Physical Properties
Property
Value
Unit
Source
ω
0.2253
Relay (1.0) Calculated Property
Δc H°solid
-10466.00 ± 1.00
kJ/mol
NIST
Δf G°
-5.00
kJ/mol
Joback Calculated Property
Δf H°gas
-369.96
kJ/mol
Relay (1.0) Calculated Property
Δfus H°
6.96
kJ/mol
Joback Calculated Property
Δvap H°
73.14
kJ/mol
Relay (1.0) Calculated Property
IE
9.64
eV
Relay (1.0) Calculated Property
log 10 WS
-6.50
Relay (1.0) Calculated Property
log Poct/wat
6.242
Crippen Calculated Property
McVol
225.440
ml/mol
McGowan Calculated Property
Pc
1947.51
kPa
Joback Calculated Property
Inp
[1876.00; 1883.00]
Inp
1883.00
NIST
Inp
1880.00
NIST
Inp
1881.00
NIST
Inp
1876.00
NIST
Inp
1883.00
NIST
Tboil
595.41
K
Relay (1.0) Calculated Property
Tc
778.64
K
Relay (1.0) Calculated Property
Tfus
[332.00; 333.70]
K
Tfus
333.70 ± 0.30
K
NIST
Tfus
332.00 ± 0.50
K
NIST
Vc
0.767
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Δfus H
[1.26; 18.83]
kJ/mol
[271.20; 332.20]
Δfus H
18.83
kJ/mol
271.20
NIST
Δfus H
1.26
kJ/mol
283.20
NIST
Δfus H
4.18
kJ/mol
332.20
NIST
Δfus H
4.18
kJ/mol
332.20
NIST
Δfus S
[4.43; 69.42]
J/mol×K
[271.20; 332.20]
Δfus S
69.42
J/mol×K
271.20
NIST
Δfus S
4.43
J/mol×K
283.20
NIST
Δfus S
12.59
J/mol×K
332.20
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
368.70
K
0.10
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[255.60; 840.99]
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 -1.34410e+02
Coefficient B 1.57640e+00
Coefficient C -5.19000e-04
Coefficient D -8.20000e-08
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
255.60
J/mol×K
273.00
Calculated Property
Cp,gas
354.70
J/mol×K
353.78
Calculated Property
Cp,gas
445.89
J/mol×K
434.56
Calculated Property
Cp,gas
528.91
J/mol×K
515.33
Calculated Property
Cp,gas
603.50
J/mol×K
596.11
Calculated Property
Cp,gas
669.41
J/mol×K
676.89
Calculated Property
Cp,gas
726.37
J/mol×K
757.67
Calculated Property
Cp,gas
774.13
J/mol×K
838.44
Calculated Property
Cp,gas
812.42
J/mol×K
919.22
Calculated Property
Cp,gas
840.99
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0038119; 0.0000092]
Pa×s
[332.85; 621.24]
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 -1.85564e+01
Coefficient B 4.32266e+03
Coefficient C 0.00000e+00
Coefficient D 0.00000e+00
Coefficient E 0.00000e+00
Temperature range, min. 332.85
Temperature range, max. 621.24
η
0.0038119
Pa×s
332.85
Calculated Property
η
0.0012186
Pa×s
364.89
Calculated Property
η
0.0004683
Pa×s
396.94
Calculated Property
η
0.0002076
Pa×s
428.98
Calculated Property
η
0.0001031
Pa×s
461.02
Calculated Property
η
0.0000560
Pa×s
493.07
Calculated Property
η
0.0000328
Pa×s
525.11
Calculated Property
η
0.0000204
Pa×s
557.15
Calculated Property
η
0.0000134
Pa×s
589.20
Calculated Property
η
0.0000092
Pa×s
621.24
Calculated Property
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.65]
kPa
[417.59; 614.10]
The Yaws Handbook of Vapor Pressure
Equation ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A 1.36568e+01
Coefficient B -4.36416e+03
Coefficient C -9.11500e+01
Temperature range, min. 417.59
Temperature range, max. 614.10
Pvap
1.33
kPa
417.59
Calculated Property
Pvap
3.08
kPa
439.42
Calculated Property
Pvap
6.46
kPa
461.26
Calculated Property
Pvap
12.45
kPa
483.09
Calculated Property
Pvap
22.41
kPa
504.93
Calculated Property
Pvap
38.03
kPa
526.76
Calculated Property
Pvap
61.34
kPa
548.60
Calculated Property
Pvap
94.74
kPa
570.43
Calculated Property
Pvap
140.87
kPa
592.27
Calculated Property
Pvap
202.65
kPa
614.10
Calculated Property
Similar Compounds
Find more compounds similar to Cyclohexadecane .
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