Physical Properties
Temperature Dependent Properties
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
357.20
K
0.10
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[115.00; 256.61]
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 -1.53300e+01
Coefficient B 5.94440e-01
Coefficient C -4.68600e-04
Coefficient D 1.46100e-07
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
115.00
J/mol×K
273.00
Calculated Property
Cp,gas
142.79
J/mol×K
353.78
Calculated Property
Cp,gas
166.49
J/mol×K
434.56
Calculated Property
Cp,gas
186.55
J/mol×K
515.33
Calculated Property
Cp,gas
203.45
J/mol×K
596.11
Calculated Property
Cp,gas
217.65
J/mol×K
676.89
Calculated Property
Cp,gas
229.60
J/mol×K
757.67
Calculated Property
Cp,gas
239.77
J/mol×K
838.44
Calculated Property
Cp,gas
248.62
J/mol×K
919.22
Calculated Property
Cp,gas
256.61
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0034441; 0.0001949]
Pa×s
[353.95; 503.89]
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 -1.53226e+01
Coefficient B 3.41615e+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. 353.95
Temperature range, max. 503.89
η
0.0034441
Pa×s
353.95
Calculated Property
η
0.0022318
Pa×s
370.61
Calculated Property
η
0.0015012
Pa×s
387.27
Calculated Property
η
0.0010434
Pa×s
403.93
Calculated Property
η
0.0007464
Pa×s
420.59
Calculated Property
η
0.0005477
Pa×s
437.25
Calculated Property
η
0.0004112
Pa×s
453.91
Calculated Property
η
0.0003150
Pa×s
470.57
Calculated Property
η
0.0002457
Pa×s
487.23
Calculated Property
η
0.0001949
Pa×s
503.89
Calculated Property
Similar Compounds
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Sources
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