Chemical Properties of Heptanoic acid, ethyl ester (CAS 106-30-9)

InChI

InChI=1S/C9H18O2/c1-3-5-6-7-8-9(10)11-4-2/h3-8H2,1-2H3

InChI Key

TVQGDYNRXLTQAP-UHFFFAOYSA-N

Formula

C9H18O2

SMILES

CCCCCCC(=O)OCC

Molecular Weight¹

158.24

CAS

106-30-9

Other Names

• Aether oenanthicus
• Cognac oil
• Enanthic acid ethyl ester
• Ethyl enanthate
• Ethyl ester of heptanoic acid
• Ethyl heptoate
• Ethyl n-heptanoate
• Ethyl oenanthate
• Ethyl oenanthylate
• Grape oil
• NSC 8891
• Oenanthic ether
• Oleum vitis viniferae
• Wine oil
• enanthylic ether
• ethyl enantate
• ethyl heptanoate
• ethyl heptylate

• 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_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).
• 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).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• c_sound,fluid : Speed of sound in fluid (m/s).
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced pressure (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).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Pressure Dependent Properties
4. Datasets
5. Correlations
6. Similar Compounds
7. Mixtures
8. Sources

Physical Properties

Property	Value	Unit	Source
ω	0.5659		Relay (1.0) Calculated Property
ΔfG°	-285.47	kJ/mol	Joback Calculated Property
ΔfH°gas	-548.00 ± 2.00	kJ/mol	NIST
ΔfH°liquid	-603.80 ± 1.50	kJ/mol	NIST
ΔfusH°	23.43	kJ/mol	Joback Calculated Property
ΔvapH°	[55.80; 56.00]	kJ/mol
ΔvapH°	56.00 ± 1.00	kJ/mol	NIST
ΔvapH°	55.80	kJ/mol	NIST
IE	9.70	eV	Relay (1.0) Calculated Property
log10WS	[-2.74; -2.71]
log10WS	-2.71		Aq. Solubility Prediction
log10WS	-2.74		Estimated Solubility
logPoct/wat	2.520		Crippen Calculated Property
McVol	145.110	ml/mol	McGowan Calculated Property
Pc	2356.90	kPa	Development of a Predictive Equation of State for CO2 + Ethyl Ester Mixtures Based on Critical Points Measurements
Inp	[1068.00; 1108.00]
Inp	1077.00		NIST
Inp	1081.00		NIST
Inp	1096.00		NIST
Inp	1081.00		NIST
Inp	1075.00		NIST
Inp	1084.00		NIST
Inp	1080.00		NIST
Inp	1084.00		NIST
Inp	1084.00		NIST
Inp	1080.00		NIST
Inp	1084.00		NIST
Inp	1089.00		NIST
Inp	1098.00		NIST
Inp	1096.00		NIST
Inp	1085.00		NIST
Inp	1093.00		NIST
Inp	1091.00		NIST
Inp	1095.00		NIST
Inp	1099.00		NIST
Inp	1081.00		NIST
Inp	1082.00		NIST
Inp	1093.00		NIST
Inp	1081.00		NIST
Inp	1083.00		NIST
Inp	1083.00		NIST
Inp	1088.00		NIST
Inp	1080.00		NIST
Inp	1093.30		NIST
Inp	1099.00		NIST
Inp	1108.00		NIST
Inp	1099.00		NIST
Inp	1097.00		NIST
Inp	1100.00		NIST
Inp	1097.00		NIST
Inp	1107.00		NIST
Inp	1108.00		NIST
Inp	1097.00		NIST
Inp	1095.00		NIST
Inp	1103.00		NIST
Inp	1099.00		NIST
Inp	1083.00		NIST
Inp	1080.00		NIST
Inp	1082.00		NIST
Inp	1080.00		NIST
Inp	1084.00		NIST
Inp	1078.00		NIST
Inp	1093.00		NIST
Inp	1098.00		NIST
Inp	1098.00		NIST
Inp	1104.00		NIST
Inp	1103.00		NIST
Inp	1096.00		NIST
Inp	1097.00		NIST
Inp	1099.00		NIST
Inp	Outlier 1068.00		NIST
Inp	Outlier 1068.00		NIST
Inp	1099.00		NIST
Inp	1082.00		NIST
Inp	1097.00		NIST
Inp	1082.00		NIST
Inp	1081.00		NIST
Inp	1080.00		NIST
Inp	1081.00		NIST
Inp	1082.00		NIST
Inp	1082.00		NIST
Inp	1084.00		NIST
Inp	1093.30		NIST
I	[1310.00; 1375.00]
I	1328.00		NIST
I	Outlier 1375.00		NIST
I	1325.00		NIST
I	Outlier 1369.00		NIST
I	Outlier 1367.00		NIST
I	1332.00		NIST
I	1341.00		NIST
I	1336.00		NIST
I	1324.00		NIST
I	1352.00		NIST
I	1329.00		NIST
I	1328.00		NIST
I	Outlier 1372.00		NIST
I	1323.00		NIST
I	1324.00		NIST
I	1324.00		NIST
I	1334.00		NIST
I	1337.00		NIST
I	1360.00		NIST
I	1326.00		NIST
I	1331.00		NIST
I	1327.00		NIST
I	1341.00		NIST
I	1324.00		NIST
I	1331.00		NIST
I	1332.00		NIST
I	1317.00		NIST
I	1325.00		NIST
I	1310.00		NIST
I	1310.00		NIST
I	1342.00		NIST
I	1315.00		NIST
I	1321.00		NIST
I	1338.00		NIST
I	1342.00		NIST
I	1330.00		NIST
I	1336.00		NIST
I	1349.00		NIST
I	1315.00		NIST
I	1317.00		NIST
I	1327.00		NIST
I	1331.00		NIST
I	1331.00		NIST
I	1321.00		NIST
I	1345.00		NIST
I	1335.00		NIST
I	1345.00		NIST
I	1321.00		NIST
I	1325.00		NIST
I	1336.00		NIST
I	1331.00		NIST
I	1345.00		NIST
I	1341.00		NIST
I	1328.00		NIST
I	1334.00		NIST
I	1332.00		NIST
Tboil	[460.30; 461.70]	K
Tboil	461.70	K	KDB
Tboil	461.70	K	NIST
Tboil	461.70 ± 0.30	K	NIST
Tboil	460.30 ± 2.00	K	NIST
Tc	634.30 ± 0.60	K	NIST
Tfus	[206.90; 207.12]	K
Tfus	207.05	K	KDB
Tfus	207.12	K	Aq. Solubility Prediction
Tfus	206.90 ± 0.50	K	NIST
Vc	0.566	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
n0	[1.38421; 1.42006]		[278.15; 358.15]
n0	1.42006		278.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41784		283.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41562		288.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41341		293.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41119		298.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.40896		303.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.40673		308.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.40445		313.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.40216		318.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.39988		323.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.39761		328.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.39535		333.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.39311		338.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.39088		343.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.38866		348.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.38645		353.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.38421		358.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	881.30	kg/m3	293.15	Phase equilibrium of (water + formic or acetic acid + ethyl heptanoate) ternary liquid systems at different temperatures
λ	[0.11; 0.15]	W/m×K	[250.38; 393.46]
λ	0.15	W/m×K	250.38	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.15	W/m×K	260.21	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.14	W/m×K	270.16	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.14	W/m×K	280.02	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.14	W/m×K	289.93	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.14	W/m×K	299.84	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.13	W/m×K	309.90	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.13	W/m×K	319.73	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.13	W/m×K	329.73	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.13	W/m×K	337.72	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.13	W/m×K	341.71	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.13	W/m×K	347.65	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.12	W/m×K	353.60	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.12	W/m×K	363.50	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.12	W/m×K	373.51	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.12	W/m×K	383.64	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.11	W/m×K	393.46	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	351.20	K	1.90	NIST

Datasets

1. Molar heat capacity at constant pressure, J/K/mol (1)
2. Mass density, kg/m3 (1)
3. Speed of sound, m/s (1)

Molar heat capacity at constant pressure, J/K/mol

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
305.40	100.00	318.30
305.40	4040.00	317.70
305.40	8190.00	317.30
305.40	12090.00	316.80
305.50	16070.00	316.40
315.70	100.00	322.50
315.80	4190.00	322.00
315.90	8150.00	321.60
315.90	12260.00	320.50
316.00	16160.00	319.60
326.50	100.00	326.80
326.50	4140.00	325.90
326.60	8170.00	325.20
326.60	12110.00	324.30
326.20	16030.00	323.60
335.30	100.00	330.30
335.30	4060.00	330.10
335.40	8050.00	328.60
335.40	12030.00	327.60
335.50	16070.00	326.90
345.10	100.00	334.20
345.20	4070.00	333.50
345.60	8230.00	332.50
345.70	12160.00	332.20
345.70	16230.00	330.50
354.20	100.00	337.80
354.20	4120.00	337.30
354.30	8010.00	336.50
354.40	12390.00	335.60
354.50	16250.00	334.50
364.90	100.00	342.10
365.30	3870.00	341.30
365.60	8320.00	340.30
365.70	12160.00	339.50
365.80	15950.00	338.30
374.80	100.00	346.10
375.00	3980.00	345.50
375.50	8020.00	344.00
375.70	12070.00	342.60
375.90	16040.00	341.40
384.00	100.00	349.80
385.00	4020.00	349.10
385.40	8040.00	347.10
385.50	11880.00	346.10
385.70	15890.00	345.60
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
303.20	100.00	860.8
303.20	3020.00	864.5
303.10	6000.00	867.7
303.20	9010.00	871.2
303.21	11950.00	874.5
303.19	14980.00	877.5
312.96	100.00	851.2
313.06	3060.00	854.7
313.13	6090.00	858.1
313.17	9070.00	861.4
313.18	12000.00	864.7
313.17	15010.00	867.9
323.09	100.00	841.6
323.11	3100.00	845.2
323.14	6110.00	848.8
323.10	9100.00	852.5
323.13	12060.00	855.8
323.09	15150.00	859.2
333.05	100.00	832.1
333.14	3010.00	835.6
333.18	6080.00	839.7
333.14	9020.00	843.2
333.14	12010.00	846.8
333.20	15070.00	850.5
343.02	100.00	823.0
343.06	3010.00	827.1
343.23	6050.00	831.0
343.20	9000.00	834.8
343.22	12100.00	838.5
343.19	15000.00	842.1
352.85	100.00	815.1
352.95	3090.00	819.4
353.11	6070.00	823.2
353.06	9090.00	827.5
353.14	12070.00	831.2
353.23	15010.00	835.1
Reference

Speed of sound, m/s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
293.27	110.00	1254.03
303.20	100.00	1219.89
313.04	90.00	1185.84
323.08	110.00	1145.28
332.61	100.00	1119.94
343.14	100.00	1075.42
353.04	110.00	1044.19
363.11	100.00	1008.42
372.84	90.00	971.9
382.87	100.00	941.96
392.49	100.00	909.29
401.72	110.00	876.2
412.92	100.00	837.29
422.78	110.00	800.01
432.75	100.00	768.89
441.74	90.00	736.98
452.13	100.00	703.21
293.55	1040.00	1263.87
302.87	1020.00	1230.26
313.07	1000.00	1189.64
323.15	1020.00	1154.57
332.75	980.00	1123.74
343.15	1020.00	1086.84
352.67	1000.00	1053.08
362.35	1010.00	1014.12
371.83	1020.00	987.06
382.34	1020.00	948.49
392.73	980.00	912.95
401.77	1030.00	883.74
412.69	1050.00	841.82
422.42	1000.00	807.44
432.36	1120.00	778.68
441.56	1020.00	750.38
451.89	990.00	714.64
462.89	1110.00	677.9
471.98	1010.00	647.85
482.54	1000.00	610.64
293.40	2560.00	1278.44
303.46	2500.00	1233.57
313.11	2510.00	1200.03
323.11	2490.00	1164.66
332.84	2500.00	1127.35
451.94	2540.00	731.06
463.03	2520.00	699.91
472.16	2540.00	667.91
482.35	2490.00	636.04
293.20	4000.00	1290.82
303.00	4050.00	1253.21
312.99	4070.00	1207.7
323.12	3990.00	1173.82
332.85	4010.00	1140.43
343.20	4050.00	1101.44
352.64	4010.00	1073.47
362.37	4060.00	1038.84
371.97	4040.00	1005.36
382.36	3940.00	970.18
392.65	4020.00	936.25
401.75	4030.00	907.66
412.64	4050.00	868.48
422.45	4040.00	836.46
432.43	4070.00	805.62
441.62	4050.00	783.09
452.05	4040.00	748.01
463.13	4040.00	714.4
472.23	4040.00	687.28
483.02	4020.00	655.14
293.74	5550.00	1291.01
303.04	5540.00	1254.0
313.12	5550.00	1223.42
323.12	5530.00	1181.98
333.57	5530.00	1140.54
343.18	5510.00	1114.79
352.70	5540.00	1079.0
362.26	5530.00	1045.42
372.00	5590.00	1016.18
382.32	5500.00	983.52
392.67	5520.00	946.64
401.62	5620.00	919.87
412.54	5550.00	885.03
422.48	5560.00	854.66
432.45	5500.00	819.99
441.62	5570.00	795.09
452.08	5580.00	763.54
463.22	5530.00	728.32
382.36	7030.00	991.78
392.69	6990.00	960.26
401.59	6980.00	932.15
412.71	7010.00	898.63
422.53	6970.00	866.85
432.47	6990.00	831.89
441.61	7020.00	810.86
452.07	7050.00	781.2
463.25	7020.00	748.5
472.22	7040.00	716.46
483.13	7020.00	690.38
294.07	8560.00	1302.85
303.06	8580.00	1271.63
313.03	8520.00	1229.84
323.14	8520.00	1198.91
332.87	8520.00	1168.42
343.18	8540.00	1133.1
352.86	8580.00	1098.06
362.06	8560.00	1073.66
372.00	8580.00	1035.47
382.40	8550.00	1003.61
392.72	8520.00	974.33
401.43	8550.00	945.5
412.77	8460.00	910.68
422.49	8460.00	880.79
432.50	8520.00	845.66
441.61	8500.00	822.18
452.07	8500.00	791.7
463.26	8550.00	758.92
472.22	8560.00	727.9
483.34	8540.00	700.94
293.99	10050.00	1302.01
303.06	10060.00	1275.7
313.06	9950.00	1235.73
323.14	9970.00	1202.86
332.88	10020.00	1171.25
343.18	10030.00	1146.59
352.81	9950.00	1114.93
362.02	9960.00	1086.09
372.00	9980.00	1054.29
382.38	10030.00	1013.95
392.70	10020.00	988.42
342.92	2540.00	1095.65
352.61	2510.00	1056.91
362.38	2500.00	1028.17
371.91	2580.00	995.52
382.38	2510.00	958.12
392.65	2490.00	924.2
401.70	2510.00	892.06
412.73	2540.00	858.95
422.35	2540.00	826.98
432.43	2500.00	790.22
441.59	2560.00	766.2
472.22	5550.00	706.95
483.07	5540.00	677.03
293.91	7040.00	1299.58
303.06	7040.00	1262.89
313.09	7070.00	1225.84
323.13	7000.00	1188.04
332.88	7010.00	1156.97
343.18	7060.00	1119.21
352.76	7070.00	1088.79
361.99	7040.00	1061.57
372.00	7060.00	1029.84
401.51	10090.00	955.49
412.74	10010.00	920.21
422.51	9930.00	896.93
432.49	10010.00	865.32
441.61	10030.00	837.4
452.07	10040.00	804.8
463.25	10030.00	765.58
472.22	10050.00	743.93
483.14	10030.00	706.31
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[212.74; 491.76]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			2.01160e+01
Coefficient B			8.04040e-01
Coefficient C			-3.71200e-04
Coefficient D			3.88000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	212.74	J/mol×K	273.00	Calculated Property
Cp,gas	259.83	J/mol×K	353.78	Calculated Property
Cp,gas	302.60	J/mol×K	434.56	Calculated Property
Cp,gas	341.20	J/mol×K	515.33	Calculated Property
Cp,gas	375.73	J/mol×K	596.11	Calculated Property
Cp,gas	406.32	J/mol×K	676.89	Calculated Property
Cp,gas	433.10	J/mol×K	757.67	Calculated Property
Cp,gas	456.18	J/mol×K	838.44	Calculated Property
Cp,gas	475.69	J/mol×K	919.22	Calculated Property
Cp,gas	491.76	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0141167; 0.0002612]	Pa×s	[207.02; 444.01]	Joback Predicted correlation
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.17359e+01
Coefficient B			1.54760e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc.
Temperature range, min.			207.02
Temperature range, max.			444.01
η	0.0141167	Pa×s	207.02	Calculated Property
η	0.0060728	Pa×s	233.36	Calculated Property
η	0.0030999	Pa×s	259.69	Calculated Property
η	0.0017909	Pa×s	286.02	Calculated Property
η	0.0011349	Pa×s	312.35	Calculated Property
η	0.0007721	Pa×s	338.68	Calculated Property
η	0.0005553	Pa×s	365.01	Calculated Property
η	0.0004175	Pa×s	391.35	Calculated Property
η	0.0003253	Pa×s	417.68	Calculated Property
η	0.0002612	Pa×s	444.01	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[345.12; 483.23]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.53528e+01
Coefficient B			-4.15873e+03
Coefficient C			-6.90720e+01
Temperature range, min.			345.12
Temperature range, max.			483.23
Pvap	1.33	kPa	345.12	Calculated Property
Pvap	2.95	kPa	360.47	Calculated Property
Pvap	6.02	kPa	375.81	Calculated Property
Pvap	11.48	kPa	391.16	Calculated Property
Pvap	20.66	kPa	406.50	Calculated Property
Pvap	35.31	kPa	421.85	Calculated Property
Pvap	57.72	kPa	437.19	Calculated Property
Pvap	90.72	kPa	452.54	Calculated Property
Pvap	137.70	kPa	467.88	Calculated Property
Pvap	202.64	kPa	483.23	Calculated Property

Similar Compounds

Find more compounds similar to Heptanoic acid, ethyl ester.

Mixtures

• Heptanoic acid, ethyl ester + Formic acid + Water
• Heptanoic acid, ethyl ester + Acetic acid + Water
• Carbon dioxide + Heptanoic acid, ethyl ester

Sources

• Cheméo Relay (1.0)
• Crippen Method
• Phase equilibrium of (water + formic or acetic acid + ethyl heptanoate) ternary liquid systems at different temperatures
• Measurement of speed of sound and thermal diffusivity of ethyl heptanoate using light scattering method
• Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
• Isobaric heat capacities of ethyl heptanoate and ethyl cinnamate at pressures up to 16.3 MPa
• Thermophysical properties of fatty acid methyl and ethyl esters
• Densities and Viscosities of Ethyl Heptanoate and Ethyl Octanoate at Temperatures from 303 to 353 K and at Pressures up to 15 MPa
• Development of a Predictive Equation of State for CO2 + Ethyl Ester Mixtures Based on Critical Points Measurements
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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