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Design and production planning for multiproduct dehydration plants

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dc.contributor.author Kiranoudis, CT en
dc.contributor.author Maroulis, ZB en
dc.contributor.author Marinos-Kouris, D en
dc.date.accessioned 2014-03-01T01:10:54Z
dc.date.available 2014-03-01T01:10:54Z
dc.date.issued 1995 en
dc.identifier.issn 0098-1354 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/11489
dc.subject Chemical Engineering en
dc.subject Generic Model en
dc.subject Mathematical Model en
dc.subject Nonlinear Regression en
dc.subject Optimization Problem en
dc.subject Production Planning en
dc.subject Production Process en
dc.subject Profitability en
dc.subject Raw Materials en
dc.subject Long Range en
dc.subject Time Varying en
dc.subject.classification Computer Science, Interdisciplinary Applications en
dc.subject.classification Engineering, Chemical en
dc.subject.other Computer Techniques en
dc.subject.other Drying en
dc.title Design and production planning for multiproduct dehydration plants en
heal.type journalArticle en
heal.identifier.primary 10.1016/0098-1354(94)00069-7 en
heal.identifier.secondary http://dx.doi.org/10.1016/0098-1354(94)00069-7 en
heal.language English en
heal.publicationDate 1995 en
heal.abstract Drying operations constitute an important field of chemical engineering, which is still governed by empiricism. This paper deals with two important aspects related to the construction and operation of dehydration plants. The design problem involves the determination of process flowsheet structure, when a nominal production level is specified for all products processed in the plant. The production planning problem describes the production policy of the plant within a long-range planning horizon, under time-varying product demand and market prices of raw materials and saleable products. The policy adopted assigns production levels and duration of production runs for each product processed, in each one of the plant processors, at a certain time period, within the planning horizon. The objective in each approach is to optimize the total annual profit resulting from the construction of a new plant or the operation of an existing one. The process was described by deducing the mathematical model of conveyor-belt dryers. For the forementioned problems, appropriate formulations were developed and studied. The most general model presented involves numerous integer and continuous decision variables and a large number of space variables and constraints, resulting in cumbersome calculations and tremendous computational load. For the reduction of the computational effort, a shortcut modeling of total annual plant cost was proposed and evaluated from the operational data of a large number of possible flowsheet structures, through a simple analytical equation. The parameters of the proposed shortcut equation were estimated by nonlinear regression over an extensive number of computed points; each one of them was determined by solving an NLP optimization problem. The design and production problems were formulated as MINLP problems in which use of the shortcut cost equation reduced drastically the computational effort involved. Related problems (i.e. process modification and design under production planning criteria) were also taken into consideration. Characteristic examples were presented in order to demonstrate the effectiveness of each proposed approach. en
heal.publisher PERGAMON-ELSEVIER SCIENCE LTD en
heal.journalName Computers and Chemical Engineering en
dc.identifier.doi 10.1016/0098-1354(94)00069-7 en
dc.identifier.isi ISI:A1995QN82700008 en
dc.identifier.volume 19 en
dc.identifier.issue 5 en
dc.identifier.spage 581 en
dc.identifier.epage 606 en


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