Abstract
A model for mass transfer in the liquid phase in packed towers, proposed in a previous work[5], is employed in the case of mass transfer with controlling resistance in the gas phase. On taking into account the semistagnant liquid pockets by the liquid residence time distribution function, relationships are established between the volumetric mass transfer coefficients in different operations: evaporation, physical absorption, chemical absorption. The calculated values of the mass transfer coefficients agree well with experimental data.
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