Physical Properties
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Δfus H
38.09
kJ/mol
322.40
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
[465.70; 470.20]
K
[0.10; 0.10]
Tboilr
465.70
K
0.10
NIST
Tboilr
470.20
K
0.10
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[410.60; 1006.63]
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 -5.90260e+01
Coefficient B 2.07452e+00
Coefficient C -1.40616e-03
Coefficient D 3.97300e-07
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
410.60
J/mol×K
273.00
Calculated Property
Cp,gas
516.49
J/mol×K
353.78
Calculated Property
Cp,gas
609.53
J/mol×K
434.56
Calculated Property
Cp,gas
690.98
J/mol×K
515.33
Calculated Property
Cp,gas
762.10
J/mol×K
596.11
Calculated Property
Cp,gas
824.14
J/mol×K
676.89
Calculated Property
Cp,gas
878.35
J/mol×K
757.67
Calculated Property
Cp,gas
926.00
J/mol×K
838.44
Calculated Property
Cp,gas
968.35
J/mol×K
919.22
Calculated Property
Cp,gas
1006.63
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0315988; 0.0000131]
Pa×s
[325.92; 686.57]
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 -1.82863e+01
Coefficient B 4.83400e+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. 325.92
Temperature range, max. 686.57
η
0.0315988
Pa×s
325.92
Calculated Property
η
0.0062294
Pa×s
366.00
Calculated Property
η
0.0016920
Pa×s
406.07
Calculated Property
η
0.0005808
Pa×s
446.14
Calculated Property
η
0.0002378
Pa×s
486.21
Calculated Property
η
0.0001115
Pa×s
526.28
Calculated Property
η
0.0000582
Pa×s
566.35
Calculated Property
η
0.0000331
Pa×s
606.42
Calculated Property
η
0.0000202
Pa×s
646.49
Calculated Property
η
0.0000131
Pa×s
686.57
Calculated Property
Similar Compounds
Find more compounds similar to Phenol, 3-pentadecyl- .
Mixtures
Sources
Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
Cheméo Relay (1.0)
Crippen Method
Crippen Method
Solubilities of 3-Pentadecylphenol in Ethanol, 1-Butanol, Toluene, Acetone, Tetrachloromethane, and Ethyl Acetate
Joback Method
McGowan Method
NIST Webbook
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