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The final stage is the practical application of the processing ideas and concepts to generate intensified process alternatives.
In principle, there are two process alternatives.
The approach involved four steps: process modeling and analysis, identification of process alternatives, selection of process alternatives and incorporation of multiobjective optimization.
In this work, distillation, pervaporation and hybrid distillation/pervaporation processes are considered as process alternatives.
Process alternatives were identified from both literature and sensitivity analysis procedures.
In this paper, the design and control of two reaction-separation-recycle process alternatives are developed.
The superstructure imbeds 30,720 possible process alternatives and unit operation options.
Different process alternatives are considered and screened to attain the optimum design.
Using the example of dieless clinching, the full potential of such process alternatives is visible.
Reverse approach is used to identify the final design details for process alternatives.
The total power consumption is approximately the same for the two process alternatives.
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