Physical Properties
Property
Value
Unit
Source
ω
0.7243
Relay (1.0) Calculated Property
Δf G°
17.33
kJ/mol
Joback Calculated Property
Δf H°gas
-181.35
kJ/mol
Relay (1.0) Calculated Property
Δfus H°
22.38
kJ/mol
Joback Calculated Property
Δvap H°
88.87
kJ/mol
Relay (1.0) Calculated Property
IE
8.82
eV
Relay (1.0) Calculated Property
log 10 WS
-2.29
Relay (1.0) Calculated Property
log Poct/wat
2.392
Crippen Calculated Property
McVol
147.960
ml/mol
McGowan Calculated Property
Pc
2918.68
kPa
Joback Calculated Property
Tboil
555.13
K
Relay (1.0) Calculated Property
Tc
768.31
K
Relay (1.0) Calculated Property
Tfus
265.24
K
Relay (1.0) Calculated Property
Vc
0.539
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Δvap H
58.20
kJ/mol
401.50
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
428.20
K
2.70
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[194.08; 486.98]
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 -3.57250e+01
Coefficient B 1.00390e+00
Coefficient C -6.36200e-04
Coefficient D 1.55000e-07
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
194.08
J/mol×K
273.00
Calculated Property
Cp,gas
246.67
J/mol×K
353.78
Calculated Property
Cp,gas
293.11
J/mol×K
434.56
Calculated Property
Cp,gas
333.88
J/mol×K
515.33
Calculated Property
Cp,gas
369.47
J/mol×K
596.11
Calculated Property
Cp,gas
400.38
J/mol×K
676.89
Calculated Property
Cp,gas
427.10
J/mol×K
757.67
Calculated Property
Cp,gas
450.11
J/mol×K
838.44
Calculated Property
Cp,gas
469.90
J/mol×K
919.22
Calculated Property
Cp,gas
486.98
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0116411; 0.0001328]
Pa×s
[300.97; 532.18]
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 -1.47506e+01
Coefficient B 3.09921e+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. 300.97
Temperature range, max. 532.18
η
0.0116411
Pa×s
300.97
Calculated Property
η
0.0051795
Pa×s
326.66
Calculated Property
η
0.0025934
Pa×s
352.35
Calculated Property
η
0.0014265
Pa×s
378.04
Calculated Property
η
0.0008467
Pa×s
403.73
Calculated Property
η
0.0005349
Pa×s
429.42
Calculated Property
η
0.0003559
Pa×s
455.11
Calculated Property
η
0.0002474
Pa×s
480.80
Calculated Property
η
0.0001784
Pa×s
506.49
Calculated Property
η
0.0001328
Pa×s
532.18
Calculated Property
Similar Compounds
Find more compounds similar to Benzenepentanol .
Mixtures
Sources
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