Physical Properties
Property
Value
Unit
Source
Δf G°
-380.04
kJ/mol
Joback Calculated Property
Δf H°gas
-483.27
kJ/mol
Joback Calculated Property
Δf H°liquid
-625.00 ± 3.40
kJ/mol
NIST
Δfus H°
10.50
kJ/mol
Joback Calculated Property
Δvap H°
40.40
kJ/mol
Joback Calculated Property
IE
10.00
eV
NIST
log 10 WS
-0.13
Crippen Calculated Property
log Poct/wat
0.096
Crippen Calculated Property
McVol
76.230
ml/mol
McGowan Calculated Property
Pc
[4000.00; 4680.00]
kPa
Pc
4000.00 ± 200.00
kPa
NIST
Pc
4680.00 ± 405.30
kPa
NIST
Inp
[699.00; 706.00]
Inp
706.00
NIST
Inp
706.00
NIST
Inp
699.00
NIST
Inp
706.00
NIST
I
[1227.00; 1240.00]
I
1236.00
NIST
I
1240.00
NIST
I
1227.00
NIST
I
1227.00
NIST
S°gas
389.95
J/mol×K
NIST
Tboil
[403.55; 413.15]
K
Tboil
412.70
K
NIST
Tboil
412.70
K
NIST
Tboil
412.65 ± 0.40
K
NIST
Tboil
412.15 ± 1.00
K
NIST
Tboil
412.65 ± 0.50
K
NIST
Tboil
412.60 ± 0.50
K
NIST
Tboil
413.00 ± 0.40
K
NIST
Tboil
412.55 ± 1.00
K
NIST
Tboil
410.00 ± 3.00
K
NIST
Tboil
413.15 ± 0.30
K
NIST
Tboil
Outlier 403.55 ± 0.20
K
NIST
Tc
[569.00; 606.00]
K
Tc
606.00 ± 4.00
K
NIST
Tc
569.00 ± 20.00
K
NIST
Tfus
[199.02; 201.05]
K
Tfus
200.00
K
NIST
Tfus
200.15 ± 0.30
K
NIST
Tfus
199.05 ± 1.00
K
NIST
Tfus
199.02 ± 0.07
K
NIST
Tfus
199.11 ± 2.00
K
NIST
Tfus
200.15 ± 1.00
K
NIST
Tfus
201.05 ± 0.50
K
NIST
Tfus
200.15 ± 0.40
K
NIST
Tfus
200.05 ± 0.40
K
NIST
Vc
0.289
m3 /kmol
Joback Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[140.13; 176.35]
J/mol×K
[421.08; 613.71]
Cp,gas
140.13
J/mol×K
421.08
Joback Calculated Property
Cp,gas
146.68
J/mol×K
453.18
Joback Calculated Property
Cp,gas
153.04
J/mol×K
485.29
Joback Calculated Property
Cp,gas
159.19
J/mol×K
517.39
Joback Calculated Property
Cp,gas
165.13
J/mol×K
549.50
Joback Calculated Property
Cp,gas
170.85
J/mol×K
581.60
Joback Calculated Property
Cp,gas
176.35
J/mol×K
613.71
Joback Calculated Property
Cp,liquid
[168.20; 204.34]
J/mol×K
[303.20; 333.15]
Cp,liquid
168.20
J/mol×K
303.20
NIST
Cp,liquid
200.73
J/mol×K
313.15
Heat Ca...
Cp,liquid
204.34
J/mol×K
333.15
Heat Ca...
η
[0.0005210; 0.0008880]
Pa×s
[293.15; 338.15]
η
0.0008880
Pa×s
293.15
Densiti...
η
0.0008290
Pa×s
298.15
Densiti...
η
0.0007780
Pa×s
303.15
Densiti...
η
0.0007290
Pa×s
308.15
Densiti...
η
0.0006880
Pa×s
313.15
Densiti...
η
0.0006480
Pa×s
318.15
Densiti...
η
0.0006100
Pa×s
323.15
Densiti...
η
0.0005800
Pa×s
328.15
Densiti...
η
0.0005480
Pa×s
333.15
Densiti...
η
0.0005210
Pa×s
338.15
Densiti...
Δvap H
[43.30; 47.60]
kJ/mol
[366.50; 469.50]
Δvap H
45.50
kJ/mol
366.50
NIST
Δvap H
44.20
kJ/mol
374.00
NIST
Δvap H
43.30
kJ/mol
389.00
NIST
Δvap H
47.60
kJ/mol
469.50
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
[317.00; 317.20]
K
[2.00; 2.00]
Tboilr
317.20
K
2.00
NIST
Tboilr
317.00
K
2.00
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Pvap
[2.71e-05; 1447.59]
kPa
[200.15; 569.00]
KDB Vap...
Equation ln(Pvp) = A + B/T + C*ln(T) + D*T^2 Coefficient A 1.70607e+02 Coefficient B -1.12828e+04 Coefficient C -2.37023e+01 Coefficient D 2.12043e-05 Temperature range, min. 200.15
Temperature range, max. 569.00
Pvap
2.71e-05
kPa
200.15
Calculated Property
Pvap
6.96e-03
kPa
241.13
Calculated Property
Pvap
0.24
kPa
282.12
Calculated Property
Pvap
2.58
kPa
323.10
Calculated Property
Pvap
14.10
kPa
364.08
Calculated Property
Pvap
50.47
kPa
405.07
Calculated Property
Pvap
139.20
kPa
446.05
Calculated Property
Pvap
327.62
kPa
487.03
Calculated Property
Pvap
704.19
kPa
528.02
Calculated Property
Pvap
1447.59
kPa
569.00
Calculated Property
Similar Compounds
Find more compounds similar to Acetic anhydride .
Mixtures
Sources
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that the value is more than 2 standard deviations away from the
property mean.