Physical Properties
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Δfus H
36.16
kJ/mol
259.20
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
378.20
K
0.50
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[297.60; 698.12]
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 1.64800e+01
Coefficient B 1.18404e+00
Coefficient C -5.88800e-04
Coefficient D 8.64000e-08
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
297.60
J/mol×K
273.00
Calculated Property
Cp,gas
365.50
J/mol×K
353.78
Calculated Property
Cp,gas
426.91
J/mol×K
434.56
Calculated Property
Cp,gas
482.11
J/mol×K
515.33
Calculated Property
Cp,gas
531.37
J/mol×K
596.11
Calculated Property
Cp,gas
574.96
J/mol×K
676.89
Calculated Property
Cp,gas
613.16
J/mol×K
757.67
Calculated Property
Cp,gas
646.24
J/mol×K
838.44
Calculated Property
Cp,gas
674.47
J/mol×K
919.22
Calculated Property
Cp,gas
698.12
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0084429; 0.0002208]
Pa×s
[258.15; 505.02]
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 -1.22284e+01
Coefficient B 1.92424e+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. 258.15
Temperature range, max. 505.02
η
0.0084429
Pa×s
258.15
Calculated Property
η
0.0041262
Pa×s
285.58
Calculated Property
η
0.0022862
Pa×s
313.01
Calculated Property
η
0.0013931
Pa×s
340.44
Calculated Property
η
0.0009140
Pa×s
367.87
Calculated Property
η
0.0006358
Pa×s
395.30
Calculated Property
η
0.0004636
Pa×s
422.73
Calculated Property
η
0.0003513
Pa×s
450.16
Calculated Property
η
0.0002748
Pa×s
477.59
Calculated Property
η
0.0002208
Pa×s
505.02
Calculated Property
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.64]
kPa
[410.00; 555.04]
The Yaws Handbook of Vapor Pressure
Equation ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A 1.63515e+01
Coefficient B -5.12005e+03
Coefficient C -9.12700e+01
Temperature range, min. 410.00
Temperature range, max. 555.04
Pvap
1.33
kPa
410.00
Calculated Property
Pvap
2.89
kPa
426.12
Calculated Property
Pvap
5.83
kPa
442.23
Calculated Property
Pvap
11.06
kPa
458.35
Calculated Property
Pvap
19.88
kPa
474.46
Calculated Property
Pvap
34.10
kPa
490.58
Calculated Property
Pvap
56.07
kPa
506.69
Calculated Property
Pvap
88.84
kPa
522.81
Calculated Property
Pvap
136.18
kPa
538.92
Calculated Property
Pvap
202.64
kPa
555.04
Calculated Property
Similar Compounds
Find more compounds similar to Undecanoic acid, ethyl ester .
Sources
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.
Calculated This icon marks a calculated value or equation: a prediction, not a measurement.
Compiled This icon marks a compiled value or equation: taken from a data compilation such as ChemSep, not from an original measurement report.
These property values are available through the Cheméo API . A free account gives you an access key.