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
174
Water
7732-18-5
H2O
DIPPR105 Equation Parameters (Density in kg/m
3
, T in K)
No.
A
B
C
D
T
min
T
max
(1)
0.14395
0.0112
649.727
0.05107
273
648
Calculation Over Validity Range
Temperature [K]
Density
(1)
[kg/m3]
273
1014.44
280.5
1009.9
288
1005.29
295.5
1000.62
303
995.867
310.5
991.044
318
986.142
325.5
981.159
333
976.091
340.5
970.935
348
965.687
355.5
960.344
363
954.9
370.5
949.351
378
943.693
385.5
937.92
393
932.025
400.5
926.004
408
919.849
415.5
913.552
423
907.106
430.5
900.503
438
893.732
445.5
886.783
453
879.644
460.5
872.303
468
864.745
475.5
856.955
483
848.914
490.5
840.603
498
831.999
505.5
823.076
513
813.805
520.5
804.15
528
794.073
535.5
783.526
543
772.455
550.5
760.792
558
748.457
565.5
735.349
573
721.345
580.5
706.282
588
689.951
595.5
672.066
603
652.226
610.5
629.837
618
603.963
625.5
572.978
633
533.62
640.5
477.318
648
354.855
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