Design algorithms multiple reactions

Table 8-3 gives the algorithm for the design of PFRs and PBRs with heat exchange for case A conversion as the reaction variable and case S molar flow rates as the reaction variable. The procedure in case B must be used when multiple reactions are present... 

The algorithm for the design of the operation of batch reactors, with existent only one phase, multiple reactions taking place and operational constraints on temperature present, has been presented earlier (Papaeconomou et al., 2002). The key factor is the existence of desired reactions and of competing reactions, where the latter need to be suppressed. In addition to the operational constraints, there are also end constraints/objectives, namely the molefraction of the limiting reactant in the reaction of interest that should be as low as possible and the progress of the reaction of interest that should be as high as possible. At least one of the end constraints has to be satisfied. 

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