Physical Properties
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[279.70; 346.77]
J/mol×K
[458.73; 633.80]
Cp,gas
279.70
J/mol×K
458.73
Joback Calculated Property
Cp,gas
291.94
J/mol×K
487.91
Joback Calculated Property
Cp,gas
303.75
J/mol×K
517.09
Joback Calculated Property
Cp,gas
315.14
J/mol×K
546.26
Joback Calculated Property
Cp,gas
326.10
J/mol×K
575.44
Joback Calculated Property
Cp,gas
336.64
J/mol×K
604.62
Joback Calculated Property
Cp,gas
346.77
J/mol×K
633.80
Joback Calculated Property
η
[0.0004290; 0.0011020]
Pa×s
[288.15; 343.15]
η
0.0011020
Pa×s
288.15
Densiti...
η
0.0008160
Pa×s
293.15
Density...
η
0.0008160
Pa×s
293.15
Density...
η
0.0007570
Pa×s
298.15
Density...
η
0.0009400
Pa×s
298.15
Densiti...
η
0.0007040
Pa×s
303.15
Density...
η
0.0007040
Pa×s
303.15
Density...
η
0.0008140
Pa×s
308.15
Densiti...
η
0.0006560
Pa×s
308.15
Density...
η
0.0006140
Pa×s
313.15
Density...
η
0.0006140
Pa×s
313.15
Density...
η
0.0005760
Pa×s
318.15
Density...
η
0.0007110
Pa×s
318.15
Densiti...
η
0.0005410
Pa×s
323.15
Density...
η
0.0005090
Pa×s
328.15
Density...
η
0.0004820
Pa×s
333.15
Density...
η
0.0004560
Pa×s
338.15
Density...
η
0.0004290
Pa×s
343.15
Density...
Δvap H
[47.40; 51.80]
kJ/mol
[294.00; 422.50]
Δvap H
50.80 ± 0.40
kJ/mol
294.00
NIST
Δvap H
48.60
kJ/mol
338.00
NIST
Δvap H
47.40 ± 0.30
kJ/mol
359.50
NIST
Δvap H
51.80
kJ/mol
422.50
NIST
Pvap
[3.44e-03; 174.60]
kPa
[253.41; 462.43]
Pvap
3.44e-03
kPa
253.41
Experim...
Pvap
0.01
kPa
263.26
Experim...
Pvap
0.07
kPa
283.06
Experim...
Pvap
0.14
kPa
293.05
Experim...
Pvap
0.29
kPa
303.03
Experim...
Pvap
0.56
kPa
313.15
Experim...
Pvap
1.02
kPa
323.18
Experim...
Pvap
1.78
kPa
333.11
Experim...
Pvap
2.98
kPa
343.09
Experim...
Pvap
4.55
kPa
351.97
Experim...
Pvap
7.18
kPa
362.10
Experim...
Pvap
10.93
kPa
372.13
Experim...
Pvap
11.35
kPa
373.15
Isother...
Pvap
16.07
kPa
382.15
Experim...
Pvap
16.69
kPa
383.15
Isother...
Pvap
23.19
kPa
392.23
Experim...
Pvap
23.94
kPa
393.15
Isother...
Pvap
32.56
kPa
402.19
Experim...
Pvap
33.59
kPa
403.15
Isother...
Pvap
44.90
kPa
412.21
Experim...
Pvap
46.18
kPa
413.15
Isother...
Pvap
60.62
kPa
422.19
Experim...
Pvap
62.32
kPa
423.15
Isother...
Pvap
80.76
kPa
432.28
Experim...
Pvap
82.69
kPa
433.15
Isother...
Pvap
105.57
kPa
442.29
Experim...
Pvap
108.02
kPa
443.15
Isother...
Pvap
136.73
kPa
452.34
Experim...
Pvap
139.11
kPa
453.15
Isother...
Pvap
174.60
kPa
462.43
Experim...
n 0
[1.37754; 1.41438]
[278.15; 358.15]
n 0
1.41438
278.15
Thermop...
n 0
1.41210
283.15
Thermop...
n 0
1.40982
288.15
Thermop...
n 0
1.40753
293.15
Thermop...
n 0
1.40525
298.15
Thermop...
n 0
1.40295
303.15
Thermop...
n 0
1.40063
308.15
Thermop...
n 0
1.39829
313.15
Thermop...
n 0
1.39594
318.15
Thermop...
n 0
1.39360
323.15
Thermop...
n 0
1.39128
328.15
Thermop...
n 0
1.38897
333.15
Thermop...
n 0
1.38667
338.15
Thermop...
n 0
1.38438
343.15
Thermop...
n 0
1.38210
348.15
Thermop...
n 0
1.37983
353.15
Thermop...
n 0
1.37754
358.15
Thermop...
ρl
[865.59; 866.29]
kg/m3
[298.15; 298.15]
ρl
866.29
kg/m3
298.15
Refract...
ρl
865.59
kg/m3
298.15
Ebullio...
csound,fluid
[592.40; 1220.10]
m/s
[294.37; 473.82]
csound,fluid
1220.10
m/s
294.37
Speed o...
csound,fluid
1191.00
m/s
301.55
Speed o...
csound,fluid
1152.70
m/s
313.34
Speed o...
csound,fluid
1115.10
m/s
324.26
Speed o...
csound,fluid
1077.60
m/s
333.16
Speed o...
csound,fluid
1046.10
m/s
343.20
Speed o...
csound,fluid
1010.00
m/s
353.08
Speed o...
csound,fluid
975.00
m/s
363.12
Speed o...
csound,fluid
942.00
m/s
373.14
Speed o...
csound,fluid
905.40
m/s
383.76
Speed o...
csound,fluid
870.10
m/s
393.30
Speed o...
csound,fluid
834.90
m/s
402.64
Speed o...
csound,fluid
800.80
m/s
413.59
Speed o...
csound,fluid
764.00
m/s
423.96
Speed o...
csound,fluid
730.30
m/s
433.99
Speed o...
csound,fluid
697.60
m/s
443.55
Speed o...
csound,fluid
661.00
m/s
452.90
Speed o...
csound,fluid
628.80
m/s
463.10
Speed o...
csound,fluid
592.40
m/s
473.82
Speed o...
γ
[0.02; 0.03]
N/m
[288.15; 358.15]
γ
0.03
N/m
288.15
Densiti...
γ
0.03
N/m
298.15
Densiti...
γ
0.02
N/m
308.15
Densiti...
γ
0.02
N/m
318.15
Densiti...
γ
0.02
N/m
328.15
Densiti...
γ
0.02
N/m
338.15
Densiti...
γ
0.02
N/m
348.15
Densiti...
γ
0.02
N/m
358.15
Densiti...
λ
[0.12; 0.15]
W/m×K
[254.29; 383.37]
λ
0.15
W/m×K
254.29
Measure...
λ
0.14
W/m×K
264.08
Measure...
λ
0.14
W/m×K
274.02
Measure...
λ
0.14
W/m×K
283.95
Measure...
λ
0.14
W/m×K
293.74
Measure...
λ
0.14
W/m×K
303.70
Measure...
λ
0.13
W/m×K
313.76
Measure...
λ
0.13
W/m×K
323.67
Measure...
λ
0.13
W/m×K
333.63
Measure...
λ
0.12
W/m×K
343.56
Measure...
λ
0.12
W/m×K
353.55
Measure...
λ
0.12
W/m×K
363.41
Measure...
λ
0.12
W/m×K
373.40
Measure...
λ
0.12
W/m×K
383.37
Measure...
Correlations
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.67]
kPa
[329.12; 468.56]
The Yaw...
Equation ln(Pvp) = A + B/(T + C) Coefficient A 1.48813e+01 Coefficient B -3.87622e+03 Coefficient C -6.35120e+01 Temperature range, min. 329.12
Temperature range, max. 468.56
Pvap
1.33
kPa
329.12
Calculated Property
Pvap
2.98
kPa
344.61
Calculated Property
Pvap
6.12
kPa
360.11
Calculated Property
Pvap
11.72
kPa
375.60
Calculated Property
Pvap
21.08
kPa
391.09
Calculated Property
Pvap
35.98
kPa
406.59
Calculated Property
Pvap
58.62
kPa
422.08
Calculated Property
Pvap
91.73
kPa
437.57
Calculated Property
Pvap
138.51
kPa
453.07
Calculated Property
Pvap
202.67
kPa
468.56
Calculated Property
Similar Compounds
Find more compounds similar to Hexanoic acid, ethyl ester .
Mixtures
Sources
Crippen Method
Speed of sound measurement and prediction of ethyl hexanoate and ethyl octanoate at temperatures from (293.15 to 473.15) K and pressures from (0.1 to 10) MPa
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
Thermophysical properties of fatty acid methyl and ethyl esters
Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
Liquid-Liquid Equilibria for Ternary Mixtures of Water + Ethanol with 1-Hexanol, Butyl Propionate, or Ethyl Caproate
Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
Density and Viscosity of Binary Mixtures of Ethyl-2-methylbutyrate and Ethyl Hexanoate with Methanol, Ethanol, and 1-Propanol at (293.15, 303.15, 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 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
Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Ebulliometric Determination and Prediction of Vapor Liquid Equilibria for Binary Mixtures of Ethanol and Ethyl Hexanoate
Isothermal Vapor Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
Development of a Predictive Equation of State for CO2 + Ethyl Ester Mixtures Based on Critical Points Measurements
Joback Method
Estimated Solubility Method
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure
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