Transactions on Engineering Technologies 2018
DOI: 10.1007/978-981-10-7488-2_4
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Improvement of Maximum Production in the Batch Transesterification Reactor of Biodiesel by Using Nonlinear Model Based Control

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Cited by 3 publications
(7 citation statements)
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“…State observers have already been used as a strategy to estimate variables [5,9,[19][20][21][22], parameters [21], and even the reaction heat [10] in the homogeneous transesterification of oils for biodiesel production. The estimated variables are used as soft sensors in supervision systems or as elements in control strategies [21]; the final objective is to enhance the performance of reactors for biodiesel production.…”
Section: Discussionmentioning
confidence: 99%
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“…State observers have already been used as a strategy to estimate variables [5,9,[19][20][21][22], parameters [21], and even the reaction heat [10] in the homogeneous transesterification of oils for biodiesel production. The estimated variables are used as soft sensors in supervision systems or as elements in control strategies [21]; the final objective is to enhance the performance of reactors for biodiesel production.…”
Section: Discussionmentioning
confidence: 99%
“…The methodology of implementing an extended Luenberger observer to estimate the concentration of TG, M, E, and G throughout the transesterification reaction may be the easiest one and offers a balance between precision and complexity. In comparison with other methods such as the EKF [5,10,38], fuzzy methods [19,20], and multimodel methods [22,23], the computational load of Luenberger observers is lower since no recurrent calculations are required. The reported observers consider six [5,10,20] or four [19,21] differential equations; multiobservers consider two equations or set of models with two equations [9,22], but these are reduced models, and only two variables are estimated.…”
Section: Discussionmentioning
confidence: 99%
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