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Equilibrium in LiquidLiquid Extraction
Diffusion and Interphase Mass Transport
18 other sections not shown
A. I. Cb acetic acid acetone aqueous axial mixing binary characteristic velocity Chem cm/sec coalescence column height concentration constant contactor continuous and dispersed continuous phase correlation diffusion direction of solute disc contactor dispersed phase holdup droplets effect Engng Cbem Engng Prog Engng Sci Engrs equilibrium estimation experimental data extraction columns extractor following equation ft/hr heavy phase inch increase indicated interfacial area interfacial tension investigated isobutanol liquid phases liquid systems liquid-liquid extraction mass transfer coefficient mass transfer rates methyl methyl isobutyl ketone mixer-settler nozzle observed obtained operation overall mass transfer packed columns Peclet number perforated phase coefficient phase flow phase flow rates plate plot plug flow Pratt pulse Raschig rings ratio reported Reynolds number rotary disc rotor rotor speed shown in Fig sieve-plate sodium hydroxide solute transfer solvent spray column stage efficiency terminal velocity tion toluene tower Trans transfer units Treybal viscosity