Physical Properties
Property
Value
Unit
Source
ω
1.3203
Relay (1.0) Calculated Property
Δf G°
-192.71
kJ/mol
Joback Calculated Property
Δf H°gas
-898.23
kJ/mol
Relay (1.0) Calculated Property
Δfus H°
68.06
kJ/mol
Joback Calculated Property
Δvap H°
152.25
kJ/mol
Relay (1.0) Calculated Property
IE
10.23
eV
Relay (1.0) Calculated Property
log 10 WS
-8.17
Relay (1.0) Calculated Property
log Poct/wat
8.673
Crippen Calculated Property
McVol
356.460
ml/mol
McGowan Calculated Property
Pc
848.50
kPa
Joback Calculated Property
Inp
[2685.00; 2760.00]
Inp
2685.00
NIST
Inp
2760.00
NIST
Inp
2685.00
NIST
Inp
2760.00
NIST
Tboil
640.41
K
Relay (1.0) Calculated Property
Tc
846.09
K
Relay (1.0) Calculated Property
Tfus
358.45 ± 2.00
K
NIST
Vc
1.406
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
545.20
K
1.30
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[528.23; 1268.29]
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 -1.43280e+01
Coefficient B 2.33462e+00
Coefficient C -1.35440e-03
Coefficient D 3.02400e-07
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
528.23
J/mol×K
273.00
Calculated Property
Cp,gas
655.48
J/mol×K
353.78
Calculated Property
Cp,gas
769.25
J/mol×K
434.56
Calculated Property
Cp,gas
870.48
J/mol×K
515.33
Calculated Property
Cp,gas
960.14
J/mol×K
596.11
Calculated Property
Cp,gas
1039.18
J/mol×K
676.89
Calculated Property
Cp,gas
1108.56
J/mol×K
757.67
Calculated Property
Cp,gas
1169.23
J/mol×K
838.44
Calculated Property
Cp,gas
1222.16
J/mol×K
919.22
Calculated Property
Cp,gas
1268.29
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0095478; 0.0000668]
Pa×s
[358.45; 767.01]
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 -1.39672e+01
Coefficient B 3.33922e+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. 358.45
Temperature range, max. 767.01
η
0.0095478
Pa×s
358.45
Calculated Property
η
0.0033506
Pa×s
403.85
Calculated Property
η
0.0014530
Pa×s
449.24
Calculated Property
η
0.0007345
Pa×s
494.64
Calculated Property
η
0.0004164
Pa×s
540.03
Calculated Property
η
0.0002578
Pa×s
585.43
Calculated Property
η
0.0001710
Pa×s
630.82
Calculated Property
η
0.0001199
Pa×s
676.22
Calculated Property
η
0.0000879
Pa×s
721.62
Calculated Property
η
0.0000668
Pa×s
767.01
Calculated Property
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.67]
kPa
[590.12; 728.41]
The Yaws Handbook of Vapor Pressure
Equation ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A 2.12110e+01
Coefficient B -9.15711e+03
Coefficient C -1.52472e+02
Temperature range, min. 590.12
Temperature range, max. 728.41
Pvap
1.33
kPa
590.12
Calculated Property
Pvap
2.71
kPa
605.49
Calculated Property
Pvap
5.26
kPa
620.85
Calculated Property
Pvap
9.79
kPa
636.22
Calculated Property
Pvap
17.53
kPa
651.58
Calculated Property
Pvap
30.33
kPa
666.95
Calculated Property
Pvap
50.82
kPa
682.31
Calculated Property
Pvap
82.71
kPa
697.68
Calculated Property
Pvap
131.07
kPa
713.04
Calculated Property
Pvap
202.67
kPa
728.41
Calculated Property
Similar Compounds
Find more compounds similar to Tetracosanoic acid .
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