Vapor liquid equilibrium for the binary systems 2-methylpentane + 2-butanol at 329.2 K and n-hexane + 2-butanol at 329.2 and 363.2 K with a static apparatus

Phase equilibrium measurements for systems containing propanenitrile with tert-butyl ethyl ether and C4-hydrocarbons

“…Thus measurements with the glass circulation still apparatus were carried out to ensure the 0378 2.2.1. The automated static total pressure apparatus The setup of the static total pressure apparatus and the experimental procedure are described in detail in the article by Uusi-Kyyny et al [6]. The description of the automation of the apparatus can be found in Ouni et al [7].…”

“…The critical values needed for the calculations, the acentric factor and the liquid molar volume are presented in Table 2. The scheme for the data reduction used in this work is reported in [6]. Data reductions were also carried out using the Wilson model [15] for modeling the liquid phase activity coefficients.…”

Isothermal binary vapour–liquid equilibrium for butanes and butenes with dimethylsulphide

“…The static total pressure apparatus is described in more detail by Uusi-Kyyny et al [6]. The experimental set-up is presented in Fig.…”

“…The equilibrium cell was immersed in a water bath with a volume of approximately 70 dm 3 . The temperature stability of the water bath was ±0.02 K as discussed earlier [6]. The total volume of the equilibrium cell was 103.33 cm 3 .…”

“…The scheme for data reduction used in this work is reported in [6]. The critical properties needed for data reduction by Barker's method are presented in Table 1.…”