Continuous Distillation:  In a typical distillation column, feed enters the distillation tower at the boiling point.  The feed gets in contact with the liquid reflux traveling down the rectification section.  The vapors leave the column and are condensed in a total condenser.  Liquid is withdrawn and a part of it is used as reflux.  The residue from the bottom of the column is withdrawn and is reboiled to strip off the more-volatile product.  The section above the feed plate is called rectification section where more-volatile component is fractionated.  The section below the feed plate is called stripping section where less-volatile component is fractionated.  Heating steam is provided to strip more-volatile component.

The McCabe-Thiele method is used to calculate the number of stages.  Typically, the composition of the distillate and residue are available.  If the amount and composition of streams are given in mass basis, then we can obtain the corresponding values in molar basis as follows:

And the mole fraction of feed is given as:

Where XF is mass fraction of component A (more-volatile) in the feed, F' is mass flow rate of feed, xF imole fraction of A in the feed, and F is molar flow rate of feed.  Molecular weight of the feed can be computed as follows:

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Module for Calculation of Fractionation Parameters:

F' feed rate, lb per hr
XF feed composition, wt fraction
XD distillate composition, wt fraction
XW residue composition, wt fraction
MA molecular weight of A
MB molecular weight of B