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
11
Ethanol
64-17-5
C2H6O
DIPPR105 Equation Parameters (Density in kg/m
3
, T in K)
No.
A
B
C
D
T
min
T
max
(1)
99.3974
0.310729
513.18
0.305143
191
513
Calculation Over Validity Range
Temperature [K]
Density
(1)
[kg/m3]
191
881.844
197.44
876.369
203.88
870.85
210.32
865.286
216.76
859.675
223.2
854.017
229.64
848.308
236.08
842.548
242.52
836.734
248.96
830.864
255.4
824.937
261.84
818.948
268.28
812.897
274.72
806.781
281.16
800.595
287.6
794.338
294.04
788.006
300.48
781.596
306.92
775.103
313.36
768.523
319.8
761.852
326.24
755.084
332.68
748.215
339.12
741.239
345.56
734.148
352
726.936
358.44
719.594
364.88
712.115
371.32
704.488
377.76
696.702
384.2
688.744
390.64
680.601
397.08
672.257
403.52
663.693
409.96
654.888
416.4
645.818
422.84
636.452
429.28
626.756
435.72
616.689
442.16
606.198
448.6
595.22
455.04
583.674
461.48
571.452
467.92
558.413
474.36
544.357
480.8
528.994
487.24
511.868
493.68
492.188
500.12
468.366
506.56
436.092
513
354.644
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