Chemical Properties of Propanoic acid, ethyl ester (CAS 105-37-3)

InChI

InChI=1S/C5H10O2/c1-3-5(6)7-4-2/h3-4H2,1-2H3

InChI Key

FKRCODPIKNYEAC-UHFFFAOYSA-N

Formula

C5H10O2

SMILES

CCOC(=O)CC

Molecular Weight¹

102.13

CAS

105-37-3

Other Names

• C2H5COOC2H5
• ETHYL ESTER PROPIONIC ACID
• Ethyl ester of propanoic acid
• Ethyl n-propionate
• Ethyl propanoate
• Ethyl propionate
• Ethylester kyseliny propionove
• NSC 8848
• Propionate d'ethyle
• Propionic acid, ethyl ester
• Propionic ester
• Propionic ether
• UN 1195
• n-Ethyl propanoate

• ω : Acentric Factor.
• 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).
• 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_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).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ : Liquid thermal conductivity (W/m×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	0.3910		KDB
ΔcH°liquid	[-2912.10; -2888.00]	kJ/mol
ΔcH°liquid	-2894.00 ± 0.65	kJ/mol	NIST
ΔcH°liquid	-2888.00	kJ/mol	NIST
ΔcH°liquid	-2912.10 ± 2.00	kJ/mol	NIST
μ	1.80	debye	KDB
ΔfG°	-323.70	kJ/mol	KDB
ΔfH°gas	[-470.20; -463.60]	kJ/mol
ΔfH°gas	-470.20	kJ/mol	KDB
ΔfH°gas	-466.50 ± 0.40	kJ/mol	NIST
ΔfH°gas	-463.60 ± 0.70	kJ/mol	NIST
ΔfH°liquid	[-505.59; -502.70]	kJ/mol
ΔfH°liquid	-505.59 ± 0.50	kJ/mol	NIST
ΔfH°liquid	-502.70 ± 0.70	kJ/mol	NIST
ΔfusH°	11.49	kJ/mol	Joback Calculated Property
ΔvapH°	36.60	kJ/mol	Relay (1.0) Calculated Property
IE	10.00 ± 0.02	eV	NIST
log10WS	[-0.66; -0.66]
log10WS	-0.66		Aq. Solubility Prediction
log10WS	-0.66		Estimated Solubility
logPoct/wat	0.959		Crippen Calculated Property
McVol	88.750	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
Pc	[3359.70; 3510.00]	kPa
Pc	3362.00	kPa	KDB
Pc	3385.60	kPa	Development of a Predictive Equation of State for CO2 + Ethyl Ester Mixtures Based on Critical Points Measurements
Pc	3362.00 ± 81.06	kPa	NIST
Pc	3359.70 ± 40.00	kPa	NIST
Pc	3510.00 ± 202.65	kPa	NIST
Pc	3510.00 ± 202.65	kPa	NIST
ρc	[285.97; 296.90]	kg/m3
ρc	296.49 ± 10.01	kg/m3	NIST
ρc	296.90 ± 4.09	kg/m3	NIST
ρc	285.97 ± 10.01	kg/m3	NIST
ρc	285.97 ± 10.01	kg/m3	NIST
Inp	[651.00; 733.00]
Inp	694.20		NIST
Inp	678.95		NIST
Inp	700.00		NIST
Inp	678.00		NIST
Inp	692.00		NIST
Inp	684.00		NIST
Inp	688.00		NIST
Inp	695.00		NIST
Inp	707.00		NIST
Inp	685.00		NIST
Inp	694.00		NIST
Inp	691.00		NIST
Inp	694.00		NIST
Inp	692.00		NIST
Inp	704.00		NIST
Inp	695.00		NIST
Inp	679.00		NIST
Inp	Outlier 668.00		NIST
Inp	693.00		NIST
Inp	692.00		NIST
Inp	693.00		NIST
Inp	694.00		NIST
Inp	699.00		NIST
Inp	700.00		NIST
Inp	685.00		NIST
Inp	706.00		NIST
Inp	692.00		NIST
Inp	709.00		NIST
Inp	706.00		NIST
Inp	704.00		NIST
Inp	714.00		NIST
Inp	709.00		NIST
Inp	711.00		NIST
Inp	705.00		NIST
Inp	680.00		NIST
Inp	681.00		NIST
Inp	714.00		NIST
Inp	696.00		NIST
Inp	681.00		NIST
Inp	681.00		NIST
Inp	711.00		NIST
Inp	691.00		NIST
Inp	712.00		NIST
Inp	700.00		NIST
Inp	708.00		NIST
Inp	726.00		NIST
Inp	712.00		NIST
Inp	726.00		NIST
Inp	725.00		NIST
Inp	698.00		NIST
Inp	708.00		NIST
Inp	714.00		NIST
Inp	714.00		NIST
Inp	710.00		NIST
Inp	714.00		NIST
Inp	702.00		NIST
Inp	Outlier 651.00		NIST
Inp	714.00		NIST
Inp	690.00		NIST
Inp	Outlier 729.00		NIST
Inp	705.00		NIST
Inp	683.00		NIST
Inp	705.00		NIST
Inp	714.00		NIST
Inp	705.00		NIST
Inp	717.20		NIST
Inp	712.00		NIST
Inp	695.00		NIST
Inp	703.00		NIST
Inp	703.00		NIST
Inp	705.00		NIST
Inp	691.00		NIST
Inp	709.00		NIST
Inp	691.00		NIST
Inp	691.00		NIST
Inp	695.00		NIST
Inp	Outlier 657.00		NIST
Inp	700.00		NIST
Inp	726.00		NIST
Inp	Outlier 733.00		NIST
Inp	699.00		NIST
Inp	714.00		NIST
Inp	714.00		NIST
Inp	710.00		NIST
Inp	712.00		NIST
Inp	711.00		NIST
Inp	709.00		NIST
Inp	708.00		NIST
Inp	692.00		NIST
Inp	707.00		NIST
Inp	692.00		NIST
Inp	708.00		NIST
Inp	708.00		NIST
Inp	703.00		NIST
Inp	705.00		NIST
Inp	714.00		NIST
Inp	691.00		NIST
Inp	709.00		NIST
Inp	705.00		NIST
Inp	709.00		NIST
Inp	709.00		NIST
Inp	709.00		NIST
Inp	692.00		NIST
Inp	Outlier 663.00		NIST
Inp	694.00		NIST
Inp	693.00		NIST
Inp	695.00		NIST
Inp	714.00		NIST
Inp	715.00		NIST
Inp	695.00		NIST
Inp	679.00		NIST
Inp	692.00		NIST
Inp	693.00		NIST
Inp	691.00		NIST
Inp	691.00		NIST
Inp	691.00		NIST
Inp	679.00		NIST
Inp	692.00		NIST
Inp	708.00		NIST
Inp	698.00		NIST
Inp	714.00		NIST
Inp	726.00		NIST
Inp	710.00		NIST
Inp	703.00		NIST
Inp	705.00		NIST
Inp	Outlier 663.00		NIST
Inp	715.00		NIST
Inp	691.00		NIST
Inp	694.20		NIST
Inp	684.00		NIST
Inp	694.00		NIST
Inp	695.00		NIST
Inp	702.00		NIST
I	[910.00; 977.00]
I	977.00		NIST
I	957.00		NIST
I	954.00		NIST
I	Outlier 910.00		NIST
I	949.00		NIST
I	970.00		NIST
I	936.00		NIST
I	977.00		NIST
I	955.00		NIST
I	966.00		NIST
I	966.00		NIST
I	951.00		NIST
I	946.00		NIST
I	953.00		NIST
I	955.00		NIST
I	976.00		NIST
I	957.00		NIST
I	939.00		NIST
I	947.00		NIST
I	922.00		NIST
I	925.00		NIST
I	928.00		NIST
I	925.00		NIST
I	961.00		NIST
I	964.00		NIST
I	953.00		NIST
I	970.00		NIST
I	951.00		NIST
I	940.00		NIST
I	960.00		NIST
I	959.00		NIST
I	960.00		NIST
I	957.00		NIST
I	965.00		NIST
I	955.00		NIST
I	Outlier 915.00		NIST
I	924.00		NIST
I	951.00		NIST
I	945.00		NIST
I	960.00		NIST
I	952.00		NIST
I	949.00		NIST
I	971.00		NIST
I	956.00		NIST
I	953.00		NIST
I	953.00		NIST
I	946.00		NIST
I	931.00		NIST
I	950.00		NIST
I	950.00		NIST
I	952.00		NIST
I	952.00		NIST
I	955.00		NIST
I	955.00		NIST
I	949.00		NIST
I	945.00		NIST
I	961.00		NIST
I	967.00		NIST
I	944.00		NIST
I	940.00		NIST
I	944.00		NIST
I	952.00		NIST
I	957.00		NIST
I	939.00		NIST
I	956.00		NIST
I	957.00		NIST
I	974.00		NIST
I	964.00		NIST
I	961.00		NIST
I	957.00		NIST
I	959.00		NIST
I	Outlier 916.00		NIST
I	944.00		NIST
I	950.00		NIST
I	938.00		NIST
I	925.00		NIST
I	925.00		NIST
I	925.00		NIST
I	966.00		NIST
I	944.00		NIST
I	940.00		NIST
I	948.00		NIST
I	977.00		NIST
I	970.00		NIST
I	960.00		NIST
I	955.00		NIST
I	952.00		NIST
Tboil	[371.91; 372.25]	K
Tboil	372.20	K	KDB
Tboil	372.20	K	(Liquid + liquid) equilibria of (water + butyric acid + esters) ternary systems
Tboil	372.25	K	Isobaric vapour-liquid equilibrium for binary systems of ethyl iodide with ethanol, propionic acid and ethyl propionate at 101.3 kPa
Tboil	372.25	K	Solubility and critical surface in the system propionic acid-ethanol-ethyl propionate-water at 293.15, 303.15 and 313.15 K
Tboil	371.91	K	Isobaric Vapor-Liquid Equilibria and Excess Quantities for Binary Mixtures of an Ethyl Ester + tert-Butanol and a New Approach to VLE Data Processing
Tc	[545.60; 553.80]	K
Tc	546.00	K	KDB
Tc	546.00	K	NIST
Tc	546.10 ± 1.00	K	NIST
Tc	546.00 ± 1.00	K	NIST
Tc	545.60 ± 1.00	K	NIST
Tc	552.70 ± 5.00	K	NIST
Tc	545.60 ± 2.00	K	NIST
Tc	553.80 ± 5.00	K	NIST
Tfus	[199.20; 200.24]	K
Tfus	199.85	K	Aq. Solubility Prediction
Tfus	199.20	K	KDB
Tfus	199.71	K	Efficient determination of crystallisation and melting points at low cooling and heating rates with novel computer controlled equipment
Tfus	199.25 ± 0.40	K	NIST
Tfus	200.24 ± 0.20	K	NIST
Vc	0.345	m3/kmol	KDB
Zc	0.2554980		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[163.46; 210.46]	J/mol×K	[390.09; 568.66]
Cp,gas	163.46	J/mol×K	390.09	Joback Calculated Property
Cp,gas	171.91	J/mol×K	419.85	Joback Calculated Property
Cp,gas	180.12	J/mol×K	449.61	Joback Calculated Property
Cp,gas	188.08	J/mol×K	479.38	Joback Calculated Property
Cp,gas	195.80	J/mol×K	509.14	Joback Calculated Property
Cp,gas	203.26	J/mol×K	538.90	Joback Calculated Property
Cp,gas	210.46	J/mol×K	568.66	Joback Calculated Property
Cp,liquid	[199.58; 200.90]	J/mol×K	[298.15; 298.33]
Cp,liquid	200.90	J/mol×K	298.15	NIST
Cp,liquid	199.58	J/mol×K	298.33	NIST
η	[0.0003150; 0.0005230]	Pa×s	[293.15; 343.15]
η	0.0005230	Pa×s	293.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0004920	Pa×s	298.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0004640	Pa×s	303.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0004410	Pa×s	308.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0004180	Pa×s	313.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0003980	Pa×s	318.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0003780	Pa×s	323.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0003600	Pa×s	328.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0003440	Pa×s	333.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0003290	Pa×s	338.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0003150	Pa×s	343.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
ΔvapH	[33.88; 38.20]	kJ/mol	[313.00; 455.00]
ΔvapH	38.20 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	36.60 ± 0.10	kJ/mol	336.00	NIST
ΔvapH	38.20	kJ/mol	339.00	NIST
ΔvapH	36.00 ± 0.10	kJ/mol	344.00	NIST
ΔvapH	35.50 ± 0.10	kJ/mol	351.00	NIST
ΔvapH	34.50 ± 0.10	kJ/mol	363.00	NIST
ΔvapH	36.70	kJ/mol	367.50	NIST
ΔvapH	33.88	kJ/mol	372.20	NIST
ΔvapH	34.40	kJ/mol	455.00	NIST
Pvap	[10.60; 101.30]	kPa	[313.15; 372.25]
Pvap	10.60	kPa	313.15	Total Vapor Pressure Measurements for 2-Ethoxyethanol with Methyl Acetate, Ethyl Acetate, Propyl Acetate, and Ethyl Propionate at 313.15 K and for 2-Ethoxyethanol with Methyl Formate at 308.15 K
Pvap	101.30	kPa	372.25	Isobaric vapour-liquid equilibrium for binary systems of ethyl iodide with ethanol, propionic acid and ethyl propionate at 101.3 kPa
n0	[1.37110; 1.38150]		[298.15; 318.15]
n0	1.38150		298.15	Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) I: HE and V E for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1-x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 5, a = 1 and v = x = 2 to 6
n0	1.38110		298.15	Improvements in the Experimentation and the Representation of Thermodynamic Properties (iso-p VLE and yE) of Alkyl Propanoate + Alkane Binaries
n0	1.37110		318.15	Thermodynamic properties of (an ester + and alkane). XVII. Experimental He and Ve values for (an alkyl propanoate + an alkane) at 318.15K
ρl	895.00	kg/m3	289.00	KDB
λ	[0.12; 0.15]	W/m×K	[263.55; 356.28]
λ	0.15	W/m×K	263.55	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.15	W/m×K	268.41	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.15	W/m×K	270.94	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.15	W/m×K	278.51	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.14	W/m×K	283.51	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.14	W/m×K	288.56	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.14	W/m×K	293.54	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.14	W/m×K	296.36	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.14	W/m×K	301.40	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.14	W/m×K	306.51	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.13	W/m×K	311.34	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.13	W/m×K	316.45	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.13	W/m×K	321.47	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.13	W/m×K	326.44	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.13	W/m×K	331.53	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.13	W/m×K	336.40	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.12	W/m×K	341.36	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.12	W/m×K	346.42	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.12	W/m×K	351.35	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.12	W/m×K	356.28	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase

Datasets

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	298.15	884.3
100.00	303.15	878.5
100.00	308.15	872.7
100.00	313.15	866.8
100.00	318.15	860.9
100.00	323.15	854.9
100.00	328.15	849.2
100.00	333.15	843.1
100.00	338.15	836.9
100.00	343.15	831.1
100.00	348.15	824.9
100.00	353.15	818.7
100.00	363.15	803.5
100.00	373.15	790.9
1000.00	298.15	884.8
1000.00	303.15	879.0
1000.00	308.15	873.2
1000.00	313.15	867.4
1000.00	318.15	861.5
1000.00	323.15	856.0
1000.00	328.15	850.2
1000.00	333.15	844.2
1000.00	338.15	838.2
1000.00	343.15	832.2
1000.00	348.15	826.0
1000.00	353.15	819.9
1000.00	363.15	805.1
1000.00	373.15	792.6
1000.00	383.15	780.0
1000.00	393.15	766.4
2000.00	298.15	885.7
2000.00	303.15	880.0
2000.00	308.15	874.2
2000.00	313.15	868.4
2000.00	318.15	862.6
2000.00	323.15	857.1
2000.00	328.15	851.3
2000.00	333.15	845.4
2000.00	338.15	839.5
2000.00	343.15	833.5
2000.00	348.15	827.4
2000.00	353.15	821.3
2000.00	363.15	806.9
2000.00	373.15	794.5
2000.00	383.15	782.1
2000.00	393.15	768.7
3000.00	298.15	886.6
3000.00	303.15	880.9
3000.00	308.15	875.2
3000.00	313.15	869.4
3000.00	318.15	863.7
3000.00	323.15	858.1
3000.00	328.15	852.5
3000.00	333.15	846.6
3000.00	338.15	840.7
3000.00	343.15	834.8
3000.00	348.15	828.8
3000.00	353.15	822.7
3000.00	363.15	808.7
3000.00	373.15	796.4
3000.00	383.15	784.1
3000.00	393.15	770.8
3340.00	298.15	886.9
3340.00	303.15	881.2
3340.00	308.15	875.5
3340.00	313.15	869.8
3340.00	318.15	864.1
3340.00	323.15	858.4
3340.00	328.15	852.9
3340.00	333.15	847.0
3340.00	338.15	841.1
3340.00	343.15	835.2
3340.00	348.15	829.3
3340.00	353.15	823.2
3340.00	363.15	809.3
3340.00	373.15	797.1
3340.00	383.15	784.8
3340.00	393.15	771.5
5000.00	298.15	888.7
5000.00	303.15	883.0
5000.00	308.15	877.4
5000.00	313.15	871.7
5000.00	318.15	866.1
5000.00	323.15	860.3
5000.00	328.15	854.7
5000.00	333.15	849.0
5000.00	338.15	843.1
5000.00	343.15	837.4
5000.00	348.15	831.5
5000.00	353.15	825.6
5000.00	363.15	812.0
5000.00	373.15	800.0
5000.00	383.15	787.9
5000.00	393.15	775.0
10000.00	298.15	892.9
10000.00	303.15	887.4
10000.00	308.15	882.0
10000.00	313.15	876.5
10000.00	318.15	871.0
10000.00	323.15	865.4
10000.00	328.15	860.0
10000.00	333.15	854.6
10000.00	338.15	848.8
10000.00	343.15	843.4
10000.00	348.15	837.7
10000.00	353.15	832.1
10000.00	363.15	819.6
10000.00	373.15	808.2
10000.00	383.15	796.6
10000.00	393.15	784.5
15000.00	298.15	896.9
15000.00	303.15	891.6
15000.00	308.15	886.3
15000.00	313.15	880.9
15000.00	318.15	875.6
15000.00	323.15	870.2
15000.00	328.15	865.0
15000.00	333.15	859.7
15000.00	338.15	854.4
15000.00	343.15	848.9
15000.00	348.15	843.4
15000.00	353.15	838.0
15000.00	363.15	826.5
15000.00	373.15	815.6
15000.00	383.15	804.6
15000.00	393.15	793.1
20000.00	298.15	900.7
20000.00	303.15	895.6
20000.00	308.15	890.4
20000.00	313.15	885.1
20000.00	318.15	880.0
20000.00	323.15	874.7
20000.00	328.15	869.6
20000.00	333.15	864.5
20000.00	338.15	859.4
20000.00	343.15	854.0
20000.00	348.15	848.8
20000.00	353.15	843.5
20000.00	363.15	833.0
20000.00	373.15	822.5
20000.00	383.15	811.9
20000.00	393.15	800.8
25000.00	298.15	904.4
25000.00	303.15	899.4
25000.00	308.15	894.3
25000.00	313.15	889.3
25000.00	318.15	884.1
25000.00	323.15	879.1
25000.00	328.15	874.0
25000.00	333.15	869.2
25000.00	338.15	863.6
25000.00	343.15	859.1
25000.00	348.15	854.0
25000.00	353.15	848.9
25000.00	363.15	839.1
25000.00	373.15	829.0
25000.00	383.15	818.7
25000.00	393.15	808.0
30000.00	298.15	908.9
30000.00	303.15	904.0
30000.00	308.15	899.2
30000.00	313.15	894.4
30000.00	318.15	889.1
30000.00	323.15	884.3
30000.00	328.15	879.4
30000.00	333.15	874.8
30000.00	338.15	869.9
30000.00	343.15	865.0
30000.00	348.15	860.1
30000.00	353.15	855.3
30000.00	363.15	844.8
30000.00	373.15	834.9
30000.00	383.15	825.0
30000.00	393.15	814.7
35000.00	298.15	913.6
35000.00	303.15	908.9
35000.00	308.15	904.2
35000.00	313.15	899.5
35000.00	318.15	894.3
35000.00	323.15	889.7
35000.00	328.15	884.9
35000.00	333.15	880.6
35000.00	338.15	875.8
35000.00	343.15	871.0
35000.00	348.15	866.3
35000.00	353.15	861.6
35000.00	363.15	850.2
35000.00	373.15	840.6
35000.00	383.15	830.9
35000.00	393.15	820.9
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.62]	kPa	[275.40; 396.11]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.45526e+01
Coefficient B			-3.16736e+03
Coefficient C			-5.33670e+01
Temperature range, min.			275.40
Temperature range, max.			396.11
Pvap	1.33	kPa	275.40	Calculated Property
Pvap	3.00	kPa	288.81	Calculated Property
Pvap	6.20	kPa	302.22	Calculated Property
Pvap	11.89	kPa	315.64	Calculated Property
Pvap	21.40	kPa	329.05	Calculated Property
Pvap	36.47	kPa	342.46	Calculated Property
Pvap	59.27	kPa	355.87	Calculated Property
Pvap	92.45	kPa	369.29	Calculated Property
Pvap	139.07	kPa	382.70	Calculated Property
Pvap	202.62	kPa	396.11	Calculated Property
Pvap	[7.72e-04; 3311.89]	kPa	[199.25; 546.00]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			1.01207e+02
Coefficient B			-8.10148e+03
Coefficient C			-1.28594e+01
Coefficient D			9.33835e-06
Temperature range, min.			199.25
Temperature range, max.			546.00
Pvap	7.72e-04	kPa	199.25	Calculated Property
Pvap	0.07	kPa	237.78	Calculated Property
Pvap	1.36	kPa	276.31	Calculated Property
Pvap	11.39	kPa	314.83	Calculated Property
Pvap	54.26	kPa	353.36	Calculated Property
Pvap	178.61	kPa	391.89	Calculated Property
Pvap	457.44	kPa	430.42	Calculated Property
Pvap	985.54	kPa	468.94	Calculated Property
Pvap	1883.25	kPa	507.47	Calculated Property
Pvap	3311.89	kPa	546.00	Calculated Property

Similar Compounds

Find more compounds similar to Propanoic acid, ethyl ester.

Mixtures

• Propanoic acid, ethyl ester + Heptane
• Propanoic acid, ethyl ester + Nonane
• Propanoic acid, ethyl ester + Undecane
• Propanoic acid, ethyl ester + Tridecane
• Propanoic acid, ethyl ester + Pentadecane
• Propanoic acid, ethyl ester + Heptadecane
• Propanoic acid, ethyl ester + Ethane, 1,2-dichloro-
• Propanoic acid, ethyl ester + Propane, 1,3-dichloro-
• Propanoic acid, ethyl ester + Butane, 1,4-dichloro-
• Propanoic acid, ethyl ester + Pentane, 1,5-dichloro-
• Propanoic acid, ethyl ester + Hexane, 1,6-dichloro-
• Propanoic acid, ethyl ester + Ethane, 1,2-dibromo-
• Propanoic acid, ethyl ester + Propane, 1,3-dibromo-
• Propanoic acid, ethyl ester + Butane, 1,4-dibromo-
• Propanoic acid, ethyl ester + Pentane, 1,5-dibromo-
• Propanoic acid, ethyl ester + Hexane, 1,6-dibromo-
• Propanoic acid, ethyl ester + Butanoic acid + Water
• Propanoic acid, ethyl ester + Water
• Propanoic acid, ethyl ester + Ethane, iodo-
• Propanoic acid, ethyl ester + Propanoic acid + Water

Find more mixtures with Propanoic acid, ethyl ester.

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Experimental determination and calculation of the critical curves for the binary systems of CO2 containing ketone, alkane, ester and alcohol, respectively
• Temperature dependence of limiting activity coefficients, Henry's law constants, and related infinite dilution properties of C4-C6 isomeric n-alkyl ethanoates/ethyl n-alkanoates in water. Measurement, critical compilation, correlation, and recommended data
• Vapor-liquid equilibrium in the binary and ternary systems containing ethyl propionate, ethanol and alkane at 101.3 kPa
• Thermodynamic properties of (an ester + and alkane). XVII. Experimental He and Ve values for (an alkyl propanoate + an alkane) at 318.15K
• Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) I: HE and V E for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1-x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 5, a = 1 and v = x = 2 to 6
• Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) II: HE m and V E m for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1 - x)a,x-BrCH2(CH2)v-2CH2Br}, where u = 1 to 5, a = 1 and v = x = 2 to 6
• (Liquid + liquid) equilibria of (water + butyric acid + esters) ternary systems
• Efficient determination of crystallisation and melting points at low cooling and heating rates with novel computer controlled equipment
• Isothermal (vapour + liquid) equilibria for the binary systems of (carbon monoxide + methyl propionate) and (carbon monoxide + ethyl propionate)
• Liquid-liquid equilibrium of alcohol-ester systems with deep eutectic solvent on the base of choline chloride
• Isobaric vapour-liquid equilibrium for binary systems of ethyl iodide with ethanol, propionic acid and ethyl propionate at 101.3 kPa
• Solubility and critical surface in the system propionic acid-ethanol-ethyl propionate-water at 293.15, 303.15 and 313.15 K
• Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
• Isobaric Vapor-Liquid Equilibria and Excess Quantities for Binary Mixtures of an Ethyl Ester + tert-Butanol and a New Approach to VLE Data Processing
• Total Vapor Pressure Measurements for 2-Ethoxyethanol with Methyl Acetate, Ethyl Acetate, Propyl Acetate, and Ethyl Propionate at 313.15 K and for 2-Ethoxyethanol with Methyl Formate at 308.15 K
• Vapor-Liquid Equilibria of the Carbon Dioxide + Ethyl Propanoate and Carbon Dioxide + Ethyl Acetate Systems at Pressure from 2.96 MPa to 11.79 MPa and Temperature from 313 K to 393 K
• Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
• Improvements in the Experimentation and the Representation of Thermodynamic Properties (iso-p VLE and yE) of Alkyl Propanoate + Alkane Binaries
• Development of a Predictive Equation of State for CO2 + Ethyl Ester Mixtures Based on Critical Points Measurements
• PVT Property Measurements for Ethyl Propionate, Ethyl Butyrate, and Ethyl Pentanoate Esters from (298 to 393) K and up to 35 MPa
• 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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