Chemical Properties of Benzoic acid, methyl ester (CAS 93-58-3)

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).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• EA : Electron affinity (eV).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced pressure (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

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. Solubility Prediction
log10WS	-1.85		Estimated Solubility
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	Critical Point Measurements for n-Alkyl Benzoates (C8 to C13)
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. Solubility Prediction
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]
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]
η	0.0022970	Pa×s	288.15	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
η	0.0019180	Pa×s	298.15	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
η	0.0018510	Pa×s	298.15	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
η	0.0016670	Pa×s	303.15	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
η	0.0017780	Pa×s	303.15	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
η	0.0016790	Pa×s	303.15	Thermophysical Properties of Isoamyl Acetate or Methyl Benzoate + Hydrocarbon Binary Mixtures, at (303.15 and 313.15) K
η	0.0016630	Pa×s	308.15	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
η	0.0015310	Pa×s	308.15	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
η	0.0015140	Pa×s	308.15	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
η	0.0014020	Pa×s	313.15	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
η	0.0014140	Pa×s	313.15	Thermophysical Properties of Isoamyl Acetate or Methyl Benzoate + Hydrocarbon Binary Mixtures, at (303.15 and 313.15) K
η	0.0013760	Pa×s	313.15	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
η	0.0012970	Pa×s	318.15	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
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]
ΔvapH	57.20 ± 0.10	kJ/mol	303.00	NIST
ΔvapH	50.70	kJ/mol	381.00	NIST
ΔvapH	48.30	kJ/mol	381.00	NIST
ΔvapH	52.80	kJ/mol	387.00	NIST
ΔvapH	51.10 ± 0.20	kJ/mol	437.50	NIST
ΔvapH	48.50 ± 0.20	kJ/mol	437.50	NIST
ΔvapH	45.80 ± 0.20	kJ/mol	437.50	NIST
ΔvapH	43.00 ± 0.40	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	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
ρl	1077.00	kg/m3	303.15	Study of molecular interactions in the mixtures of some primary alcohols with equimolar mixture of 1-propanol and alkylbenzoates at T = 303.15 K
γ	[0.03; 0.04]	N/m	[288.15; 358.15]
γ	0.04	N/m	288.15	Densities, Viscosities, Refractive Indices, and Surface Tensions for 12 Flavor Esters from T ) 288.15 K to T ) 358.15 K
γ	0.04	N/m	298.15	Densities, Viscosities, Refractive Indices, and Surface Tensions for 12 Flavor Esters from T ) 288.15 K to T ) 358.15 K
γ	0.04	N/m	308.15	Densities, Viscosities, Refractive Indices, and Surface Tensions for 12 Flavor Esters from T ) 288.15 K to T ) 358.15 K
γ	0.03	N/m	318.15	Densities, Viscosities, Refractive Indices, and Surface Tensions for 12 Flavor Esters from T ) 288.15 K to T ) 358.15 K
γ	0.03	N/m	328.15	Densities, Viscosities, Refractive Indices, and Surface Tensions for 12 Flavor Esters from T ) 288.15 K to T ) 358.15 K
γ	0.03	N/m	338.15	Densities, Viscosities, Refractive Indices, and Surface Tensions for 12 Flavor Esters from T ) 288.15 K to T ) 358.15 K
γ	0.03	N/m	348.15	Densities, Viscosities, Refractive Indices, and Surface Tensions for 12 Flavor Esters from T ) 288.15 K to T ) 358.15 K
γ	0.03	N/m	358.15	Densities, Viscosities, Refractive Indices, and Surface Tensions for 12 Flavor Esters from T ) 288.15 K to T ) 358.15 K

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 Yaws Handbook of Vapor Pressure
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
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 Vapor Pressure Data
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
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
• Cheméo Relay (1.0)
• 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

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.
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