Abstract
Graphical comparison of the Murphree mass transfer efficiency with the efficiency of the complex model has been made. We have proved and illustrated the expediency of using the Murphree mass transfer efficiency determination in the vapor and the liquid phases for the parallel flow, the counterflow, and the crossflow at phase equilibrium coefficients close to 1; at its other values it is recommended to use the efficiency of the complex model. The impossibility of using the Murphree efficiency in a liquid for analyzing the mass transfer in the counterflow of the phases, which in this case is equal to zero, has been proved.
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