Distillation sequence side-stripper

Consider now ways in which the best arrangement of a distillation sequence can be determined more systematically. Given the possibilities for changing the sequence of simple columns or the introduction of prefractionators, side-strippers, side-rectifiers and fully thermally coupled arrangements, the problem is complex with many structural options. The problem can be addressed using the optimization of a superstructure. As discussed in Chapter 1, this approach starts by setting up a grand flowsheet in which all structural features for an optimal solution are embedded. 

By complex column, we mean a distillation set-up that can handle a mixture of at least three components, and deliver more than two products. The arrangement consists of a main distillation column surrounded by additional devices, as prefractionator, heaters, inter-coolers, side-strippers and side-rectifiers. Figure 7.25 presents seven design alternatives for separating a ternary mixture ABC. Note that direct and indirect two-column sequences are included in this list, since they may be seen as reference alternatives. The operation of different types may be summarised as follows ... 

Due to the tremendous costs associated to distillative separations, many alternate schemes to the simple column shown above have been proposed over the past several years both to improve on some of its inherent costs. Traditionally, when purifying a multicomponent mixture, an entire series of distillation columns are used in series, and the way in which these columns are sequenced may make a tremendous difference in the eventual process costs. However, due to the large energy requirements of even the most optimal sequence, more complex column arrangements have been proposed and subsequently utilized. These arrangements include thermally coupled columns such as side rectifiers and strippers, the fully thermally coupled columns (often referred to as the Petlyuk and Kaibel columns). 

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