temperature and Elevated Pressure
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.