Physical Properties
Property
Value
Unit
Source
ω
0.5664
Relay (1.0) Calculated Property
Δc H°solid
-6761.00
kJ/mol
NIST
Δf G°
128.78
kJ/mol
Joback Calculated Property
Δf H°gas
49.71
kJ/mol
NIST
Δf H°solid
-67.00
kJ/mol
NIST
Δfus H°
23.29
kJ/mol
Joback Calculated Property
Δsub H°
[116.60; 116.70]
kJ/mol
Δsub H°
116.60
kJ/mol
NIST
Δsub H°
116.70
kJ/mol
NIST
Δvap H°
85.56
kJ/mol
Relay (1.0) Calculated Property
IE
8.19
eV
Relay (1.0) Calculated Property
log 10 WS
-2.40
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
Tboil
[578.00; 585.20]
K
Tboil
585.20
K
NIST
Tboil
585.00
K
NIST
Tboil
578.00 ± 6.00
K
NIST
Tc
846.14
K
Relay (1.0) Calculated Property
Tfus
325.00
K
NIST
Vc
0.540
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Δfus H
23.40
kJ/mol
325.70
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
448.00
K
2.40
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
[0.0120116; 0.0000291]
Pa×s
[325.00; 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. 325.00
Temperature range, max. 619.91
η
0.0120116
Pa×s
325.00
Calculated Property
η
0.0037676
Pa×s
357.77
Calculated Property
η
0.0014356
Pa×s
390.54
Calculated Property
η
0.0006351
Pa×s
423.30
Calculated Property
η
0.0003159
Pa×s
456.07
Calculated Property
η
0.0001726
Pa×s
488.84
Calculated Property
η
0.0001017
Pa×s
521.61
Calculated Property
η
0.0000638
Pa×s
554.38
Calculated Property
η
0.0000422
Pa×s
587.14
Calculated Property
η
0.0000291
Pa×s
619.91
Calculated Property
Similar Compounds
Find more compounds similar to Phenol, 2-(phenylmethyl)- .
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