Nonlinear Model Order Reduction of Dynamical Systems in Process Engineering: Review and Comparison
This work provides a comparative analysis for researchers and engineers in process engineering seeking efficient models for real-time optimization and control, but it is incremental as it builds on existing methods.
The authors reviewed and compared nonlinear model order reduction methods for dynamical systems in process engineering, extending manifold-Galerkin approaches to handle inputs and applying eight methods to an air separation process model to evaluate their strengths and weaknesses.
Computationally cheap yet accurate enough dynamical models are vital for real-time capable nonlinear optimization and model-based control. When given a computationally expensive high-order prediction model, a reduction to a lower-order simplified model can enable such real-time applications. Herein, we review state-of-the-art nonlinear model order reduction methods and provide a theoretical comparison of method properties. Additionally, we discuss both general-purpose methods and tailored approaches for (chemical) process systems and we identify similarities and differences between these methods. As manifold-Galerkin approaches currently do not account for inputs in the construction of the reduced state subspace, we extend these methods to dynamical systems with inputs. In a comparative case study, we apply eight established model order reduction methods to an air separation process model: POD-Galerkin, nonlinear-POD-Galerkin, manifold-Galerkin, dynamic mode decomposition, Koopman theory, manifold learning with latent predictor, compartment modeling, and model aggregation. Herein, we do not investigate hyperreduction (reduction of FLOPS). Based on our findings, we discuss strengths and weaknesses of the model order reduction methods.