Introduction

 

Linear cascades

 

       Linear cascades are commonly used in several mass transfer devices consisting of assemblies of individual units, or stages.  These stages are connected to ach other in such a way that the material being processed has to pass, usually as two streams moving counter-currently, through each stage in turn; therefore the term cascade is used to describe them.  In each stage, they are brought into contact, mixed and then separated.  (McCabe, Smith, Harriott).  For simplifying purposes, the stages are assumed to be ideal; that is, the leaving streams are assumed to be in equilibrium, although in reality they are not.  Although a stage can be represented in several ways, for this example, each stage would be simulated as a binary splitter, such as the one described in Example 23.1-2.

 

       Linear cascades are used in a variety of processes such as gas absorption and distillation, where the stages are arranged in a vertical column (one on top of the other), or in leaching, where the stages are basically a series of stirring tanks.  The first type of arrangement, which is the one described in Example 23.5-3, can be observed in Figure 1.  Although a vertical column such as the one described in this example can be used in distillation as well as in gas absorption, there is usually no reflux (liquid obtained from the condenser that is returned to the top of the column) in the latter one, therefore creating the need of using several operating lines to describe the operation.  Since I will be discussing total reflux, you are encouraged to think of this example as a possible condition in which to operate a distillation column.  In fact, batch distillation is run at total reflux.  

 

 

Batch distillation

  

       In batch distillation, the idea is to use vapor liquid equilibrium (VLE) to achieve a separation of a solution into its more volatile and its liquid parts.  To do this, a mixture is feed into a still or into a reboiler and then passed through a rectifying column, usually mounted on top of it (as in our example), with reflux to increase the purity of the overhead product.

 

 

 

 

Figure 1: (a) Reboiler with fractionating column; (b) Detail of sieve plate (McCabe, Smith, Harriott)