- InChI
- InChI=1S/C9H10O2/c1-2-11-9(10)8-6-4-3-5-7-8/h3-7H,2H2,1H3
- InChI Key
- MTZQAGJQAFMTAQ-UHFFFAOYSA-N
- Formula
- C9H10O2
- SMILES
- CCOC(=O)c1ccccc1
- Molecular Weight1
- 150.17
- CAS
- 93-89-0
- Other Names
-
- 2-methoxy-1-phenyl-ethanone
- BENZOIC ETHER
- ETHYL BENZENECARBOXYLATE
- Essence of niobe
- Ethyl benzoate
- Ethylester kyseliny benzoove
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase 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).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (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 |
|---|---|---|---|
| ω | 0.4800 | KDB | |
| ΔfG° | -96.61 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -237.36 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 15.89 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 61.10 ± 0.30 | kJ/mol | NIST |
| IE | [8.90; 9.20] | eV |
|
| IE | 8.90 | eV | NIST |
| IE | 9.20 | eV | NIST |
| log10WS | [-2.32; -2.32] |
|
|
| log10WS | -2.32 | Aq. Sol... | |
| log10WS | -2.32 | Estimat... | |
| logPoct/wat | 1.863 | Crippen Calculated Property | |
| McVol | 121.350 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [2320.00; 3050.00] | kPa |
|
| Pc | 2320.00 | kPa | KDB |
| Pc | 3050.00 | kPa | Critica... |
| Inp | [1133.38; 1206.00] |
|
|
| Inp | 1133.38 | NIST | |
| Inp | 1153.14 | NIST | |
| Inp | 1148.70 | NIST | |
| Inp | 1144.00 | NIST | |
| Inp | 1142.00 | NIST | |
| Inp | 1142.00 | NIST | |
| Inp | 1174.00 | NIST | |
| Inp | 1147.00 | NIST | |
| Inp | 1169.00 | NIST | |
| Inp | 1166.00 | NIST | |
| Inp | 1157.00 | NIST | |
| Inp | 1176.00 | NIST | |
| Inp | 1164.00 | NIST | |
| Inp | 1176.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1178.00 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1152.00 | NIST | |
| Inp | 1157.00 | NIST | |
| Inp | 1164.00 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1143.00 | NIST | |
| Inp | 1143.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1149.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1180.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1168.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1172.90 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1141.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1175.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1143.00 | NIST | |
| Inp | 1138.20 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1141.00 | NIST | |
| Inp | 1184.00 | NIST | |
| Inp | 1168.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1147.00 | NIST | |
| Inp | 1157.00 | NIST | |
| Inp | 1143.00 | NIST | |
| Inp | 1155.00 | NIST | |
| Inp | 1145.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1155.00 | NIST | |
| Inp | 1143.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1145.00 | NIST | |
| Inp | 1153.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1156.00 | NIST | |
| Inp | 1155.00 | NIST | |
| Inp | 1156.00 | NIST | |
| Inp | 1153.00 | NIST | |
| Inp | Outlier 1206.00 | NIST | |
| Inp | Outlier 1206.00 | NIST | |
| Inp | 1169.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1155.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1187.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1140.00 | NIST | |
| Inp | 1140.00 | NIST | |
| Inp | 1139.00 | NIST | |
| Inp | 1145.00 | NIST | |
| Inp | 1145.00 | NIST | |
| Inp | 1141.00 | NIST | |
| Inp | 1175.00 | NIST | |
| Inp | 1176.00 | NIST | |
| Inp | 1177.00 | NIST | |
| Inp | 1176.00 | NIST | |
| Inp | 1175.00 | NIST | |
| Inp | 1146.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1170.80 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1165.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1138.00 | NIST | |
| Inp | 1147.00 | NIST | |
| Inp | 1176.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1146.00 | NIST | |
| Inp | 1150.00 | NIST | |
| Inp | 1150.00 | NIST | |
| Inp | 1143.00 | NIST | |
| Inp | 1147.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1139.00 | NIST | |
| Inp | 1143.00 | NIST | |
| Inp | 1149.00 | NIST | |
| Inp | 1184.00 | NIST | |
| Inp | 1147.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1151.00 | NIST | |
| Inp | 1177.00 | NIST | |
| Inp | 1174.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1175.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1168.00 | NIST | |
| Inp | 1162.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1156.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1185.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1146.00 | NIST | |
| Inp | 1151.00 | NIST | |
| Inp | 1143.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1133.38 | NIST | |
| Inp | 1142.00 | NIST | |
| Inp | 1157.00 | NIST | |
| Inp | 1178.00 | NIST | |
| Inp | 1164.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1175.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1172.90 | NIST | |
| Inp | 1143.00 | NIST | |
| Inp | 1184.00 | NIST | |
| Inp | 1156.00 | NIST | |
| Inp | Outlier 1206.00 | NIST | |
| Inp | 1155.00 | NIST | |
| I | [1634.00; 1709.00] |
|
|
| I | Outlier 1706.00 | NIST | |
| I | 1693.00 | NIST | |
| I | 1689.00 | NIST | |
| I | Outlier 1705.00 | NIST | |
| I | 1685.00 | NIST | |
| I | Outlier 1709.00 | NIST | |
| I | 1683.00 | NIST | |
| I | 1658.00 | NIST | |
| I | 1640.00 | NIST | |
| I | 1641.00 | NIST | |
| I | 1645.00 | NIST | |
| I | 1653.00 | NIST | |
| I | 1645.00 | NIST | |
| I | 1644.00 | NIST | |
| I | 1651.00 | NIST | |
| I | 1658.00 | NIST | |
| I | 1644.00 | NIST | |
| I | 1648.00 | NIST | |
| I | 1649.00 | NIST | |
| I | 1673.00 | NIST | |
| I | 1673.00 | NIST | |
| I | 1698.00 | NIST | |
| I | 1651.00 | NIST | |
| I | 1675.00 | NIST | |
| I | 1653.00 | NIST | |
| I | 1652.00 | NIST | |
| I | 1650.00 | NIST | |
| I | 1650.00 | NIST | |
| I | 1650.00 | NIST | |
| I | 1647.00 | NIST | |
| I | 1650.00 | NIST | |
| I | 1651.00 | NIST | |
| I | 1655.00 | NIST | |
| I | 1654.00 | NIST | |
| I | 1676.00 | NIST | |
| I | 1668.00 | NIST | |
| I | 1655.00 | NIST | |
| I | 1670.00 | NIST | |
| I | 1649.00 | NIST | |
| I | 1681.00 | NIST | |
| I | 1672.00 | NIST | |
| I | Outlier 1706.00 | NIST | |
| I | 1681.00 | NIST | |
| I | 1678.00 | NIST | |
| I | 1664.00 | NIST | |
| I | 1680.00 | NIST | |
| I | 1640.00 | NIST | |
| I | 1653.00 | NIST | |
| I | 1640.00 | NIST | |
| I | 1670.00 | NIST | |
| I | 1673.00 | NIST | |
| I | 1649.00 | NIST | |
| I | 1657.00 | NIST | |
| I | 1663.00 | NIST | |
| I | 1653.00 | NIST | |
| I | 1660.00 | NIST | |
| I | 1660.00 | NIST | |
| I | 1666.00 | NIST | |
| I | 1647.00 | NIST | |
| I | 1662.00 | NIST | |
| I | 1662.00 | NIST | |
| I | 1662.00 | NIST | |
| I | 1650.00 | NIST | |
| I | 1650.00 | NIST | |
| I | 1647.00 | NIST | |
| I | 1634.00 | NIST | |
| I | 1643.00 | NIST | |
| I | 1656.00 | NIST | |
| I | 1693.00 | NIST | |
| I | 1694.00 | NIST | |
| I | 1693.00 | NIST | |
| I | 1694.00 | NIST | |
| I | 1650.00 | NIST | |
| I | 1658.00 | NIST | |
| I | 1647.00 | NIST | |
| I | 1647.00 | NIST | |
| I | 1653.00 | NIST | |
| I | 1681.00 | NIST | |
| I | 1685.00 | NIST | |
| I | 1684.00 | NIST | |
| I | 1677.00 | NIST | |
| I | 1663.00 | NIST | |
| I | 1645.00 | NIST | |
| I | 1653.00 | NIST | |
| I | 1658.00 | NIST | |
| I | 1685.00 | NIST | |
| I | 1683.00 | NIST | |
| I | 1670.00 | NIST | |
| I | 1681.00 | NIST | |
| Tboil | [482.30; 486.20] | K |
|
| Tboil | 485.70 | K | KDB |
| Tboil | 486.20 | K | NIST |
| Tboil | 486.00 | K | NIST |
| Tboil | 485.65 ± 0.40 | K | NIST |
| Tboil | 485.60 ± 0.30 | K | NIST |
| Tboil | 485.60 ± 0.50 | K | NIST |
| Tboil | 485.60 ± 0.50 | K | NIST |
| Tboil | 484.00 ± 4.00 | K | NIST |
| Tboil | Outlier 482.30 ± 0.60 | K | NIST |
| Tboil | 486.05 ± 0.40 | K | NIST |
| Tboil | 484.95 ± 1.00 | K | NIST |
| Tc | 668.70 | K | KDB |
| Tfus | [238.30; 240.90] | K |
|
| Tfus | 238.30 | K | KDB |
| Tfus | 239.00 | K | NIST |
| Tfus | 238.40 ± 0.30 | K | NIST |
| Tfus | 238.45 ± 0.30 | K | NIST |
| Tfus | 238.60 ± 0.40 | K | NIST |
| Tfus | Outlier 240.90 ± 0.40 | K | NIST |
| Tfus | 238.95 ± 0.40 | K | NIST |
| Vc | 0.456 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [256.39; 321.72] | J/mol×K | [508.29; 724.46] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 250 260 270 280 290 300 310 320 550 600 650 700 | ||||
| Cp,gas | 256.39 | J/mol×K | 508.29 | Joback Calculated Property |
| Cp,gas | 269.00 | J/mol×K | 544.32 | Joback Calculated Property |
| Cp,gas | 280.90 | J/mol×K | 580.35 | Joback Calculated Property |
| Cp,gas | 292.11 | J/mol×K | 616.37 | Joback Calculated Property |
| Cp,gas | 302.63 | J/mol×K | 652.40 | Joback Calculated Property |
| Cp,gas | 312.50 | J/mol×K | 688.43 | Joback Calculated Property |
| Cp,gas | 321.72 | J/mol×K | 724.46 | Joback Calculated Property |
| Cp,liquid | [241.80; 282.80] | J/mol×K | [290.00; 298.15] |
|
| Cp,liquid | 282.80 | J/mol×K | 290.00 | NIST |
| Cp,liquid | 241.80 | J/mol×K | 292.70 | NIST |
| Cp,liquid | 241.80 | J/mol×K | 292.70 | NIST |
| Cp,liquid | 246.00 | J/mol×K | 298.15 | NIST |
| η | [0.0013680; 0.0024440] | Pa×s | [288.15; 318.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 1.40e-3 1.60e-3 1.80e-3 2.00e-3 2.20e-3 2.40e-3 290 300 310 | ||||
| η | 0.0024440 | Pa×s | 288.15 | Densiti... |
| η | 0.0019710 | Pa×s | 298.15 | Densiti... |
| η | 0.0017480 | Pa×s | 303.15 | Viscosi... |
| η | 0.0016240 | Pa×s | 308.15 | Densiti... |
| η | 0.0014380 | Pa×s | 313.15 | Viscosi... |
| η | 0.0013680 | Pa×s | 318.15 | Densiti... |
| ΔvapH | [43.60; 57.00] | kJ/mol | [310.50; 450.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 44 46 48 50 52 54 56 58 350 400 450 | ||||
| ΔvapH | 55.90 | kJ/mol | 310.50 | NIST |
| ΔvapH | 57.00 | kJ/mol | 392.00 | NIST |
| ΔvapH | 50.50 | kJ/mol | 392.00 | NIST |
| ΔvapH | 51.90 | kJ/mol | 401.50 | NIST |
| ΔvapH | 50.40 | kJ/mol | 422.50 | NIST |
| ΔvapH | 43.60 ± 0.50 | kJ/mol | 450.00 | NIST |
| ΔvapH | 52.50 ± 0.20 | kJ/mol | 450.00 | NIST |
| ΔvapH | 49.60 ± 0.20 | kJ/mol | 450.00 | NIST |
| ΔvapH | 46.70 ± 0.30 | kJ/mol | 450.00 | NIST |
| Pvap | [7.10e-03; 0.29] | kPa | [283.90; 332.50] |
|
|
T(K) Vapor pressure (kPa) 0 0.05 0.1 0.15 0.2 0.25 0.3 300 320 | ||||
| Pvap | 7.10e-03 | kPa | 283.90 | Thermod... |
| Pvap | 9.30e-03 | kPa | 286.90 | Thermod... |
| Pvap | 0.01 | kPa | 289.00 | Thermod... |
| Pvap | 0.01 | kPa | 292.00 | Thermod... |
| Pvap | 0.02 | kPa | 294.10 | Thermod... |
| Pvap | 0.02 | kPa | 295.00 | Thermod... |
| Pvap | 0.02 | kPa | 298.10 | Thermod... |
| Pvap | 0.03 | kPa | 299.10 | Thermod... |
| Pvap | 0.03 | kPa | 301.20 | Thermod... |
| Pvap | 0.04 | kPa | 304.20 | Thermod... |
| Pvap | 0.05 | kPa | 307.20 | Thermod... |
| Pvap | 0.06 | kPa | 310.10 | Thermod... |
| Pvap | 0.07 | kPa | 312.30 | Thermod... |
| Pvap | 0.09 | kPa | 315.30 | Thermod... |
| Pvap | 0.11 | kPa | 317.30 | Thermod... |
| Pvap | 0.13 | kPa | 320.30 | Thermod... |
| Pvap | 0.17 | kPa | 323.40 | Thermod... |
| Pvap | 0.20 | kPa | 326.40 | Thermod... |
| Pvap | 0.25 | kPa | 329.50 | Thermod... |
| Pvap | 0.29 | kPa | 332.50 | Thermod... |
| ρl | [1041.30; 1046.00] | kg/m3 | [293.00; 303.15] |
|
|
T(K) Liquid Density (kg/m3) 1041 1042 1043 1044 1045 1046 295 300 | ||||
| ρl | 1046.00 | kg/m3 | 293.00 | KDB |
| ρl | 1041.30 | kg/m3 | 298.15 | Excess ... |
| ρl | 1041.30 | kg/m3 | 298.15 | Excess ... |
| ρl | 1041.42 | kg/m3 | 298.15 | Refract... |
| ρl | 1042.00 | kg/m3 | 303.15 | Study o... |
| γ | [0.03; 0.04] | N/m | [288.15; 358.15] |
|
|
T(K) Surface Tension (N/m) 0.03 0.03 0.03 0.03 0.04 300 320 340 | ||||
| γ | 0.04 | N/m | 288.15 | Densiti... |
| γ | 0.03 | N/m | 298.15 | Densiti... |
| γ | 0.03 | N/m | 308.15 | Densiti... |
| γ | 0.03 | N/m | 318.15 | Densiti... |
| γ | 0.03 | N/m | 328.15 | Densiti... |
| γ | 0.03 | N/m | 338.15 | Densiti... |
| γ | 0.03 | N/m | 348.15 | Densiti... |
| γ | 0.03 | N/m | 358.15 | Densiti... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [360.20; 360.30] | K | [1.30; 1.30] |
|
| Tboilr | 360.20 | K | 1.30 | NIST |
| Tboilr | 360.30 | K | 1.30 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [358.72; 517.33] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.52741e+01 | |||
| Coefficient B | -4.71347e+03 | |||
| Coefficient C | -4.42100e+01 | |||
| Temperature range, min. | 358.72 | |||
| Temperature range, max. | 517.33 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
| Pvap | 1.33 | kPa | 358.72 | Calculated Property |
| Pvap | 2.95 | kPa | 376.34 | Calculated Property |
| Pvap | 6.04 | kPa | 393.97 | Calculated Property |
| Pvap | 11.52 | kPa | 411.59 | Calculated Property |
| Pvap | 20.73 | kPa | 429.21 | Calculated Property |
| Pvap | 35.42 | kPa | 446.84 | Calculated Property |
| Pvap | 57.87 | kPa | 464.46 | Calculated Property |
| Pvap | 90.89 | kPa | 482.08 | Calculated Property |
| Pvap | 137.84 | kPa | 499.71 | Calculated Property |
| Pvap | 202.67 | kPa | 517.33 | Calculated Property |
| Pvap | [1.25e-04; 3203.03] | kPa | [238.45; 698.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.97631e+01 | |||
| Coefficient B | -8.66976e+03 | |||
| Coefficient C | -7.77947e+00 | |||
| Coefficient D | 3.43034e-06 | |||
| Temperature range, min. | 238.45 | |||
| Temperature range, max. | 698.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 400 600 | ||||
| Pvap | 1.25e-04 | kPa | 238.45 | Calculated Property |
| Pvap | 0.02 | kPa | 289.51 | Calculated Property |
| Pvap | 0.52 | kPa | 340.57 | Calculated Property |
| Pvap | 5.51 | kPa | 391.63 | Calculated Property |
| Pvap | 31.56 | kPa | 442.69 | Calculated Property |
| Pvap | 120.54 | kPa | 493.76 | Calculated Property |
| Pvap | 348.62 | kPa | 544.82 | Calculated Property |
| Pvap | 829.21 | kPa | 595.88 | Calculated Property |
| Pvap | 1714.57 | kPa | 646.94 | Calculated Property |
| Pvap | 3203.03 | kPa | 698.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzoic acid, ethyl ester.
Mixtures
- 1-Propanol + 1-Butanol + Benzoic acid, ethyl ester
- 1-Propanol + 1-Pentanol + Benzoic acid, ethyl ester
- 1-Propanol + Benzoic acid, ethyl ester
- Carbonic acid, dimethyl ester + Benzoic acid, ethyl ester
- Benzoic acid, ethyl ester + o-Xylene
- Benzene, 1,3-dimethyl- + Benzoic acid, ethyl ester
- p-Xylene + Benzoic acid, ethyl ester
- Ethylbenzene + Benzoic acid, ethyl ester
- Ethanol + Benzoic acid, ethyl ester
- Carbon dioxide + Benzoic acid, ethyl ester
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Study of molecular interactions in the mixtures of some primary alcohols with equimolar mixture of 1-propanol and alkylbenzoates at T = 303.15 K
- Excess Molar Entalpies of Dimethyl Carbonate with o-Xylene, m-Xylene, p-Xylene, Ethylbenzene, or Ethyl Benzoate at 298.15 K
- Excess Molar Enthalpies for Dimethyl Carbonate with o-Xylene, m-Xylene, p-Xylene, Ethylbenzene or Ethyl Benzoate at 298.15 K and 10.2 MPa
- Viscosity, Density, and Refractive Index of Some (Ester + Hydrocarbon) Binary Mixtures at 303.15 K and 313.15 K
- Densities, Viscosities, Refractive Indices, and Surface Tensions for 12 Flavor Esters from T ) 288.15 K to T ) 358.15 K
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 7. Activity Coefficients of Aliphatic and Aromatic Esters and Benzylamine in 1-Methyl-3-ethylimidazolium Bis(trifluoromethylsulfonyl) Imide Using the Transpiration Method
- Densities and Viscosities of Binary Mixtures of Isoamyl Acetate, Ethyl Caproate, Ethyl Benzoate, Isoamyl Butyrate, Ethyl Phenylacetate, and Ethyl Caprylate with Ethanol at T = (288.15, 298.15, 308.15, and 318.15) K
- Refractive Indices and Surface Tensions of Binary Mixtures of Isoamyl Acetate, Ethyl Caproate, Ethyl Benzoate, Isoamyl Butyrate, Ethyl Phenylacetate, and Ethyl Caprylate with Ethanol at (288.15, 298.15, 308.15, and 318.15) K
- Critical Point Measurements for n-Alkyl Benzoates (C8 to C13)
- Limiting Diffusion Coefficients of Ethyl Benzoate, Benzylacetone, and Eugenol in Carbon Dioxide at Supercritical Conditions
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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