2010
DOI: 10.1016/j.jprocont.2010.06.010
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Plantwide Optimizing Control of a continuous bioethanol production process

Abstract: A mis padres por su amor y apoyo incondicional.A Huguis por ser mi inspiración y el sol de mi vida. I would also like to thank M. Eng. Miguel Ricardo Hernandez-Garcia from University of South California for the opportunity to use high performance computation in some of the simulations. Man muss Optimist sein Max PlanckMi agradecimiento de todo corazón a mis padres por su amor y apoyo incondicional durante toda mi vida. A Huguis por ser mi compañero en esta gran aventura que es la vida, y por ser mi sol especia… Show more

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Cited by 49 publications
(44 citation statements)
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“…In line with the conclusions of Ochoa et al (2010) and Aikman and Pridmore (2001), it should be stated that lack of buyersupplier knowledge forms an important source of production uncertainty. The lack of knowledge related to the measurement of biomass quality by the local buyer-suppliers has become evident for instance, as only one of the interviewed rubber farmers was able to describe a quality measurement process.…”
Section: Production and Operational Uncertaintymentioning
confidence: 69%
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“…In line with the conclusions of Ochoa et al (2010) and Aikman and Pridmore (2001), it should be stated that lack of buyersupplier knowledge forms an important source of production uncertainty. The lack of knowledge related to the measurement of biomass quality by the local buyer-suppliers has become evident for instance, as only one of the interviewed rubber farmers was able to describe a quality measurement process.…”
Section: Production and Operational Uncertaintymentioning
confidence: 69%
“…Education is shown by Aikman and Pridmore (2001) to be an important factor leading to externally caused machine failures, either through improper machine usage or by affecting the quality of inputs delivered (Ochoa et al, 2010).…”
Section: Methodsmentioning
confidence: 99%
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“…Instrumented with liquid level sensor to determine the reaction volume, its set-point was set to half of total volume and product concentration set-point to 60 kg.m -3 . For liquid level, a single-input-single-output (SISO) control loop was implemented in reason that it is a simple and reliable strategy for level control and was also successfully applied by Ochoa et al (2010a). Two different strategies were tested for product concentration, the first based on a SISO loop, comparing the process variable with set-point and actuating in enzymatic solution inlet flow because it is the most affecting variable to glucose concentration.…”
Section: Resultsmentioning
confidence: 99%
“…For example, Ochoa et al apply plant-wide one-level and two-level methods to a bioethanol production process, contrasting these to a more conventional decentralized RTO method [11]. Zavala et al explicitly account for forecasting uncertainty in the optimal control of energy systems [12].…”
Section: Introductionmentioning
confidence: 99%