Physical Properties
Property
Value
Unit
Source
ω
1.0298
Relay (1.0) Calculated Property
Δc H°liquid
[-11128.00; -11127.10]
kJ/mol
Δc H°liquid
-11127.10
kJ/mol
NIST
Δc H°liquid
-11128.00
kJ/mol
NIST
Δc H°solid
-11040.40
kJ/mol
NIST
Δf G°
-163.01
kJ/mol
Joback Calculated Property
Δf H°gas
-706.03
kJ/mol
Relay (1.0) Calculated Property
Δf H°liquid
-769.00
kJ/mol
NIST
Δfus H°
52.72
kJ/mol
Joback Calculated Property
Δvap H°
124.37
kJ/mol
Relay (1.0) Calculated Property
IE
9.17
eV
Relay (1.0) Calculated Property
log 10 WS
-5.79
Relay (1.0) Calculated Property
log Poct/wat
6.109
Crippen Calculated Property
McVol
267.620
ml/mol
McGowan Calculated Property
Pc
1270.97
kPa
Joback Calculated Property
Inp
[2123.00; 2143.90]
Inp
2141.00
NIST
Inp
2143.90
NIST
Inp
2123.00
NIST
Tboil
606.18
K
Relay (1.0) Calculated Property
Tc
807.69
K
Relay (1.0) Calculated Property
Tfus
[316.95; 320.00]
K
Tfus
316.95 ± 0.50
K
NIST
Tfus
317.15 ± 1.00
K
NIST
Tfus
320.00 ± 1.00
K
NIST
Vc
1.010
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
[507.20; 561.20]
K
[2.00; 13.30]
Tboilr
507.20
K
2.00
NIST
Tboilr
561.20
K
13.30
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[386.95; 928.16]
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 -2.30560e+01
Coefficient B 1.78462e+00
Coefficient C -1.11180e-03
Coefficient D 2.78400e-07
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
386.95
J/mol×K
273.00
Calculated Property
Cp,gas
481.48
J/mol×K
353.78
Calculated Property
Cp,gas
565.36
J/mol×K
434.56
Calculated Property
Cp,gas
639.46
J/mol×K
515.33
Calculated Property
Cp,gas
704.67
J/mol×K
596.11
Calculated Property
Cp,gas
761.87
J/mol×K
676.89
Calculated Property
Cp,gas
811.94
J/mol×K
757.67
Calculated Property
Cp,gas
855.76
J/mol×K
838.44
Calculated Property
Cp,gas
894.21
J/mol×K
919.22
Calculated Property
Cp,gas
928.16
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0113678; 0.0001286]
Pa×s
[318.03; 660.17]
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 -1.31254e+01
Coefficient B 2.75050e+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. 318.03
Temperature range, max. 660.17
η
0.0113678
Pa×s
318.03
Calculated Property
η
0.0045149
Pa×s
356.05
Calculated Property
η
0.0021429
Pa×s
394.06
Calculated Property
η
0.0011596
Pa×s
432.08
Calculated Property
η
0.0006930
Pa×s
470.10
Calculated Property
η
0.0004473
Pa×s
508.11
Calculated Property
η
0.0003069
Pa×s
546.13
Calculated Property
η
0.0002211
Pa×s
584.14
Calculated Property
η
0.0001658
Pa×s
622.16
Calculated Property
η
0.0001286
Pa×s
660.17
Calculated Property
Property
Value
Unit
Temperature (K)
Source
Pvap
[0.13; 100.91]
kPa
[444.50; 635.00]
NIST
Equation ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A 2.06467e+01
Coefficient B -1.04353e+04
Coefficient C 1.58860e+01
Reference Stull, 1947
Comment Coefficents calculated by NIST from author's data.
Temperature range, min. 444.50
Temperature range, max. 635.00
Pvap
0.13
kPa
444.50
Calculated Property
Pvap
0.36
kPa
465.67
Calculated Property
Pvap
0.89
kPa
486.83
Calculated Property
Pvap
2.07
kPa
508.00
Calculated Property
Pvap
4.49
kPa
529.17
Calculated Property
Pvap
9.18
kPa
550.33
Calculated Property
Pvap
17.83
kPa
571.50
Calculated Property
Pvap
33.08
kPa
592.67
Calculated Property
Pvap
58.87
kPa
613.83
Calculated Property
Pvap
100.91
kPa
635.00
Calculated Property
Similar Compounds
Find more compounds similar to 9-Octadecenoic acid .
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