Reboilers are essential for the proper work of distillation
and stripping columns. Hereby the intensity of axial mixing along
the reboiler (Peclet number) is used for the reboiler separation efficiency
modeling and estimation for binary systems. Two fully worked examples
show that the separation (Murphree) efficiency varies significantly
depending on the adopted reboiler flow model. Murphree efficiency
ranges between 1.40 and 0.663 in example 1, and between 1.962 and
1 in example 2. The general conclusion is that the reboiler performance
must be considered carefully in the case of design of the new plants,as
well as in the case of “brown field” projects.