Property Calculation
⇒
Saturated Vapor Pressure
⇒
Saturated Liquid Density
⇒
Liquid Dynamic Viscosity
⇒
Surface Tension
⇒
Heat of Vaporization
Property Estimation
⇒
UNIFAC
⇒
MOSCED
⇒
Joback
Surface Tension
Calculation by DIPPR106 Equation
Component
1,2-Ethanediol
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
m-Xylene
Methane
Methanol
N-Methyl-2-pyrrolidone
Naphthalene
Nitrogen
p-Xylene
Potassium chloride
Sodium chloride
Sulfolane
Tetrahydrofuran
Water
Temperature Unit
°C
K
°F
Property Unit
mN/m
Temperatures
(optional)
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Component Details
#DDB
Name
CAS-No.
Formula
4
Acetone
67-64-1
C3H6O
DIPPR106 Equation Parameters (Surface Tension in mN/m, T in K)
No.
A
B
C
D
E
T
c
T
min
T
max
(1)
63.442
1.1612
0
0
0
508.1
182
329
Calculation Over Validity Range
Temperature [K]
Surface Tension
(1)
[mN/m]
182
37.9081
184.94
37.5115
187.88
37.1155
190.82
36.7201
193.76
36.3253
196.7
35.9311
199.64
35.5375
202.58
35.1444
205.52
34.752
208.46
34.3603
211.4
33.9691
214.34
33.5785
217.28
33.1886
220.22
32.7993
223.16
32.4107
226.1
32.0227
229.04
31.6354
231.98
31.2487
234.92
30.8626
237.86
30.4773
240.8
30.0926
243.74
29.7086
246.68
29.3253
249.62
28.9427
252.56
28.5608
255.5
28.1796
258.44
27.7991
261.38
27.4193
264.32
27.0403
267.26
26.662
270.2
26.2844
273.14
25.9076
276.08
25.5315
279.02
25.1562
281.96
24.7817
284.9
24.408
287.84
24.0351
290.78
23.6629
293.72
23.2916
296.66
22.9211
299.6
22.5515
302.54
22.1826
305.48
21.8146
308.42
21.4475
311.36
21.0813
314.3
20.7159
317.24
20.3514
320.18
19.9879
323.12
19.6252
326.06
19.2635
329
18.9027
DIPPR106 Equation Form
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