A crude column configuration lets one draw multiple products from a single configuration having one heat source (furnace) at the bottom. Each product will not be pure, as in a chemical type process, but will cover a range of distillation temperatures; just how narrow a range depends on the degree of fractionation (number of trays) between product draws. As you go up the column, the liquid has less and less of the heavier ends of the crude feed, so product draws will be lighter and lighter. However, at any particular product draw point, although the liquid will contain a sufficiently low concentration of heavier material not wanted in that product, it also will contain some material that is lighter than is what is wanted. This is because the lighter material must pass through the draw tray on its way higher up, and some will be absorbed in the liquid at that point. The lighter material can be rejected by feeding the liquid draw to the top of a sidestripper, having a reboiler or stripping steam feed at the bottom. The overhead vapor, containing the unwanted lighter material (and of course some of the desired stuff), is returned to the main column, and the stripper bottom product contains just the boiling range desired for that product.
Any good text on petroleum distillation ought to cover this stuff.