Physical Properties
Property
Value
Unit
Source
ω
0.4894
Relay (1.0) Calculated Property
Δc H°liquid
-3436.50 ± 0.60
kJ/mol
NIST
Δf G°
-415.73
kJ/mol
Joback Calculated Property
Δf H°gas
-611.65
kJ/mol
Relay (1.0) Calculated Property
Δf H°liquid
-639.50 ± 0.60
kJ/mol
NIST
Δfus H°
16.85
kJ/mol
Joback Calculated Property
Δvap H°
50.10
kJ/mol
Relay (1.0) Calculated Property
IE
9.53
eV
Relay (1.0) Calculated Property
log 10 WS
-0.25
Relay (1.0) Calculated Property
log Poct/wat
0.586
Crippen Calculated Property
McVol
108.710
ml/mol
McGowan Calculated Property
Pc
3065.95
kPa
Joback Calculated Property
Tboil
429.04
K
Relay (1.0) Calculated Property
Tc
603.94
K
Relay (1.0) Calculated Property
Tfus
220.73
K
Relay (1.0) Calculated Property
Vc
0.417
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Δvap H
46.10
kJ/mol
380.00
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
333.50 ± 0.50
K
2.40
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[164.51; 355.48]
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 4.83430e+01
Coefficient B 4.55840e-01
Coefficient C -9.70000e-05
Coefficient D -5.17000e-08
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
164.51
J/mol×K
273.00
Calculated Property
Cp,gas
195.18
J/mol×K
353.78
Calculated Property
Cp,gas
223.87
J/mol×K
434.56
Calculated Property
Cp,gas
250.42
J/mol×K
515.33
Calculated Property
Cp,gas
274.65
J/mol×K
596.11
Calculated Property
Cp,gas
296.42
J/mol×K
676.89
Calculated Property
Cp,gas
315.55
J/mol×K
757.67
Calculated Property
Cp,gas
331.88
J/mol×K
838.44
Calculated Property
Cp,gas
345.24
J/mol×K
919.22
Calculated Property
Cp,gas
355.48
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0042765; 0.0002356]
Pa×s
[221.94; 413.90]
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 -1.17050e+01
Coefficient B 1.38721e+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. 221.94
Temperature range, max. 413.90
η
0.0042765
Pa×s
221.94
Calculated Property
η
0.0024722
Pa×s
243.27
Calculated Property
η
0.0015612
Pa×s
264.60
Calculated Property
η
0.0010559
Pa×s
285.93
Calculated Property
η
0.0007540
Pa×s
307.26
Calculated Property
η
0.0005624
Pa×s
328.59
Calculated Property
η
0.0004348
Pa×s
349.92
Calculated Property
η
0.0003463
Pa×s
371.24
Calculated Property
η
0.0002826
Pa×s
392.57
Calculated Property
η
0.0002356
Pa×s
413.90
Calculated Property
Similar Compounds
Find more compounds similar to Acetic acid, ethoxy-, ethyl ester .
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