2020
DOI: 10.1016/j.conengprac.2020.104580
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Constrained iterative learning control of batch transesterification process under uncertainty

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Cited by 9 publications
(7 citation statements)
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“…The kinetic model involving the mass balances on the reactants is adopted from [43,44] and is given as:…”
Section: System Descriptionmentioning
confidence: 99%
“…The kinetic model involving the mass balances on the reactants is adopted from [43,44] and is given as:…”
Section: System Descriptionmentioning
confidence: 99%
“… 30 , 31 Along similar lines, a constrained batch-to-batch ILC that utilizes the previous knowledge of the process to obtain the updated control policy was proposed. 32 , 33 It is also shown that latent variable point-to-point iterative learning MPC (LV-PTP-ILMPC) shows faster convergence and better efficiency as compared to the PTP-ILC. 34 Tube-based ILMPC proved to show superior performance for nonlinear batch processes as compared to the ILMPC.…”
Section: Introductionmentioning
confidence: 99%
“…In related work, to capture inherently time-varying parameters and non-linearities, the linear parameter varying model has been used in a model learning MPC framework for the batch process . Further, it has been shown that a combination of ILC with appropriate process knowledge and system identification techniques helps in multi-variable nonlinear tracking problem. , Along similar lines, a constrained batch-to-batch ILC that utilizes the previous knowledge of the process to obtain the updated control policy was proposed. , It is also shown that latent variable point-to-point iterative learning MPC (LV-PTP-ILMPC) shows faster convergence and better efficiency as compared to the PTP-ILC . Tube-based ILMPC proved to show superior performance for nonlinear batch processes as compared to the ILMPC .…”
Section: Introductionmentioning
confidence: 99%
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“…With less modelling investigation about the temperature control of a semi-batch chemical reactor, a feedback-feedforward ILC is proposed for temperature trajectory tracking (Mezghani et al, 2002). In the case of model uncertainties and unmeasured disturbances, a constrained quadratic programming problem based batch-to-batch ILC framework is demonstrated for optimizing the endpoint fatty acid methyl esters concentration by controlling the hot water flow profile passing through the reactor jacket (De et al, 2020). By using batch-wise linearized models identified from operation data, a batch-to-batch ILC is designed for a fed-batch fermentation process (Jewaratnam et al, 2012).…”
Section: Introductionmentioning
confidence: 99%