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Integrated design and control using a dynamic inversely controlled process model

Sharifzadeh, M; Thornhill, NF; (2013) Integrated design and control using a dynamic inversely controlled process model. Computers & Chemical Engineering , 48 pp. 121-134. 10.1016/j.compchemeng.2012.08.009. Green open access

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Abstract

The profitability of chemical processes depends on their design and control. If the process design is fixed, there is little room left to improve control performance. Many commentators suggest design and control should be integrated. Nevertheless, the integrated problem is highly complex and intractable. This article proposes an optimization framework using a dynamic inversely controlled process model. The combinatorial complexities associated with the controllers are disentangled from the formulation, but the process and its control structure are still designed simultaneously. The new framework utilizes a multi-objective function to explore the trade-off between process and control objectives. The proposed optimization framework is demonstrated on a case study from the literature. Two parallel solving strategies are applied, and their implementations are explained. They are dynamic optimization based on (i) sequential integration and (ii) full discretization. The proposed integrated design and control optimization framework successfully captured the trade-off between control and process objectives.

Type: Article
Title: Integrated design and control using a dynamic inversely controlled process model
Open access status: An open access version is available from UCL Discovery
DOI: 10.1016/j.compchemeng.2012.08.009
Publisher version: http://dx.doi.org/10.1016/j.compchemeng.2012.08.00...
Language: English
Additional information: This version is the author accepted manuscript. For information on re-use, please refer to the publisher’s terms and conditions.
Keywords: Integrated design and control of chemical processes, Stochastic mixed-integer dynamic programming, Control structure selection, Multi-objective optimization, MULTIVARIABLE NONLINEAR PROCESSES, OUTPUT-FEEDBACK CONTROL, FLEXIBILITY ANALYSIS, PLANTWIDE CONTROL, CHEMICAL-PLANTS, CONTROL-SYSTEMS, OPTIMIZATION, CONTROLLABILITY, SELECTION, PERSPECTIVE
UCL classification: UCL
UCL > Provost and Vice Provost Offices
UCL > Provost and Vice Provost Offices > UCL BEAMS
UCL > Provost and Vice Provost Offices > UCL BEAMS > Faculty of Engineering Science
URI: https://discovery.ucl.ac.uk/id/eprint/10023913
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