Property Calculation
⇒
Saturated Vapor Pressure
⇒
Saturated Liquid Density
⇒
Liquid Dynamic Viscosity
⇒
Surface Tension
⇒
Heat of Vaporization
Property Estimation
⇒
UNIFAC
⇒
MOSCED
⇒
Joback
Saturated Liquid Density
Calculation by DIPPR105 Equation
Component
1,2-Ethanediol
1,2-Propanediol
1,3-Butadiene
1-Butanol
1-Hexene
2-Propanol
Acetic acid
Acetic acid butyl ester
Acetone
Acetonitrile
Benzene
Carbon dioxide
Chloroform
Cyclohexane
Diethyl ether
Ethanol
Ethyl acetate
Hexadecane
Isoprene
m-Xylene
Methane
Methanol
N-Methyl-2-pyrrolidone
Naphthalene
Nitrogen
o-Xylene
p-Xylene
Potassium chloride
Sodium chloride
Sulfolane
Tetrahydrofuran
Water
Temperature Unit
°C
K
°F
Property Unit
kg/m3
g/cm3
lbm/ft3
Temperatures
(optional)
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Component Details
#DDB
Name
CAS-No.
Formula
31
Benzene
71-43-2
C6H6
DIPPR105 Equation Parameters (Density in kg/m
3
, T in K)
No.
A
B
C
D
T
min
T
max
(1)
80.3682
0.266457
561.65
0.28797
273
561
Calculation Over Validity Range
Temperature [K]
Density
(1)
[kg/m3]
273
898.747
278.76
893.085
284.52
887.378
290.28
881.622
296.04
875.817
301.8
869.961
307.56
864.051
313.32
858.087
319.08
852.065
324.84
845.985
330.6
839.842
336.36
833.635
342.12
827.362
347.88
821.018
353.64
814.602
359.4
808.109
365.16
801.537
370.92
794.882
376.68
788.138
382.44
781.303
388.2
774.371
393.96
767.336
399.72
760.194
405.48
752.938
411.24
745.56
417
738.054
422.76
730.41
428.52
722.62
434.28
714.674
440.04
706.558
445.8
698.262
451.56
689.769
457.32
681.062
463.08
672.123
468.84
662.929
474.6
653.453
480.36
643.665
486.12
633.528
491.88
622.998
497.64
612.021
503.4
600.529
509.16
588.436
514.92
575.632
520.68
561.967
526.44
547.234
532.2
531.13
537.96
513.183
543.72
492.582
549.48
467.72
555.24
434.377
561
364.257
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