Physical Properties
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Δvap H
64.60
kJ/mol
461.50
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
428.20
K
2.00
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[224.93; 560.50]
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 -3.54750e+01
Coefficient B 1.13192e+00
Coefficient C -6.95900e-04
Coefficient D 1.59960e-07
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
224.93
J/mol×K
273.00
Calculated Property
Cp,gas
284.96
J/mol×K
353.78
Calculated Property
Cp,gas
338.12
J/mol×K
434.56
Calculated Property
Cp,gas
384.92
J/mol×K
515.33
Calculated Property
Cp,gas
425.87
J/mol×K
596.11
Calculated Property
Cp,gas
461.47
J/mol×K
676.89
Calculated Property
Cp,gas
492.23
J/mol×K
757.67
Calculated Property
Cp,gas
518.65
J/mol×K
838.44
Calculated Property
Cp,gas
541.24
J/mol×K
919.22
Calculated Property
Cp,gas
560.51
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0047245; 0.0002476]
Pa×s
[289.77; 547.80]
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 -1.16155e+01
Coefficient B 1.81413e+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. 289.77
Temperature range, max. 547.80
η
0.0047245
Pa×s
289.77
Calculated Property
η
0.0026889
Pa×s
318.44
Calculated Property
η
0.0016797
Pa×s
347.11
Calculated Property
η
0.0011274
Pa×s
375.78
Calculated Property
η
0.0008007
Pa×s
404.45
Calculated Property
η
0.0005950
Pa×s
433.12
Calculated Property
η
0.0004588
Pa×s
461.79
Calculated Property
η
0.0003646
Pa×s
490.46
Calculated Property
η
0.0002973
Pa×s
519.13
Calculated Property
η
0.0002476
Pa×s
547.80
Calculated Property
Similar Compounds
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Sources
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