Physical Properties
Property
Value
Unit
Source
ω
0.4724
Relay (1.0) Calculated Property
Δf G°
-99.55
kJ/mol
Joback Calculated Property
Δf H°gas
-134.50
kJ/mol
Relay (1.0) Calculated Property
Δfus H°
14.40
kJ/mol
Joback Calculated Property
Δvap H°
63.52
kJ/mol
Relay (1.0) Calculated Property
IE
9.23
eV
Relay (1.0) Calculated Property
log 10 WS
-1.69
Relay (1.0) Calculated Property
log Poct/wat
1.068
Crippen Calculated Property
McVol
102.960
ml/mol
McGowan Calculated Property
Pc
4339.67
kPa
Joback Calculated Property
Tboil
486.86
K
Relay (1.0) Calculated Property
Tc
755.90
K
Relay (1.0) Calculated Property
Tfus
321.67
K
Relay (1.0) Calculated Property
Vc
0.378
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Δvap H
59.70
kJ/mol
407.50
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
415.20
K
16.70
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[123.77; 293.33]
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 -1.95300e+01
Coefficient B 6.31400e-01
Coefficient C -4.16900e-04
Coefficient D 9.83600e-08
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
123.77
J/mol×K
273.00
Calculated Property
Cp,gas
156.02
J/mol×K
353.78
Calculated Property
Cp,gas
184.19
J/mol×K
434.56
Calculated Property
Cp,gas
208.60
J/mol×K
515.33
Calculated Property
Cp,gas
229.55
J/mol×K
596.11
Calculated Property
Cp,gas
247.35
J/mol×K
676.89
Calculated Property
Cp,gas
262.32
J/mol×K
757.67
Calculated Property
Cp,gas
274.76
J/mol×K
838.44
Calculated Property
Cp,gas
285.00
J/mol×K
919.22
Calculated Property
Cp,gas
293.33
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0029837; 0.0003383]
Pa×s
[298.27; 516.73]
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 -1.09642e+01
Coefficient B 1.53596e+03
Coefficient C 0.00000e+00
Coefficient D 0.00000e+00
Coefficient E 0.00000e+00
Temperature range, min. 298.27
Temperature range, max. 516.73
η
0.0029837
Pa×s
298.27
Calculated Property
η
0.0020251
Pa×s
322.54
Calculated Property
η
0.0014511
Pa×s
346.82
Calculated Property
η
0.0010862
Pa×s
371.09
Calculated Property
η
0.0008424
Pa×s
395.36
Calculated Property
η
0.0006729
Pa×s
419.63
Calculated Property
η
0.0005508
Pa×s
443.91
Calculated Property
η
0.0004604
Pa×s
468.18
Calculated Property
η
0.0003916
Pa×s
492.45
Calculated Property
η
0.0003383
Pa×s
516.73
Calculated Property
Property
Value
Unit
Temperature (K)
Source
Pvap
[0.65; 101.83]
kPa
[348.00; 466.70]
NIST
Equation ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A 1.78087e+01
Coefficient B -5.65047e+03
Coefficient C -3.81620e+01
Reference Stull, 1947
Temperature range, min. 348.00
Temperature range, max. 466.70
Pvap
0.65
kPa
348.00
Calculated Property
Pvap
1.37
kPa
361.19
Calculated Property
Pvap
2.73
kPa
374.38
Calculated Property
Pvap
5.14
kPa
387.57
Calculated Property
Pvap
9.26
kPa
400.76
Calculated Property
Pvap
15.99
kPa
413.94
Calculated Property
Pvap
26.63
kPa
427.13
Calculated Property
Pvap
42.88
kPa
440.32
Calculated Property
Pvap
66.99
kPa
453.51
Calculated Property
Pvap
101.83
kPa
466.70
Calculated Property
Similar Compounds
Find more compounds similar to Phenylglyoxal .
Sources
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