Mathematical modelling of rectification of multicomponent mix

Characteristic of process of receiving cyclohexanone is given. Mass-exchanged, dynamic models of rectification are presented and calculation of a rectifying column is made: determination of pressure in a column; calculation of temperature of top and bottom of a column; calculation of a share of an distillation of raw materials at its giving in a column; calculation of the minimum number steps of division of a column; calculation of reflux-to-product ratio; calculation of thermal balance.