'Institute of Electrical and Electronics Engineers (IEEE)'
Abstract
This paper presents structure exploitation techniques that lead to faster convergence of first-order methods for practical Model Predictive Control (MPC) formulations. We exploit the special structure of output box constraints as well as input bound and rate constraints. The output constraints are included in the MPC objective as exact penalty functions, in order to avoid feasibility issues due to e.g. plant-model mismatch. Observations from a new derivation of exact penalty functions enable us to formulate exact penalty functions that do not require additional auxiliary variables if first-order solution methods are used. We use the dual fast gradient method to illustrate the effectiveness of our approach. An average speedup of ×8 and a worst case speed-up of ×6 were obtained, compared with the fastest state-of-the-art first-order method for a subsea separation process. Moreover, hardware-in-theloop simulations using an ANSI C implementation on a PLC reveal that our first-order solver outperforms the fastest secondorder solver deployed for the subsea separation process
