G
Gabriele Pannocchia
Researcher at University of Pisa
Publications - 133
Citations - 3153
Gabriele Pannocchia is an academic researcher from University of Pisa. The author has contributed to research in topics: Model predictive control & Optimization problem. The author has an hindex of 24, co-authored 128 publications receiving 2741 citations. Previous affiliations of Gabriele Pannocchia include Wisconsin Alumni Research Foundation.
Papers
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Is suboptimal nonlinear MPC inherently robust
TL;DR: In this article, the authors study the inherent robust stability properties of nonlinear discrete-time systems controlled by suboptimal model predictive control (MPC) and prove robust exponential stability with respect to small, but otherwise arbitrary, additive process disturbances and state measurement/estimation errors.
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Optimal modified models for robust predictive controllers
Gabriele Pannocchia,D. Semino +1 more
TL;DR: In this article, an optimization technique has been developed in order to find the alternative model to be used in place of the nominal one, which offers the best compromise between nominal performance and robustness to uncertainty.
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Data-driven Models for Advanced Control of Acid Gas Treatment in Waste-to-energy Plants
Riccardo Bacci di Capaci,Gabriele Pannocchia,Alessandro Dal Pozzo,Giacomo Antonioni,Valerio Cozzani +4 more
TL;DR: In this paper , the acid gas removal line of an Italian plant, based on the injection of hydrated lime, Ca(OH)2, for the abatement of hydrogen chloride, HCl, is investigated.
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Robust Multivariable Inverse-Based Controllers: Theory and Application
D. Semino,Gabriele Pannocchia +1 more
TL;DR: The problem of designing robust inverse-based controllers for multivariable ill-conditioned processes is addressed and a methodology is developed aimed at finding modified models that are able to make the overall control structure robust.
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Analytical RTO for a critical distillation process based on offline rigorous simulation
TL;DR: In this article , an analytical real-time optimization (RTO) approach for distillation processes is presented, which calculates the setpoint of manipulated variables according to operating strategy exploiting an analytical generalized formulation.