Isobaric vapor–liquid equilibria of the binary mixtures propylene glycol methyl ether+propylene glycol methyl ether acetate, methyl acetate+propylene glycol methyl ether and methanol+propylene glycol methyl ether acetate at 101.3kPa

Separation of methyl acetate+methanol azeotropic mixture using ionic liquids as entrainers

“…The Antoine parameters [19], as well as the normal boiling point T b of pure component measured in this work and that reported in literature [20] are presented in Table 3. All of the binary and ternary experimental VLE data comply with thermodynamic consistency by the Herington test (|D -J| < 10) [21].…”

“…All of the binary and ternary experimental VLE data comply with thermodynamic consistency by the Herington test (|D -J| < 10) [21]. u(T) = 0.05 K. a From ref [19]. b From ref [20].…”

Isobaric vapor–liquid equilibrium of the binary system sec-butyl acetate +para-xylene and the quaternary system methyl acetate +para-xylene +sec-butyl acetate + acetic acid at 101.3 kPa

“…The reliability of the modified Rose still has been validated in the literature [13]. VLE data for the binary system SBA + PX and the quaternary system MA + PX + SBA + HAc at 101.3 kPa were determined.…”

Isobaric vapor–liquid equilibrium for methyl acetate+methanol system containing different ionic liquids at 101.3kPa

“…The densities of the pure components were measured at 298.15 K using a vibrating tube density meter (M196028, China), and the standard uncertainty is 0.0002 g cm À3 . The boiling points of methyl acetate and methanol were determined at 101.3 kPa, and the standard uncertainty is 0.05 K. The measured densities of components and boiling points of methyl acetate and methanol as well as the values of the corresponding literature [23][24][25] are shown in Table 2.…”

“…Only when the temperature was Standard uncertainties u are u(r) = 0.0002 g cm À3 ,u(T) = 0.05 K. a From Ref. [24]. b From Ref.…”