- InChI
- InChI=1S/C8H8O2/c1-10-8(9)7-5-3-2-4-6-7/h2-6H,1H3
- InChI Key
- QPJVMBTYPHYUOC-UHFFFAOYSA-N
- Formula
- C8H8O2
- SMILES
- COC(=O)c1ccccc1
- Molecular Weight1
- 136.15
- CAS
- 93-58-3
- Other Names
-
- CLORIUS
- Essence of niobe
- METHYL BENZENECARBOXYLATE
- Methyl benzoate
- Methyl ester of benzoic acid
- Methylester kyseliny benzoove
- NSC 9394
- Niobe oil
- Oil of Niobe
- Oniobe oil
- Oxidate le
- UN 2938
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- EA : Electron affinity (eV).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase 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).
- 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.
- 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).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.4300 | KDB | |
| PAff | 850.50 | kJ/mol | NIST |
| BasG | [814.90; 819.50] | kJ/mol |
|
| BasG | 819.50 | kJ/mol | NIST |
| BasG | 814.90 ± 0.50 | kJ/mol | NIST |
| ΔcH°liquid | -3947.90 ± 2.40 | kJ/mol | NIST |
| μ | 1.90 | debye | KDB |
| EA | 0.18 | eV | NIST |
| ΔfG° | -105.03 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-299.80; -254.10] | kJ/mol |
|
| ΔfH°gas | -254.10 | kJ/mol | KDB |
| ΔfH°gas | -269.30 ± 5.10 | kJ/mol | NIST |
| ΔfH°gas | -299.80 | kJ/mol | NIST |
| ΔfH°liquid | [-343.50; -324.30] | kJ/mol |
|
| ΔfH°liquid | -324.30 ± 3.00 | kJ/mol | NIST |
| ΔfH°liquid | -343.50 | kJ/mol | NIST |
| ΔfusH° | 13.30 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [43.70; 55.60] | kJ/mol |
|
| ΔvapH° | 53.40 | kJ/mol | NIST |
| ΔvapH° | 53.80 | kJ/mol | NIST |
| ΔvapH° | 54.70 | kJ/mol | NIST |
| ΔvapH° | 53.90 | kJ/mol | NIST |
| ΔvapH° | 55.00 | kJ/mol | NIST |
| ΔvapH° | 55.60 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 43.72 | kJ/mol | NIST |
| ΔvapH° | 43.70 | kJ/mol | NIST |
| ΔvapH° | 55.57 ± 0.04 | kJ/mol | NIST |
| IE | [9.28; 9.79] | eV |
|
| IE | 9.32 ± 0.04 | eV | NIST |
| IE | 9.32 ± 0.03 | eV | NIST |
| IE | 9.48 | eV | NIST |
| IE | 9.28 | eV | NIST |
| IE | 9.40 ± 0.10 | eV | NIST |
| IE | 9.49 | eV | NIST |
| IE | 9.35 ± 0.03 | eV | NIST |
| IE | 9.40 ± 0.03 | eV | NIST |
| IE | 9.35 ± 0.06 | eV | NIST |
| IE | Outlier 9.79 | eV | NIST |
| IE | 9.50 | eV | NIST |
| IE | 9.34 | eV | NIST |
| log10WS | [-1.85; -1.85] |
|
|
| log10WS | -1.85 | Aq. Sol... | |
| log10WS | -1.85 | Estimat... | |
| logPoct/wat | 1.473 | Crippen Calculated Property | |
| McVol | 107.260 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| Pc | [3460.00; 3640.00] | kPa |
|
| Pc | 3640.00 | kPa | KDB |
| Pc | 3460.00 | kPa | Critica... |
| Inp | [183.27; 1130.00] |
|
|
| Inp | 1077.80 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1100.00 | NIST | |
| Inp | 1101.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1101.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1087.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1109.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1106.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1102.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1065.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1061.40 | NIST | |
| Inp | 1100.00 | NIST | |
| Inp | 1105.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1075.80 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1092.46 | NIST | |
| Inp | 1096.30 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1065.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1102.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1103.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1082.00 | NIST | |
| Inp | 1082.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1130.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1098.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1107.00 | NIST | |
| Inp | 1107.00 | NIST | |
| Inp | 1094.60 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1105.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1106.00 | NIST | |
| Inp | 1065.00 | NIST | |
| Inp | 1065.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1100.00 | NIST | |
| Inp | 1103.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1105.00 | NIST | |
| Inp | 1111.00 | NIST | |
| Inp | 1103.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1099.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1103.00 | NIST | |
| Inp | 1086.00 | NIST | |
| Inp | 1077.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1087.00 | NIST | |
| Inp | Outlier 183.27 | NIST | |
| Inp | 1103.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1100.00 | NIST | |
| Inp | 1092.46 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1074.00 | NIST | |
| I | [1573.00; 1661.00] |
|
|
| I | Outlier 1661.00 | NIST | |
| I | 1643.00 | NIST | |
| I | Outlier 1657.00 | NIST | |
| I | 1589.00 | NIST | |
| I | 1640.00 | NIST | |
| I | 1608.00 | NIST | |
| I | 1586.00 | NIST | |
| I | 1600.00 | NIST | |
| I | 1573.00 | NIST | |
| I | 1574.00 | NIST | |
| I | 1631.00 | NIST | |
| I | 1596.00 | NIST | |
| I | 1600.00 | NIST | |
| I | 1605.00 | NIST | |
| I | Outlier 1657.00 | NIST | |
| I | 1614.00 | NIST | |
| I | 1602.00 | NIST | |
| I | 1614.00 | NIST | |
| I | 1604.00 | NIST | |
| I | 1607.00 | NIST | |
| I | 1650.00 | NIST | |
| I | 1602.00 | NIST | |
| I | 1654.00 | NIST | |
| I | 1634.00 | NIST | |
| I | 1607.00 | NIST | |
| I | 1632.00 | NIST | |
| I | 1590.00 | NIST | |
| I | 1600.00 | NIST | |
| I | 1595.00 | NIST | |
| I | 1598.00 | NIST | |
| I | 1608.00 | NIST | |
| I | 1612.00 | NIST | |
| I | 1632.00 | NIST | |
| I | 1627.00 | NIST | |
| I | 1607.00 | NIST | |
| I | 1631.00 | NIST | |
| I | 1628.00 | NIST | |
| I | 1602.00 | NIST | |
| I | 1641.00 | NIST | |
| I | 1624.00 | NIST | |
| I | 1616.00 | NIST | |
| I | 1641.00 | NIST | |
| I | 1615.00 | NIST | |
| I | 1617.00 | NIST | |
| I | 1591.00 | NIST | |
| I | 1603.00 | NIST | |
| I | 1591.00 | NIST | |
| I | 1615.00 | NIST | |
| I | 1636.00 | NIST | |
| I | 1613.00 | NIST | |
| I | 1635.00 | NIST | |
| I | 1611.00 | NIST | |
| I | 1617.00 | NIST | |
| I | 1575.00 | NIST | |
| I | 1623.00 | NIST | |
| I | 1632.00 | NIST | |
| I | 1632.00 | NIST | |
| I | 1595.00 | NIST | |
| I | 1600.00 | NIST | |
| I | 1605.00 | NIST | |
| I | 1631.00 | NIST | |
| I | 1582.00 | NIST | |
| I | 1594.00 | NIST | |
| I | 1611.00 | NIST | |
| I | 1633.00 | NIST | |
| I | 1628.00 | NIST | |
| I | 1595.00 | NIST | |
| I | 1580.00 | NIST | |
| I | 1619.00 | NIST | |
| I | 1638.00 | NIST | |
| I | 1590.00 | NIST | |
| I | 1600.00 | NIST | |
| I | 1641.00 | NIST | |
| I | 1614.00 | NIST | |
| I | 1616.00 | NIST | |
| I | 1600.00 | NIST | |
| I | 1628.00 | NIST | |
| I | 1590.00 | NIST | |
| I | 1600.00 | NIST | |
| I | 1589.00 | NIST | |
| I | 1573.00 | NIST | |
| I | Outlier 1661.00 | NIST | |
| I | 1624.00 | NIST | |
| I | 1591.00 | NIST | |
| I | 1613.00 | NIST | |
| I | 1623.00 | NIST | |
| I | 1605.00 | NIST | |
| I | 1633.00 | NIST | |
| Tboil | 472.20 | K | KDB |
| Tc | 692.00 | K | KDB |
| Tfus | [260.40; 260.94] | K |
|
| Tfus | 260.80 | K | KDB |
| Tfus | Outlier 260.40 | K | Aq. Sol... |
| Tfus | 260.80 | K | NIST |
| Tfus | 260.70 ± 0.20 | K | NIST |
| Tfus | 260.80 ± 0.02 | K | NIST |
| Tfus | 260.94 ± 0.05 | K | NIST |
| Tfus | 260.75 ± 0.30 | K | NIST |
| Vc | 0.396 | m3/kmol | KDB |
| Zc | 0.2505270 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [214.26; 273.64] | J/mol×K | [485.41; 705.10] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 210 220 230 240 250 260 270 500 600 700 | ||||
| Cp,gas | 214.26 | J/mol×K | 485.41 | Joback Calculated Property |
| Cp,gas | 225.73 | J/mol×K | 522.02 | Joback Calculated Property |
| Cp,gas | 236.56 | J/mol×K | 558.64 | Joback Calculated Property |
| Cp,gas | 246.75 | J/mol×K | 595.25 | Joback Calculated Property |
| Cp,gas | 256.31 | J/mol×K | 631.87 | Joback Calculated Property |
| Cp,gas | 265.28 | J/mol×K | 668.48 | Joback Calculated Property |
| Cp,gas | 273.64 | J/mol×K | 705.10 | Joback Calculated Property |
| Cp,liquid | [216.50; 221.30] | J/mol×K | [297.00; 298.15] |
|
| Cp,liquid | 216.50 | J/mol×K | 297.00 | NIST |
| Cp,liquid | 221.30 | J/mol×K | 298.15 | NIST |
| η | [0.0012970; 0.0022970] | Pa×s | [288.15; 318.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 1.20e-3 1.40e-3 1.60e-3 1.80e-3 2.00e-3 2.20e-3 290 300 310 | ||||
| η | 0.0022970 | Pa×s | 288.15 | Densiti... |
| η | 0.0019180 | Pa×s | 298.15 | Density... |
| η | 0.0018510 | Pa×s | 298.15 | Densiti... |
| η | 0.0017780 | Pa×s | 303.15 | Density... |
| η | 0.0016790 | Pa×s | 303.15 | Thermop... |
| η | 0.0016670 | Pa×s | 303.15 | Density... |
| η | 0.0015310 | Pa×s | 308.15 | Densiti... |
| η | 0.0015140 | Pa×s | 308.15 | Density... |
| η | 0.0016630 | Pa×s | 308.15 | Density... |
| η | 0.0014140 | Pa×s | 313.15 | Thermop... |
| η | 0.0014020 | Pa×s | 313.15 | Density... |
| η | 0.0013760 | Pa×s | 313.15 | Density... |
| η | 0.0012970 | Pa×s | 318.15 | Densiti... |
| ΔfusH | [13.90; 14.83] | kJ/mol | [162.50; 261.00] |
|
| ΔfusH | 14.80 | kJ/mol | 162.50 | NIST |
| ΔfusH | 14.83 | kJ/mol | 260.80 | NIST |
| ΔfusH | 13.90 | kJ/mol | 261.00 | NIST |
| ΔfusH | 13.90 | kJ/mol | 261.00 | NIST |
| ΔvapH | [43.00; 57.20] | kJ/mol | [303.00; 453.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 45 50 55 300 350 400 450 | ||||
| ΔvapH | 57.20 ± 0.10 | kJ/mol | 303.00 | NIST |
| ΔvapH | 48.30 | kJ/mol | 381.00 | NIST |
| ΔvapH | 50.70 | kJ/mol | 381.00 | NIST |
| ΔvapH | 52.80 | kJ/mol | 387.00 | NIST |
| ΔvapH | 48.50 ± 0.20 | kJ/mol | 437.50 | NIST |
| ΔvapH | 43.00 ± 0.40 | kJ/mol | 437.50 | NIST |
| ΔvapH | 51.10 ± 0.20 | kJ/mol | 437.50 | NIST |
| ΔvapH | 45.80 ± 0.20 | kJ/mol | 437.50 | NIST |
| ΔvapH | 49.70 | kJ/mol | 453.00 | NIST |
| ρl | [1077.00; 1086.00] | kg/m3 | [293.00; 303.15] |
|
| ρl | 1086.00 | kg/m3 | 293.00 | KDB |
| ρl | 1083.92 | kg/m3 | 298.15 | Refract... |
| ρl | 1077.00 | 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 0.04 0.04 300 320 340 | ||||
| γ | 0.04 | N/m | 288.15 | Densiti... |
| γ | 0.04 | N/m | 298.15 | Densiti... |
| γ | 0.04 | 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 | [370.00; 370.20] | K | [3.20; 3.20] |
|
| Tboilr | 370.20 | K | 3.20 | NIST |
| Tboilr | 370.00 ± 1.00 | K | 3.20 | NIST |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 278.15 | 100.00 | 1101.5 |
| 278.15 | 1000.00 | 1102.1 |
| 278.15 | 5000.00 | 1104.4 |
| 278.15 | 10000.00 | 1107.2 |
| 278.15 | 15000.00 | 1109.9 |
| 278.15 | 20000.00 | 1112.6 |
| 278.15 | 25000.00 | 1115.2 |
| 278.15 | 30000.00 | 1117.7 |
| 278.15 | 35000.00 | 1120.2 |
| 278.15 | 40000.00 | 1122.7 |
| 278.15 | 45000.00 | 1125.1 |
| 278.15 | 50000.00 | 1127.4 |
| 278.15 | 55000.00 | 1129.7 |
| 278.15 | 60000.00 | 1131.8 |
| 288.15 | 100.00 | 1092.1 |
| 288.15 | 1000.00 | 1092.6 |
| 288.15 | 5000.00 | 1095.0 |
| 288.15 | 10000.00 | 1097.9 |
| 288.15 | 15000.00 | 1100.8 |
| 288.15 | 20000.00 | 1103.6 |
| 288.15 | 25000.00 | 1106.3 |
| 288.15 | 30000.00 | 1109.0 |
| 288.15 | 35000.00 | 1111.6 |
| 288.15 | 40000.00 | 1114.1 |
| 288.15 | 45000.00 | 1116.6 |
| 288.15 | 50000.00 | 1119.1 |
| 288.15 | 55000.00 | 1121.4 |
| 288.15 | 60000.00 | 1123.6 |
| 298.15 | 100.00 | 1082.7 |
| 298.15 | 1000.00 | 1083.2 |
| 298.15 | 5000.00 | 1085.8 |
| 298.15 | 10000.00 | 1089.0 |
| 298.15 | 15000.00 | 1091.8 |
| 298.15 | 20000.00 | 1094.8 |
| 298.15 | 25000.00 | 1097.6 |
| 298.15 | 30000.00 | 1100.4 |
| 298.15 | 35000.00 | 1103.1 |
| 298.15 | 40000.00 | 1105.7 |
| 298.15 | 45000.00 | 1108.3 |
| 298.15 | 50000.00 | 1110.9 |
| 298.15 | 55000.00 | 1113.4 |
| 298.15 | 60000.00 | 1115.6 |
| 308.15 | 100.00 | 1073.0 |
| 308.15 | 1000.00 | 1073.6 |
| 308.15 | 5000.00 | 1076.2 |
| 308.15 | 10000.00 | 1079.5 |
| 308.15 | 15000.00 | 1082.6 |
| 308.15 | 20000.00 | 1085.7 |
| 308.15 | 25000.00 | 1088.6 |
| 308.15 | 30000.00 | 1091.5 |
| 308.15 | 35000.00 | 1094.3 |
| 308.15 | 40000.00 | 1097.1 |
| 308.15 | 45000.00 | 1099.8 |
| 308.15 | 50000.00 | 1102.4 |
| 308.15 | 55000.00 | 1105.0 |
| 308.15 | 60000.00 | 1107.4 |
| 318.15 | 100.00 | 1063.3 |
| 318.15 | 1000.00 | 1063.8 |
| 318.15 | 5000.00 | 1066.7 |
| 318.15 | 10000.00 | 1070.1 |
| 318.15 | 15000.00 | 1073.4 |
| 318.15 | 20000.00 | 1076.6 |
| 318.15 | 25000.00 | 1079.7 |
| 318.15 | 30000.00 | 1082.8 |
| 318.15 | 35000.00 | 1085.7 |
| 318.15 | 40000.00 | 1088.6 |
| 318.15 | 45000.00 | 1091.4 |
| 318.15 | 50000.00 | 1094.1 |
| 318.15 | 55000.00 | 1096.8 |
| 318.15 | 60000.00 | 1099.3 |
| 328.15 | 100.00 | 1053.6 |
| 328.15 | 1000.00 | 1054.3 |
| 328.15 | 5000.00 | 1057.2 |
| 328.15 | 10000.00 | 1060.8 |
| 328.15 | 15000.00 | 1064.3 |
| 328.15 | 20000.00 | 1067.6 |
| 328.15 | 25000.00 | 1070.9 |
| 328.15 | 30000.00 | 1074.0 |
| 328.15 | 35000.00 | 1077.1 |
| 328.15 | 40000.00 | 1080.1 |
| 328.15 | 45000.00 | 1083.0 |
| 328.15 | 50000.00 | 1085.9 |
| 328.15 | 55000.00 | 1088.7 |
| 328.15 | 60000.00 | 1091.2 |
| 338.15 | 100.00 | 1044.1 |
| 338.15 | 1000.00 | 1044.8 |
| 338.15 | 5000.00 | 1048.0 |
| 338.15 | 10000.00 | 1051.7 |
| 338.15 | 15000.00 | 1055.3 |
| 338.15 | 20000.00 | 1058.8 |
| 338.15 | 25000.00 | 1062.2 |
| 338.15 | 30000.00 | 1065.5 |
| 338.15 | 35000.00 | 1068.8 |
| 338.15 | 40000.00 | 1071.9 |
| 338.15 | 45000.00 | 1074.9 |
| 338.15 | 50000.00 | 1077.9 |
| 338.15 | 55000.00 | 1080.8 |
| 338.15 | 60000.00 | 1083.5 |
| 348.15 | 100.00 | 1034.4 |
| 348.15 | 1000.00 | 1035.1 |
| 348.15 | 5000.00 | 1038.4 |
| 348.15 | 10000.00 | 1042.4 |
| 348.15 | 15000.00 | 1046.2 |
| 348.15 | 20000.00 | 1049.8 |
| 348.15 | 25000.00 | 1053.4 |
| 348.15 | 30000.00 | 1056.9 |
| 348.15 | 35000.00 | 1060.3 |
| 348.15 | 40000.00 | 1063.5 |
| 348.15 | 45000.00 | 1066.7 |
| 348.15 | 50000.00 | 1069.8 |
| 348.15 | 55000.00 | 1072.8 |
| 348.15 | 60000.00 | 1075.5 |
| 358.15 | 100.00 | 1024.9 |
| 358.15 | 1000.00 | 1025.6 |
| 358.15 | 5000.00 | 1029.1 |
| 358.15 | 10000.00 | 1033.3 |
| 358.15 | 15000.00 | 1037.3 |
| 358.15 | 20000.00 | 1041.2 |
| 358.15 | 25000.00 | 1044.9 |
| 358.15 | 30000.00 | 1048.5 |
| 358.15 | 35000.00 | 1052.0 |
| 358.15 | 40000.00 | 1055.4 |
| 358.15 | 45000.00 | 1058.7 |
| 358.15 | 50000.00 | 1061.9 |
| 358.15 | 55000.00 | 1065.1 |
| 358.15 | 60000.00 | 1067.9 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [350.33; 502.55] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.48415e+01 | |||
| Coefficient B | -4.20259e+03 | |||
| Coefficient C | -6.15670e+01 | |||
| Temperature range, min. | 350.33 | |||
| Temperature range, max. | 502.55 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 500 | ||||
| Pvap | 1.33 | kPa | 350.33 | Calculated Property |
| Pvap | 2.98 | kPa | 367.24 | Calculated Property |
| Pvap | 6.13 | kPa | 384.16 | Calculated Property |
| Pvap | 11.74 | kPa | 401.07 | Calculated Property |
| Pvap | 21.12 | kPa | 417.98 | Calculated Property |
| Pvap | 36.04 | kPa | 434.90 | Calculated Property |
| Pvap | 58.70 | kPa | 451.81 | Calculated Property |
| Pvap | 91.81 | kPa | 468.72 | Calculated Property |
| Pvap | 138.57 | kPa | 485.64 | Calculated Property |
| Pvap | 202.65 | kPa | 502.55 | Calculated Property |
| Pvap | [1.84e-03; 3484.87] | kPa | [260.75; 693.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.04360e+02 | |||
| Coefficient B | -1.02686e+04 | |||
| Coefficient C | -1.28853e+01 | |||
| Coefficient D | 6.03145e-06 | |||
| Temperature range, min. | 260.75 | |||
| Temperature range, max. | 693.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 400 600 | ||||
| Pvap | 1.84e-03 | kPa | 260.75 | Calculated Property |
| Pvap | 0.11 | kPa | 308.78 | Calculated Property |
| Pvap | 1.86 | kPa | 356.81 | Calculated Property |
| Pvap | 13.83 | kPa | 404.83 | Calculated Property |
| Pvap | 61.63 | kPa | 452.86 | Calculated Property |
| Pvap | 194.96 | kPa | 500.89 | Calculated Property |
| Pvap | 488.25 | kPa | 548.92 | Calculated Property |
| Pvap | 1040.10 | kPa | 596.94 | Calculated Property |
| Pvap | 1979.63 | kPa | 644.97 | Calculated Property |
| Pvap | 3484.87 | kPa | 693.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzoic acid, methyl ester.
Mixtures
- Benzoic acid, methyl ester + 1-Hexanol
- Benzoic acid, methyl ester + Cyclohexane
- 1-Propanol + Benzoic acid, methyl ester + 1-Butanol
- 1-Propanol + Benzoic acid, methyl ester + 1-Pentanol
- 1-Propanol + Benzoic acid, methyl ester
- Benzoic acid, methyl ester + Formamide, N,N-dimethyl-
- Benzoic acid, methyl ester + Ethanol
- Benzoic acid, methyl ester + o-Xylene
- Benzoic acid, methyl ester + Benzene, 1,3-dimethyl-
- p-Xylene + Benzoic acid, methyl ester
- Benzoic acid, methyl ester + Ethylbenzene
- Butane + Benzoic acid, methyl ester
- Benzoic acid, methyl ester + Pentane
- n-Hexane + Benzoic acid, methyl ester
- Benzoic acid, methyl ester + Heptane
- Benzoic acid, methyl ester + Octane
- Carbon dioxide + Benzoic acid, methyl ester
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Compressed liquid density measurements for {methylbenzoate + (cyclohexane or 1-hexanol)} binary systems
- Study of molecular interactions in the mixtures of some primary alcohols with equimolar mixture of 1-propanol and alkylbenzoates at T = 303.15 K
- Solubilities of CO2 capture absorbents methyl benzoate, ethyl hexanoate and methyl heptanoate
- Below the room temperature measurements of solubilities in ester absorbents for CO2 capture
- Density and Viscosity Studies of Binary Mixtures of N,N-Dimethylformamide with Toluene and Methyl Benzoate at (298.15, 303.15, 308.15, 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
- Densities and Viscosities of Binary Mixtures of Ethyl Acetoacetate, Ethyl Isovalerate, Methyl Benzoate, Benzyl Acetate, Ethyl Salicylate, and Benzyl Propionate with Ethanol at T ) (288.15, 298.15, 308.15, and 318.15) K
- Refractive Indices and Surface Tensions of Binary Mixtures of Ethyl Acetoacetate, Ethyl Isovalerate, Methyl Benzoate, Benzyl Acetate, Ethyl Salicylate, and Benzyl Propionate with Ethanol at (288.15, 298.15, 308.15, and 318.15) K
- Critical Point Measurements for n-Alkyl Benzoates (C8 to C13)
- Thermophysical Properties of Isoamyl Acetate or Methyl Benzoate + Hydrocarbon Binary Mixtures, at (303.15 and 313.15) K
- In Situ Determination of Phase Equilibria of Methyl Benzoate + Alkane Mixtures Using an Infrared Absorption Method. Comparison with Polar GC-SAFT Predictions
- Density, Viscosity, and Speed of Sound of (Methyl Benzoate + Cyclohexane), (Methyl Benzoate + n-Hexane), (Methyl Benzoate + Heptane), and (Methyl Benzoate + Octane) at Temperatures of (303.15, 308.15, and 313.15) K
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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