Physical Properties
Property
Value
Unit
Source
ω
0.4948
Relay (1.0) Calculated Property
Δf G°
14.29
kJ/mol
Joback Calculated Property
Δf H°gas
-76.21
kJ/mol
Relay (1.0) Calculated Property
Δfus H°
17.40
kJ/mol
Joback Calculated Property
Δvap H°
66.44
kJ/mol
Relay (1.0) Calculated Property
IE
9.60
eV
NIST
log 10 WS
-2.57
Relay (1.0) Calculated Property
log Poct/wat
2.264
Crippen Calculated Property
McVol
118.890
ml/mol
McGowan Calculated Property
Pc
4311.22
kPa
Joback Calculated Property
Inp
[1304.00; 1321.00]
Inp
1304.00
NIST
Inp
1321.00
NIST
Inp
1321.00
NIST
Ip
[1971.00; 1971.00]
Ip
1971.00
NIST
Ip
1971.00
NIST
Tboil
526.07
K
Relay (1.0) Calculated Property
Tc
762.99
K
Relay (1.0) Calculated Property
Tfus
[324.00; 324.00]
K
Tfus
324.00
K
NIST
Tfus
324.00 ± 1.00
K
NIST
Vc
0.416
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
[408.00; 408.20]
K
[2.40; 2.40]
Tboilr
408.20
K
2.40
NIST
Tboilr
408.00
K
2.40
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[132.85; 311.62]
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 -2.27390e+01
Coefficient B 6.95100e-01
Coefficient C -4.95300e-04
Coefficient D 1.34560e-07
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
132.85
J/mol×K
273.00
Calculated Property
Cp,gas
167.14
J/mol×K
353.78
Calculated Property
Cp,gas
196.83
J/mol×K
434.56
Calculated Property
Cp,gas
222.35
J/mol×K
515.33
Calculated Property
Cp,gas
244.12
J/mol×K
596.11
Calculated Property
Cp,gas
262.56
J/mol×K
676.89
Calculated Property
Cp,gas
278.11
J/mol×K
757.67
Calculated Property
Cp,gas
291.19
J/mol×K
838.44
Calculated Property
Cp,gas
302.21
J/mol×K
919.22
Calculated Property
Cp,gas
311.62
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0023148; 0.0003145]
Pa×s
[324.00; 537.52]
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 -1.10935e+01
Coefficient B 1.62811e+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. 324.00
Temperature range, max. 537.52
η
0.0023148
Pa×s
324.00
Calculated Property
η
0.0016429
Pa×s
347.72
Calculated Property
η
0.0012183
Pa×s
371.45
Calculated Property
η
0.0009364
Pa×s
395.17
Calculated Property
η
0.0007415
Pa×s
418.90
Calculated Property
η
0.0006021
Pa×s
442.62
Calculated Property
η
0.0004993
Pa×s
466.35
Calculated Property
η
0.0004217
Pa×s
490.07
Calculated Property
η
0.0003617
Pa×s
513.80
Calculated Property
η
0.0003145
Pa×s
537.52
Calculated Property
Similar Compounds
Find more compounds similar to Ethanone, 2-bromo-1-phenyl- .
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