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dc.contributor.authorRahman, Imran-
dc.contributor.authorAhmad, Arsalan-
dc.contributor.authorKumar, Prakash-
dc.contributor.authorKulkarni, Bhaskar D.-
dc.date.accessioned2024-12-13T09:22:35Z-
dc.date.available2024-12-13T09:22:35Z-
dc.date.issued2008-
dc.identifier.citation10.2202/1934-2659.1111en_US
dc.identifier.urihttp://localhost:8080/xmlui/handle/123456789/2053-
dc.descriptionNITWen_US
dc.description.abstractPurified lactic acid is used for production of biodegradable polymer. Esterification with methanol and subsequent hydrolysis in distillation column using cation exchange resin as catalyst to produce purified lactic acid has obvious advantages. In this paper, we present a theoretical study on optimization of industrial production (1000 t/year) of pure lactic acid using differential evolution (DE), a robust global optimization technique. The objective function is to minimize the overall cost with a view to obtain the optimized values of the decision variables: esterification reaction temperature, number of stages, feed location, reflux ratio, catalyst weight, number of reactive stages and position of reactive stages for hydrolysis.en_US
dc.language.isoenen_US
dc.publisherChemical Product and Process Modelingen_US
dc.subjectreactive distillation,en_US
dc.subjectDifferential evolution,en_US
dc.subjectLactic aciden_US
dc.titleOptimization of a Continuous Process for the Recovery of Lactic Acid Using Differential Evolution Algorithmen_US
dc.typeArticleen_US
Appears in Collections:Chemical Engineering

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