Physical Properties
Property
Value
Unit
Source
ω
0.3032
Relay (1.0) Calculated Property
Δf G°
178.59
kJ/mol
Joback Calculated Property
Δf H°gas
127.30 ± 1.30
kJ/mol
NIST
Δf H°liquid
53.00 ± 2.00
kJ/mol
NIST
Δfus H°
12.33
kJ/mol
Joback Calculated Property
Δvap H°
[50.60; 57.70]
kJ/mol
Δvap H°
57.40 ± 0.30
kJ/mol
NIST
Δvap H°
57.70
kJ/mol
NIST
Δvap H°
50.60 ± 1.40
kJ/mol
NIST
IE
[8.73; 8.91]
eV
IE
8.73 ± 0.02
eV
NIST
IE
8.80
eV
NIST
IE
8.91
eV
NIST
log 10 WS
-2.97
Relay (1.0) Calculated Property
log Poct/wat
2.622
Crippen Calculated Property
McVol
111.550
ml/mol
McGowan Calculated Property
Pc
4000.70
kPa
Joback Calculated Property
Inp
1174.00
NIST
Tboil
495.95
K
Relay (1.0) Calculated Property
Tc
748.52
K
Relay (1.0) Calculated Property
Tfus
[297.60; 299.45]
K
Tfus
297.60
K
NIST
Tfus
299.45 ± 0.50
K
NIST
Vc
0.387
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Δfus H
[13.20; 13.20]
kJ/mol
[299.50; 299.50]
Δfus H
13.20
kJ/mol
299.50
NIST
Δfus H
13.20
kJ/mol
299.50
NIST
Δvap H
46.80
kJ/mol
380.00
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
[366.00; 366.20]
K
[1.30; 1.30]
Tboilr
366.20
K
1.30
NIST
Tboilr
366.00
K
1.30
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[113.80; 271.11]
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 -2.56890e+01
Coefficient B 6.28900e-01
Coefficient C -4.69600e-04
Coefficient D 1.37500e-07
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
113.80
J/mol×K
273.00
Calculated Property
Cp,gas
144.12
J/mol×K
353.78
Calculated Property
Cp,gas
170.21
J/mol×K
434.56
Calculated Property
Cp,gas
192.51
J/mol×K
515.33
Calculated Property
Cp,gas
211.46
J/mol×K
596.11
Calculated Property
Cp,gas
227.49
J/mol×K
676.89
Calculated Property
Cp,gas
241.03
J/mol×K
757.67
Calculated Property
Cp,gas
252.53
J/mol×K
838.44
Calculated Property
Cp,gas
262.41
J/mol×K
919.22
Calculated Property
Cp,gas
271.11
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0018585; 0.0002787]
Pa×s
[298.52; 512.06]
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 -1.08383e+01
Coefficient B 1.35840e+03
Coefficient C 0.00000e+00
Coefficient D 0.00000e+00
Coefficient E 0.00000e+00
Temperature range, min. 298.52
Temperature range, max. 512.06
η
0.0018585
Pa×s
298.52
Calculated Property
η
0.0013295
Pa×s
322.25
Calculated Property
η
0.0009957
Pa×s
345.98
Calculated Property
η
0.0007739
Pa×s
369.70
Calculated Property
η
0.0006201
Pa×s
393.43
Calculated Property
η
0.0005096
Pa×s
417.15
Calculated Property
η
0.0004276
Pa×s
440.88
Calculated Property
η
0.0003654
Pa×s
464.60
Calculated Property
η
0.0003170
Pa×s
488.33
Calculated Property
η
0.0002787
Pa×s
512.06
Calculated Property
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.64]
kPa
[354.99; 519.29]
The Yaws Handbook of Vapor Pressure
Equation ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A 1.38427e+01
Coefficient B -3.78202e+03
Coefficient C -7.59750e+01
Temperature range, min. 354.99
Temperature range, max. 519.29
Pvap
1.33
kPa
354.99
Calculated Property
Pvap
3.07
kPa
373.25
Calculated Property
Pvap
6.40
kPa
391.50
Calculated Property
Pvap
12.33
kPa
409.76
Calculated Property
Pvap
22.19
kPa
428.01
Calculated Property
Pvap
37.68
kPa
446.27
Calculated Property
Pvap
60.88
kPa
464.52
Calculated Property
Pvap
94.23
kPa
482.78
Calculated Property
Pvap
140.48
kPa
501.03
Calculated Property
Pvap
202.64
kPa
519.29
Calculated Property
Similar Compounds
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