Physical Properties
Property
Value
Unit
Source
ω
0.4152
Relay (1.0) Calculated Property
Δf G°
239.24
kJ/mol
Joback Calculated Property
Δf H°gas
71.56
kJ/mol
Relay (1.0) Calculated Property
Δfus H°
19.11
kJ/mol
Joback Calculated Property
Δvap H°
68.53
kJ/mol
Relay (1.0) Calculated Property
IE
8.27
eV
Relay (1.0) Calculated Property
log 10 WS
-4.33
Relay (1.0) Calculated Property
log Poct/wat
3.579
Crippen Calculated Property
McVol
134.870
ml/mol
McGowan Calculated Property
Pc
3265.31
kPa
Joback Calculated Property
Inp
[266.23; 266.23]
Inp
266.23
NIST
Inp
266.23
NIST
Tboil
564.70
K
NIST
Tc
820.09
K
Relay (1.0) Calculated Property
Tfus
312.70
K
Relay (1.0) Calculated Property
Vc
0.491
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Δvap H
59.80
kJ/mol
494.00
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
441.20
K
3.30
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[156.53; 382.75]
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 -4.52690e+01
Coefficient B 9.13500e-01
Coefficient C -6.95880e-04
Coefficient D 2.10400e-07
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
156.53
J/mol×K
273.00
Calculated Property
Cp,gas
200.13
J/mol×K
353.78
Calculated Property
Cp,gas
237.55
J/mol×K
434.56
Calculated Property
Cp,gas
269.48
J/mol×K
515.33
Calculated Property
Cp,gas
296.57
J/mol×K
596.11
Calculated Property
Cp,gas
319.48
J/mol×K
676.89
Calculated Property
Cp,gas
338.90
J/mol×K
757.67
Calculated Property
Cp,gas
355.47
J/mol×K
838.44
Calculated Property
Cp,gas
369.86
J/mol×K
919.22
Calculated Property
Cp,gas
382.75
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0016514; 0.0003307]
Pa×s
[315.29; 545.32]
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 -1.02189e+01
Coefficient B 1.20212e+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. 315.29
Temperature range, max. 545.32
η
0.0016514
Pa×s
315.29
Calculated Property
η
0.0012408
Pa×s
340.85
Calculated Property
η
0.0009702
Pa×s
366.41
Calculated Property
η
0.0007833
Pa×s
391.97
Calculated Property
η
0.0006492
Pa×s
417.52
Calculated Property
η
0.0005499
Pa×s
443.08
Calculated Property
η
0.0004743
Pa×s
468.64
Calculated Property
η
0.0004153
Pa×s
494.20
Calculated Property
η
0.0003685
Pa×s
519.76
Calculated Property
η
0.0003307
Pa×s
545.32
Calculated Property
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.64]
kPa
[419.52; 601.06]
The Yaws Handbook of Vapor Pressure
Equation ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A 1.42056e+01
Coefficient B -4.47322e+03
Coefficient C -9.81230e+01
Temperature range, min. 419.52
Temperature range, max. 601.06
Pvap
1.33
kPa
419.52
Calculated Property
Pvap
3.03
kPa
439.69
Calculated Property
Pvap
6.30
kPa
459.86
Calculated Property
Pvap
12.10
kPa
480.03
Calculated Property
Pvap
21.77
kPa
500.20
Calculated Property
Pvap
37.04
kPa
520.38
Calculated Property
Pvap
60.03
kPa
540.55
Calculated Property
Pvap
93.30
kPa
560.72
Calculated Property
Pvap
139.75
kPa
580.89
Calculated Property
Pvap
202.64
kPa
601.06
Calculated Property
Similar Compounds
Find more compounds similar to Naphthalene, 1-(chloromethyl)- .
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