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
110
Methanol
67-56-1
CH4O
DIPPR105 Equation Parameters (Density in kg/m
3
, T in K)
No.
A
B
C
D
T
min
T
max
(1)
54.566
0.233211
513.16
0.208875
181
513
Calculation Over Validity Range
Temperature [K]
Density
(1)
[kg/m3]
181
884.124
187.64
879.191
194.28
874.206
200.92
869.167
207.56
864.073
214.2
858.92
220.84
853.708
227.48
848.434
234.12
843.095
240.76
837.69
247.4
832.215
254.04
826.667
260.68
821.044
267.32
815.342
273.96
809.558
280.6
803.688
287.24
797.728
293.88
791.673
300.52
785.519
307.16
779.261
313.8
772.893
320.44
766.409
327.08
759.802
333.72
753.066
340.36
746.192
347
739.171
353.64
731.994
360.28
724.65
366.92
717.126
373.56
709.41
380.2
701.485
386.84
693.335
393.48
684.939
400.12
676.275
406.76
667.316
413.4
658.031
420.04
648.384
426.68
638.329
433.32
627.815
439.96
616.776
446.6
605.13
453.24
592.774
459.88
579.569
466.52
565.333
473.16
549.805
479.8
532.604
486.44
513.123
493.08
490.304
499.72
461.977
506.36
422.114
513
306.387
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