Chemical Properties of Benzoic acid, ethyl ester (CAS 93-89-0)

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.
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (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.
• NFPA Health : NFPA Health 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).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.4800		KDB
ΔfG°	-96.61	kJ/mol	Joback Calculated Property
ΔfH°gas	-303.65	kJ/mol	Relay (1.0) 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. Solubility Prediction
log10WS	-2.32		Estimated Solubility
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	Critical Point Measurements for n-Alkyl Benzoates (C8 to C13)
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	0.447	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[256.39; 321.72]	J/mol×K	[508.29; 724.46]
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]
η	0.0024440	Pa×s	288.15	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
η	0.0019710	Pa×s	298.15	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
η	0.0017480	Pa×s	303.15	Viscosity, Density, and Refractive Index of Some (Ester + Hydrocarbon) Binary Mixtures at 303.15 K and 313.15 K
η	0.0016240	Pa×s	308.15	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
η	0.0014380	Pa×s	313.15	Viscosity, Density, and Refractive Index of Some (Ester + Hydrocarbon) Binary Mixtures at 303.15 K and 313.15 K
η	0.0013680	Pa×s	318.15	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
ΔvapH	[43.60; 57.00]	kJ/mol	[310.50; 450.00]
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	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
ΔvapH	43.60 ± 0.50	kJ/mol	450.00	NIST
Pvap	[7.10e-03; 0.29]	kPa	[283.90; 332.50]
Pvap	7.10e-03	kPa	283.90	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
Pvap	9.30e-03	kPa	286.90	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
Pvap	0.01	kPa	289.00	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
Pvap	0.01	kPa	292.00	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
Pvap	0.02	kPa	294.10	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
Pvap	0.02	kPa	295.00	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
Pvap	0.02	kPa	298.10	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
Pvap	0.03	kPa	299.10	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
Pvap	0.03	kPa	301.20	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
Pvap	0.04	kPa	304.20	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
Pvap	0.05	kPa	307.20	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
Pvap	0.06	kPa	310.10	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
Pvap	0.07	kPa	312.30	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
Pvap	0.09	kPa	315.30	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
Pvap	0.11	kPa	317.30	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
Pvap	0.13	kPa	320.30	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
Pvap	0.17	kPa	323.40	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
Pvap	0.20	kPa	326.40	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
Pvap	0.25	kPa	329.50	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
Pvap	0.29	kPa	332.50	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
ρl	[1041.30; 1046.00]	kg/m3	[293.00; 303.15]
ρl	1046.00	kg/m3	293.00	KDB
ρl	1041.30	kg/m3	298.15	Excess Molar Entalpies of Dimethyl Carbonate with o-Xylene, m-Xylene, p-Xylene, Ethylbenzene, or Ethyl Benzoate at 298.15 K
ρl	1041.30	kg/m3	298.15	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
ρl	1041.42	kg/m3	298.15	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
ρl	1042.00	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	0.03	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	0.03	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	[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 Yaws Handbook of Vapor Pressure
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
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 Vapor Pressure Data
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
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
• Cheméo Relay (1.0)
• 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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