Physical Properties
Property
Value
Unit
Source
ω
0.7936
Relay (1.0) Calculated Property
Δf G°
78.80
kJ/mol
Joback Calculated Property
Δf H°gas
-275.13
kJ/mol
Relay (1.0) Calculated Property
Δfus H°
37.41
kJ/mol
Joback Calculated Property
Δvap H°
89.40
kJ/mol
Relay (1.0) Calculated Property
IE
9.88
eV
Relay (1.0) Calculated Property
log 10 WS
-6.86
Relay (1.0) Calculated Property
log Poct/wat
5.677
Crippen Calculated Property
McVol
214.940
ml/mol
McGowan Calculated Property
Pc
2007.30
kPa
Joback Calculated Property
Inp
1946.00
NIST
Tboil
575.18
K
Relay (1.0) Calculated Property
Tc
754.94
K
Relay (1.0) Calculated Property
Tfus
310.85
K
Relay (1.0) Calculated Property
Vc
0.822
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Cp,liquid
[432.62; 457.90]
J/mol×K
[310.65; 355.15]
Cp,liquid
432.62
J/mol×K
310.65
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
433.39
J/mol×K
312.15
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
434.17
J/mol×K
313.65
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
434.98
J/mol×K
315.15
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
435.79
J/mol×K
316.65
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
436.62
J/mol×K
318.15
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
437.46
J/mol×K
319.65
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
438.31
J/mol×K
321.15
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
439.17
J/mol×K
322.65
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
440.04
J/mol×K
324.15
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
440.91
J/mol×K
325.65
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
441.80
J/mol×K
327.15
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
442.68
J/mol×K
328.65
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
443.57
J/mol×K
330.15
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
444.47
J/mol×K
331.65
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
445.36
J/mol×K
333.15
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
446.26
J/mol×K
334.65
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
447.15
J/mol×K
336.15
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
448.04
J/mol×K
337.65
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
448.93
J/mol×K
339.15
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
449.82
J/mol×K
340.65
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
450.69
J/mol×K
342.15
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
451.57
J/mol×K
343.65
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
452.43
J/mol×K
345.15
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
453.29
J/mol×K
346.65
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
454.13
J/mol×K
348.15
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
454.96
J/mol×K
349.65
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
455.78
J/mol×K
351.15
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
456.59
J/mol×K
352.65
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
457.38
J/mol×K
354.15
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid
457.90
J/mol×K
355.15
Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
488.20
K
2.00
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[288.02; 656.56]
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 8.36200e+00
Coefficient B 1.22020e+00
Coefficient C -7.71800e-04
Coefficient D 1.99800e-07
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
288.02
J/mol×K
273.00
Calculated Property
Cp,gas
352.29
J/mol×K
353.78
Calculated Property
Cp,gas
409.26
J/mol×K
434.56
Calculated Property
Cp,gas
459.55
J/mol×K
515.33
Calculated Property
Cp,gas
503.80
J/mol×K
596.11
Calculated Property
Cp,gas
542.64
J/mol×K
676.89
Calculated Property
Cp,gas
576.71
J/mol×K
757.67
Calculated Property
Cp,gas
606.63
J/mol×K
838.44
Calculated Property
Cp,gas
633.04
J/mol×K
919.22
Calculated Property
Cp,gas
656.56
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0023816; 0.0002602]
Pa×s
[344.60; 555.44]
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 -1.18726e+01
Coefficient B 2.00992e+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. 344.60
Temperature range, max. 555.44
η
0.0023816
Pa×s
344.60
Calculated Property
η
0.0016430
Pa×s
368.03
Calculated Property
η
0.0011849
Pa×s
391.45
Calculated Property
η
0.0008867
Pa×s
414.88
Calculated Property
η
0.0006844
Pa×s
438.31
Calculated Property
η
0.0005423
Pa×s
461.74
Calculated Property
η
0.0004395
Pa×s
485.16
Calculated Property
η
0.0003632
Pa×s
508.59
Calculated Property
η
0.0003052
Pa×s
532.02
Calculated Property
η
0.0002602
Pa×s
555.44
Calculated Property
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.67]
kPa
[456.92; 604.60]
The Yaws Handbook of Vapor Pressure
Equation ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A 1.72197e+01
Coefficient B -5.92693e+03
Coefficient C -1.06880e+02
Temperature range, min. 456.92
Temperature range, max. 604.60
Pvap
1.33
kPa
456.92
Calculated Property
Pvap
2.85
kPa
473.33
Calculated Property
Pvap
5.69
kPa
489.74
Calculated Property
Pvap
10.75
kPa
506.15
Calculated Property
Pvap
19.32
kPa
522.56
Calculated Property
Pvap
33.20
kPa
538.96
Calculated Property
Pvap
54.85
kPa
555.37
Calculated Property
Pvap
87.44
kPa
571.78
Calculated Property
Pvap
135.04
kPa
588.19
Calculated Property
Pvap
202.67
kPa
604.60
Calculated Property
Similar Compounds
Find more compounds similar to Dodecane, 1,12-dibromo- .
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