2009
DOI: 10.3182/20090506-3-sf-4003.00048
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Closed Loop Dynamic Optimization of a Petroleum Refinery Process

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Cited by 3 publications
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“…Another approach on process optimization uses appropriate selection of control structure along with RTO (without MPC) to achieve maximum process profitability, this has been well discussed by Engell (2007). Currently, there is important interest on MPC and RTO integration, either as a whole dynamic RTO (Aho et al, 2009) or as an economic MPC (Amrit et al, 2013;Ellis et al, 2014;Ellis and Christofides, 2015), or separately with focus on robust and stable integration (Alvarez and Odloak, 2010;De Souza et al, 2010). Ideas of the incorporation of economic objective functions into the MPC formulation emerged in the 90s as nonlinear MPC flourished in the research community.…”
Section: C122 About Real-time Optimizationmentioning
confidence: 99%
“…Another approach on process optimization uses appropriate selection of control structure along with RTO (without MPC) to achieve maximum process profitability, this has been well discussed by Engell (2007). Currently, there is important interest on MPC and RTO integration, either as a whole dynamic RTO (Aho et al, 2009) or as an economic MPC (Amrit et al, 2013;Ellis et al, 2014;Ellis and Christofides, 2015), or separately with focus on robust and stable integration (Alvarez and Odloak, 2010;De Souza et al, 2010). Ideas of the incorporation of economic objective functions into the MPC formulation emerged in the 90s as nonlinear MPC flourished in the research community.…”
Section: C122 About Real-time Optimizationmentioning
confidence: 99%