Physical Properties
Property
Value
Unit
Source
ω
0.5903
Relay (1.0) Calculated Property
Δc H°solid
-6774.00
kJ/mol
NIST
Δf G°
128.78
kJ/mol
Joback Calculated Property
Δf H°gas
63.51
kJ/mol
NIST
Δf H°solid
-54.00
kJ/mol
NIST
Δfus H°
23.29
kJ/mol
Joback Calculated Property
Δsub H°
[117.50; 117.90]
kJ/mol
Δsub H°
117.90
kJ/mol
NIST
Δsub H°
117.50
kJ/mol
NIST
Δvap H°
90.30
kJ/mol
Relay (1.0) Calculated Property
IE
8.45 ± 0.05
eV
NIST
log 10 WS
-2.68
Relay (1.0) Calculated Property
log Poct/wat
2.983
Crippen Calculated Property
McVol
152.380
ml/mol
McGowan Calculated Property
Pc
3650.93
kPa
Joback Calculated Property
Inp
[295.40; 295.40]
Inp
295.40
NIST
Inp
295.40
NIST
Tboil
[594.00; 595.20]
K
Tboil
595.20
K
NIST
Tboil
594.00 ± 1.00
K
NIST
Tc
852.43
K
Relay (1.0) Calculated Property
Tfus
359.00
K
NIST
Vc
0.540
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Δsub H
97.40
kJ/mol
324.00
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
[428.50; 472.20]
K
[0.50; 1.30]
Tboilr
428.50 ± 1.50
K
0.50
NIST
Tboilr
472.20
K
1.30
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[183.64; 475.38]
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 -8.56590e+01
Coefficient B 1.23560e+00
Coefficient C -1.00216e-03
Coefficient D 3.27600e-07
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
183.64
J/mol×K
273.00
Calculated Property
Cp,gas
240.55
J/mol×K
353.78
Calculated Property
Cp,gas
288.91
J/mol×K
434.56
Calculated Property
Cp,gas
329.78
J/mol×K
515.33
Calculated Property
Cp,gas
364.17
J/mol×K
596.11
Calculated Property
Cp,gas
393.14
J/mol×K
676.89
Calculated Property
Cp,gas
417.70
J/mol×K
757.67
Calculated Property
Cp,gas
438.91
J/mol×K
838.44
Calculated Property
Cp,gas
457.79
J/mol×K
919.22
Calculated Property
Cp,gas
475.38
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0036218; 0.0000291]
Pa×s
[359.00; 619.91]
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 -1.70808e+01
Coefficient B 4.11414e+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. 359.00
Temperature range, max. 619.91
η
0.0036218
Pa×s
359.00
Calculated Property
η
0.0015383
Pa×s
387.99
Calculated Property
η
0.0007360
Pa×s
416.98
Calculated Property
η
0.0003876
Pa×s
445.97
Calculated Property
η
0.0002207
Pa×s
474.96
Calculated Property
η
0.0001341
Pa×s
503.95
Calculated Property
η
0.0000860
Pa×s
532.94
Calculated Property
η
0.0000578
Pa×s
561.93
Calculated Property
η
0.0000403
Pa×s
590.92
Calculated Property
η
0.0000291
Pa×s
619.91
Calculated Property
Similar Compounds
Find more compounds similar to p-Benzylphenol .
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