Physical Properties
Property
Value
Unit
Source
ω
0.5671
Relay (1.0) Calculated Property
Δc H°solid
[-7410.00; -7386.00]
kJ/mol
Δc H°solid
-7393.00 ± 2.00
kJ/mol
NIST
Δc H°solid
-7386.00 ± 4.60
kJ/mol
NIST
Δc H°solid
-7395.00 ± 3.00
kJ/mol
NIST
Δc H°solid
-7410.00
kJ/mol
NIST
Δf G°
42.40
kJ/mol
Joback Calculated Property
Δf H°gas
-109.20 ± 2.00
kJ/mol
NIST
Δf H°solid
[-241.00; -222.30]
kJ/mol
Δf H°solid
-228.00 ± 12.00
kJ/mol
NIST
Δf H°solid
-222.30
kJ/mol
NIST
Δf H°solid
-241.00
kJ/mol
NIST
Δfus H°
25.89
kJ/mol
Joback Calculated Property
Δsub H°
[50.20; 115.70]
kJ/mol
Δsub H°
113.30 ± 4.80
kJ/mol
NIST
Δsub H°
115.70 ± 0.90
kJ/mol
NIST
Δsub H°
115.70 ± 0.90
kJ/mol
NIST
Δsub H°
50.20
kJ/mol
NIST
Δvap H°
88.90
kJ/mol
Relay (1.0) Calculated Property
IE
[8.30; 8.45]
eV
IE
8.30
eV
NIST
IE
8.45 ± 0.05
eV
NIST
log 10 WS
-3.68
Relay (1.0) Calculated Property
log Poct/wat
3.142
Crippen Calculated Property
McVol
177.830
ml/mol
McGowan Calculated Property
Pc
2859.68
kPa
Joback Calculated Property
Tboil
607.37
K
Relay (1.0) Calculated Property
Tc
888.48
K
Relay (1.0) Calculated Property
Tfus
[350.65; 351.00]
K
Tfus
350.65
K
Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus
351.00 ± 3.00
K
NIST
Vc
0.651
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
493.20
K
2.40
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[211.02; 534.18]
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 -6.38390e+01
Coefficient B 1.21500e+00
Coefficient C -8.17200e-04
Coefficient D 2.00220e-07
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
211.02
J/mol×K
273.00
Calculated Property
Cp,gas
272.59
J/mol×K
353.78
Calculated Property
Cp,gas
326.26
J/mol×K
434.56
Calculated Property
Cp,gas
372.67
J/mol×K
515.33
Calculated Property
Cp,gas
412.46
J/mol×K
596.11
Calculated Property
Cp,gas
446.25
J/mol×K
676.89
Calculated Property
Cp,gas
474.69
J/mol×K
757.67
Calculated Property
Cp,gas
498.40
J/mol×K
838.44
Calculated Property
Cp,gas
518.02
J/mol×K
919.22
Calculated Property
Cp,gas
534.18
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0046108; 0.0002125]
Pa×s
[350.82; 665.78]
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 -1.18842e+01
Coefficient B 2.28206e+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. 350.82
Temperature range, max. 665.78
η
0.0046108
Pa×s
350.82
Calculated Property
η
0.0025558
Pa×s
385.82
Calculated Property
η
0.0015628
Pa×s
420.82
Calculated Property
η
0.0010306
Pa×s
455.81
Calculated Property
η
0.0007212
Pa×s
490.81
Calculated Property
η
0.0005293
Pa×s
525.80
Calculated Property
η
0.0004037
Pa×s
560.80
Calculated Property
η
0.0003179
Pa×s
595.79
Calculated Property
η
0.0002570
Pa×s
630.79
Calculated Property
η
0.0002125
Pa×s
665.78
Calculated Property
Similar Compounds
Find more compounds similar to Dibenzoylmethane .
Sources
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