Physical Properties
Property
Value
Unit
Source
ω
0.3488
Relay (1.0) Calculated Property
Δc H°solid
-5079.80 ± 6.30
kJ/mol
NIST
Δf G°
300.87
kJ/mol
Joback Calculated Property
Δf H°gas
235.00 ± 9.20
kJ/mol
NIST
Δf H°solid
144.00 ± 6.30
kJ/mol
NIST
Δfus H°
16.73
kJ/mol
Joback Calculated Property
Δsub H°
90.80 ± 6.70
kJ/mol
NIST
Δvap H°
69.40
kJ/mol
Relay (1.0) Calculated Property
IE
8.04
eV
Relay (1.0) Calculated Property
log 10 WS
-5.24
Relay (1.0) Calculated Property
log Poct/wat
3.444
Crippen Calculated Property
McVol
134.360
ml/mol
McGowan Calculated Property
Pc
3722.56
kPa
Joback Calculated Property
Tboil
582.58
K
Relay (1.0) Calculated Property
Tc
852.70
K
Relay (1.0) Calculated Property
Tfus
327.50 ± 0.50
K
NIST
Vc
0.476
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Δfus H
[16.04; 16.04]
kJ/mol
[327.60; 327.60]
Δfus H
16.04
kJ/mol
327.60
NIST
Δfus H
16.04
kJ/mol
327.60
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
445.20
K
2.80
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[138.99; 332.06]
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 -4.55600e+01
Coefficient B 8.50700e-01
Coefficient C -7.02480e-04
Coefficient D 2.29400e-07
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
138.99
J/mol×K
273.00
Calculated Property
Cp,gas
177.63
J/mol×K
353.78
Calculated Property
Cp,gas
210.29
J/mol×K
434.56
Calculated Property
Cp,gas
237.67
J/mol×K
515.33
Calculated Property
Cp,gas
260.52
J/mol×K
596.11
Calculated Property
Cp,gas
279.55
J/mol×K
676.89
Calculated Property
Cp,gas
295.50
J/mol×K
757.67
Calculated Property
Cp,gas
309.08
J/mol×K
838.44
Calculated Property
Cp,gas
321.03
J/mol×K
919.22
Calculated Property
Cp,gas
332.06
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0021959; 0.0003759]
Pa×s
[327.50; 592.60]
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 -1.00664e+01
Coefficient B 1.29206e+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. 327.50
Temperature range, max. 592.60
η
0.0021959
Pa×s
327.50
Calculated Property
η
0.0015857
Pa×s
356.96
Calculated Property
η
0.0012034
Pa×s
386.41
Calculated Property
η
0.0009496
Pa×s
415.87
Calculated Property
η
0.0007732
Pa×s
445.32
Calculated Property
η
0.0006458
Pa×s
474.78
Calculated Property
η
0.0005509
Pa×s
504.23
Calculated Property
η
0.0004782
Pa×s
533.69
Calculated Property
η
0.0004214
Pa×s
563.14
Calculated Property
η
0.0003759
Pa×s
592.60
Calculated Property
Similar Compounds
Find more compounds similar to Naphthalene, 2-iodo- .
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