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A Two-Phase Approach for Model-Based Design of Experiments Applied in Chemical Engineering

机译:基于模型的化学工程实验设计的两相方法

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Optimal (model-based) experimental design (OED) aims to determine the interactions between input and output quantities connected by an, often complicated, mathematical model as precisely as possible from a minimum number of experiments. While statistical design techniques can often be proven to be optimal for linear models, this is no longer the case for nonlinear models. In process engineering applications, where the models are characterized by physico-chemical laws, nonlinear models often lead to nonconvex experimental design problems, thus making the computation of optimal experimental designs arduous. On the other hand, the optimal selection of experiments from a finite set of experiments can be formulated as a convex optimization problem for the most important design criteria and, thus, solved to global optimality. Since the latter represents an approximation of common experimental design problems, we propose a two-phase strategy that first solves the convex selection problem, and then uses this optimal selection to initialize the original problem. Finally, we illustrate and evaluate this generic approach and compare it with two statistical approaches on an OED problem from chemical process engineering.
机译:最佳(基于模型的)实验设计(OED)旨在确定通过最小实验的最佳实验所以尽可能地尽可能地精确地确定输入和输出量之间的相互作用。虽然通常可以证明统计设计技术是线性模型的最佳选择,但这不再是非线性模型的情况。在工艺工程应用中,在模型的特征在于物理化学法,非线性模型往往导致非凸显实验设计问题,从而实现了最佳实验设计的计算艰巨。另一方面,可以将来自有限一组实验的实验选择可以作为最重要的设计标准制定为凸优化问题,因此解决了全球最优性。由于后者代表常见的实验设计问题的近似,我们提出了一个双相策略,首先解决了凸选择问题,然后使用此最佳选择来初始化原始问题。最后,我们说明并评估了这种通用方法,并将其与化学工艺工程中的两种统计方法进行了比较。

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