Physical Properties
Property
Value
Unit
Source
ω
0.4783
Relay (1.0) Calculated Property
Δf G°
28.36
kJ/mol
Joback Calculated Property
Δf H°gas
-199.23
kJ/mol
Relay (1.0) Calculated Property
Δfus H°
18.24
kJ/mol
Joback Calculated Property
Δvap H°
52.59
kJ/mol
Relay (1.0) Calculated Property
IE
9.79
eV
Relay (1.0) Calculated Property
log 10 WS
-4.68
Relay (1.0) Calculated Property
log Poct/wat
3.740
Crippen Calculated Property
McVol
141.080
ml/mol
McGowan Calculated Property
Pc
2744.03
kPa
Joback Calculated Property
Inp
[1093.00; 1093.00]
Inp
1093.00
NIST
Inp
1093.00
NIST
Tboil
461.70
K
NIST
Tc
650.28
K
Relay (1.0) Calculated Property
Tfus
210.64
K
Relay (1.0) Calculated Property
Vc
0.537
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Δvap H
48.40
kJ/mol
403.00
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
345.20
K
1.90
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[188.86; 441.66]
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 2.12500e+00
Coefficient B 8.07940e-01
Coefficient C -4.86000e-04
Coefficient D 1.17600e-07
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
188.86
J/mol×K
273.00
Calculated Property
Cp,gas
232.34
J/mol×K
353.78
Calculated Property
Cp,gas
271.09
J/mol×K
434.56
Calculated Property
Cp,gas
305.51
J/mol×K
515.33
Calculated Property
Cp,gas
335.96
J/mol×K
596.11
Calculated Property
Cp,gas
362.81
J/mol×K
676.89
Calculated Property
Cp,gas
386.43
J/mol×K
757.67
Calculated Property
Cp,gas
407.20
J/mol×K
838.44
Calculated Property
Cp,gas
425.49
J/mol×K
919.22
Calculated Property
Cp,gas
441.66
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0063866; 0.0003047]
Pa×s
[224.72; 443.39]
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 -1.12226e+01
Coefficient B 1.38632e+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. 224.72
Temperature range, max. 443.39
η
0.0063866
Pa×s
224.72
Calculated Property
η
0.0034983
Pa×s
249.02
Calculated Property
η
0.0021327
Pa×s
273.31
Calculated Property
η
0.0014095
Pa×s
297.61
Calculated Property
η
0.0009917
Pa×s
321.91
Calculated Property
η
0.0007330
Pa×s
346.21
Calculated Property
η
0.0005637
Pa×s
370.50
Calculated Property
η
0.0004478
Pa×s
394.80
Calculated Property
η
0.0003653
Pa×s
419.10
Calculated Property
η
0.0003047
Pa×s
443.39
Calculated Property
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.67]
kPa
[349.32; 493.06]
The Yaws Handbook of Vapor Pressure
Equation ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A 1.50922e+01
Coefficient B -4.14278e+03
Coefficient C -6.94890e+01
Temperature range, min. 349.32
Temperature range, max. 493.06
Pvap
1.33
kPa
349.32
Calculated Property
Pvap
2.97
kPa
365.29
Calculated Property
Pvap
6.08
kPa
381.26
Calculated Property
Pvap
11.61
kPa
397.23
Calculated Property
Pvap
20.89
kPa
413.20
Calculated Property
Pvap
35.67
kPa
429.18
Calculated Property
Pvap
58.21
kPa
445.15
Calculated Property
Pvap
91.27
kPa
461.12
Calculated Property
Pvap
138.15
kPa
477.09
Calculated Property
Pvap
202.67
kPa
493.06
Calculated Property
Similar Compounds
Find more compounds similar to Octane, 2-bromo-, (.+/-.)- .
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