The cleavage of cumyl hydroperoxide is a fast reaction (0.1 < t 1/2 < 1.5 s), with a rate varying of an order of magnitude by changing the medium composition, i.e., H2O and phenol concentrations. A four-paramete...
Artikel
Pareto‐Optimal Treatment of Uncertainties in Model‐Based Process Design and Operation
Von Wiley-VCH zur Verfügung gestellt
It is described how to handle here-and-now (i.e., process design-related) and wait-and-see (i.e., process operation-related) decisions in a multicriteria framework. This approach exploits the adjustability for the wait-and-see variables while at the same time respecting optimality guarantees on process key performance indicators.
Abstract
Model-based process design and operation involves here-and-now and wait-and-see decisions. Here-and-now decisions include design variables like the size of heat exchangers or the height of distillation columns, whereas wait-and-see decisions are directed towards operational variables like reflux and split ratios. In this contribution, we describe how to deal with these different types of decisions in a multicriteria framework, offering an adjustability for the wait-and-see variables while at the same time respecting optimality guarantees on process key performance indicators (KPIs).
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