Physical Properties
Property
Value
Unit
Source
ω
0.7706
Relay (1.0) Calculated Property
Δf G°
-646.22
kJ/mol
Joback Calculated Property
Δf H°gas
-827.62
kJ/mol
Relay (1.0) Calculated Property
Δfus H°
28.40
kJ/mol
Joback Calculated Property
Δvap H°
89.68
kJ/mol
Relay (1.0) Calculated Property
IE
10.10
eV
Relay (1.0) Calculated Property
log 10 WS
-0.55
Relay (1.0) Calculated Property
log Poct/wat
0.804
Crippen Calculated Property
McVol
124.370
ml/mol
McGowan Calculated Property
Pc
3100.18
kPa
Joback Calculated Property
Tboil
531.15
K
Relay (1.0) Calculated Property
Tc
716.12
K
Relay (1.0) Calculated Property
Tfus
319.32
K
Relay (1.0) Calculated Property
Vc
0.475
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Δvap H
82.90
kJ/mol
478.00
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
435.20
K
1.30
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[183.94; 399.35]
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 2.65340e+01
Coefficient B 6.64820e-01
Coefficient C -3.35000e-04
Coefficient D 4.30000e-08
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
183.94
J/mol×K
273.00
Calculated Property
Cp,gas
221.71
J/mol×K
353.78
Calculated Property
Cp,gas
255.70
J/mol×K
434.56
Calculated Property
Cp,gas
286.06
J/mol×K
515.33
Calculated Property
Cp,gas
312.91
J/mol×K
596.11
Calculated Property
Cp,gas
336.39
J/mol×K
676.89
Calculated Property
Cp,gas
356.64
J/mol×K
757.67
Calculated Property
Cp,gas
373.79
J/mol×K
838.44
Calculated Property
Cp,gas
387.99
J/mol×K
919.22
Calculated Property
Cp,gas
399.35
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0015691; 0.0002863]
Pa×s
[371.58; 528.56]
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 -1.21848e+01
Coefficient B 2.12822e+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. 371.58
Temperature range, max. 528.56
η
0.0015691
Pa×s
371.58
Calculated Property
η
0.0012137
Pa×s
389.02
Calculated Property
η
0.0009598
Pa×s
406.46
Calculated Property
η
0.0007737
Pa×s
423.91
Calculated Property
η
0.0006345
Pa×s
441.35
Calculated Property
η
0.0005282
Pa×s
458.79
Calculated Property
η
0.0004457
Pa×s
476.23
Calculated Property
η
0.0003806
Pa×s
493.67
Calculated Property
η
0.0003285
Pa×s
511.12
Calculated Property
η
0.0002863
Pa×s
528.56
Calculated Property
Similar Compounds
Find more compounds similar to Hexanedioic acid, monomethyl ester .
Mixtures
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