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   Tc   Tmin   Tmax   (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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