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Pareto design of fluidized bed dryers

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dc.contributor.author Krokida, MK en
dc.contributor.author Kiranoudis, CT en
dc.date.accessioned 2014-03-01T01:15:46Z
dc.date.available 2014-03-01T01:15:46Z
dc.date.issued 2000 en
dc.identifier.issn 1385-8947 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/13730
dc.subject Pareto design en
dc.subject fluidized bed dryers en
dc.subject multiobjective optimization en
dc.subject mathematical modeling en
dc.subject.classification Engineering, Chemical en
dc.subject.other CONVECTIVE INDUSTRIAL DRYERS en
dc.subject.other HEAT en
dc.subject.other VEGETABLES en
dc.subject.other SIMULATION en
dc.subject.other FOODS en
dc.title Pareto design of fluidized bed dryers en
heal.type journalArticle en
heal.identifier.primary 10.1016/S1385-8947(00)00140-6 en
heal.identifier.secondary http://dx.doi.org/10.1016/S1385-8947(00)00140-6 en
heal.language English en
heal.publicationDate 2000 en
heal.abstract Most of the research efforts in the field of fluidized dryer design, focus on the evaluation of the appropriate structural and operational process variables so that total annual plant cost involved is optimized. However, the increasing need for dehydrated products of the highest quality, imposes the development of new criteria that, together with cost components, determine the design rules for any drying process. Quality of dehydrated products is a complex resultant of properties characterizing the final products, where the most important one is color. Color is represented by three parameters: redness, yellowness and lightness. These three parameters of a dried product should deviate from that of its original material as little as possible. In this case, fluidized bed dryer design is a complex multi-objective optimization problem, involving the color deviation and the unit cost of final product as an objective vector and as constraints described in process models. The mathematical model of the dryer was developed and the fundamental color deterioration laws and critical financial parameters were determined for the fluidized bed drying process. In this paper, non-preference multi-criteria optimization methods were used and the Pareto-optimal set of efficient solutions was evaluated. An example for drying of sliced potato was studied in detail to demonstrate the design procedure, the process performance as well as the effectiveness of the proposed approach. (C) 2000 Elsevier Science S.A. All rights reserved. en
heal.publisher ELSEVIER SCIENCE SA en
heal.journalName CHEMICAL ENGINEERING JOURNAL en
dc.identifier.doi 10.1016/S1385-8947(00)00140-6 en
dc.identifier.isi ISI:000088891600001 en
dc.identifier.volume 79 en
dc.identifier.issue 1 en
dc.identifier.spage 1 en
dc.identifier.epage 12 en


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