Physical Properties
Property
Value
Unit
Source
ω
0.3368
Relay (1.0) Calculated Property
Δc H°liquid
[-3766.00; -3589.00]
kJ/mol
Δc H°liquid
-3766.00
kJ/mol
NIST
Δc H°liquid
-3589.00
kJ/mol
NIST
Δf G°
-41.44
kJ/mol
Joback Calculated Property
Δf H°gas
-166.62
kJ/mol
Relay (1.0) Calculated Property
Δfus H°
11.61
kJ/mol
Joback Calculated Property
Δvap H°
42.16
kJ/mol
Relay (1.0) Calculated Property
IE
9.50
eV
NIST
log 10 WS
-0.44
Relay (1.0) Calculated Property
log Poct/wat
1.542
Crippen Calculated Property
McVol
92.670
ml/mol
McGowan Calculated Property
Pc
3505.43
kPa
Joback Calculated Property
Inp
[737.00; 747.00]
Inp
737.00
NIST
Inp
747.00
NIST
Inp
744.00
NIST
Inp
745.00
NIST
Inp
744.00
NIST
I
[1135.00; 1138.00]
I
1135.00
NIST
I
1138.00
NIST
I
1135.00
NIST
Tboil
[401.00; 402.70]
K
Tboil
401.00
K
NIST
Tboil
402.70
K
NIST
Tc
587.33
K
Relay (1.0) Calculated Property
Tfus
194.90
K
Relay (1.0) Calculated Property
Vc
0.334
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Δvap H
[33.50; 42.10]
kJ/mol
[378.50; 505.00]
Δvap H
42.10 ± 0.10
kJ/mol
378.50
NIST
Δvap H
39.40 ± 0.20
kJ/mol
378.50
NIST
Δvap H
36.60 ± 0.30
kJ/mol
378.50
NIST
Δvap H
33.50 ± 0.60
kJ/mol
378.50
NIST
Δvap H
34.60
kJ/mol
505.00
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
342.20
K
13.30
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[123.88; 289.38]
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 1.80200e+00
Coefficient B 5.25820e-01
Coefficient C -3.06800e-04
Coefficient D 6.85600e-08
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
123.88
J/mol×K
273.00
Calculated Property
Cp,gas
152.46
J/mol×K
353.78
Calculated Property
Cp,gas
177.99
J/mol×K
434.56
Calculated Property
Cp,gas
200.68
J/mol×K
515.33
Calculated Property
Cp,gas
220.75
J/mol×K
596.11
Calculated Property
Cp,gas
238.42
J/mol×K
676.89
Calculated Property
Cp,gas
253.90
J/mol×K
757.67
Calculated Property
Cp,gas
267.41
J/mol×K
838.44
Calculated Property
Cp,gas
279.16
J/mol×K
919.22
Calculated Property
Cp,gas
289.38
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0032665; 0.0002718]
Pa×s
[205.55; 398.19]
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 -1.08636e+01
Coefficient B 1.05643e+03
Coefficient C 0.00000e+00
Coefficient D 0.00000e+00
Coefficient E 0.00000e+00
Temperature range, min. 205.55
Temperature range, max. 398.19
η
0.0032665
Pa×s
205.55
Calculated Property
η
0.0020118
Pa×s
226.95
Calculated Property
η
0.0013470
Pa×s
248.36
Calculated Property
η
0.0009611
Pa×s
269.76
Calculated Property
η
0.0007207
Pa×s
291.17
Calculated Property
η
0.0005621
Pa×s
312.57
Calculated Property
η
0.0004527
Pa×s
333.98
Calculated Property
η
0.0003741
Pa×s
355.38
Calculated Property
η
0.0003160
Pa×s
376.78
Calculated Property
η
0.0002718
Pa×s
398.19
Calculated Property
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.66]
kPa
[297.12; 426.44]
The Yaws Handbook of Vapor Pressure
Equation ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A 1.47920e+01
Coefficient B -3.53956e+03
Coefficient C -5.30870e+01
Temperature range, min. 297.12
Temperature range, max. 426.44
Pvap
1.33
kPa
297.12
Calculated Property
Pvap
2.99
kPa
311.49
Calculated Property
Pvap
6.15
kPa
325.86
Calculated Property
Pvap
11.76
kPa
340.23
Calculated Property
Pvap
21.17
kPa
354.60
Calculated Property
Pvap
36.11
kPa
368.96
Calculated Property
Pvap
58.80
kPa
383.33
Calculated Property
Pvap
91.92
kPa
397.70
Calculated Property
Pvap
138.67
kPa
412.07
Calculated Property
Pvap
202.66
kPa
426.44
Calculated Property
Similar Compounds
Find more compounds similar to 5-Hexen-2-one .
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