The use of factorial design for modeling membrane distillation

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dc.authorid0000-0001-8259-4786
dc.contributor.authorOnsekizoğlu, Pelin
dc.contributor.authorBahçeci, Kazım Savaş
dc.contributor.authorAcar, Jale
dc.date.accessioned2019-05-13T08:57:23Z
dc.date.available2019-05-13T08:57:23Z
dc.date.issued2010
dc.departmentHitit Üniversitesi, Mühendislik Fakültesi, Gıda Mühendisliği Bölümü
dc.description.abstractA two-level factorial experimental design was used to investigate the influence of the main operating parameters on evaporation flux and soluble solid content of apple juice during concentration through osmotic distillation (OD) and membrane distillation (MD) processes. The factorial models have been obtained from experimental design to study all interactions among the considered parameters (osmotic agent concentration (0-65% CaCl2), flow rate (10-30 L/h) and temperature difference between feed and osmotic agent (10-30 °C)) and validated statistically by analysis of variance (ANOVA). For both responses, the osmotic agent concentration was the most influential factor. The magnitude of the main influence of CaCl2 concentration was followed by the temperature difference and flow rate, respectively. The analysis of the experimental responses revealed that CaCl2 concentration and temperature difference had significant interactive effects on evaporation flux. All interactions between the studied parameters were significant in the case of soluble solid content at the 99% confidence level. Although the interaction terms have significant effects, their levels were only a small amount compared to linear effects. The predicted responses were compared with the experimental ones. In general, the predicted values were in reasonable agreement with the experimental data, further confirming the very good prediction ability of the models. © 2009 Elsevier B.V. All rights reserved.
dc.identifier.citationOnsekizoglu, P., Bahceci, K. S., & Acar, J. (2010). The use of factorial design for modeling membrane distillation. Journal of Membrane Science, 349(1-2), 225-230.
dc.identifier.doi10.1016/j.memsci.2009.11.049
dc.identifier.endpage230en_US
dc.identifier.issn0376-7388
dc.identifier.issue01.Feben_US
dc.identifier.scopusqualityQ1
dc.identifier.startpage225en_US
dc.identifier.urihttps://doi.org/10.1016/j.memsci.2009.11.049
dc.identifier.urihttps://hdl.handle.net/11491/913
dc.identifier.volume349en_US
dc.identifier.wosqualityN/A
dc.indekslendigikaynakWeb of Science
dc.indekslendigikaynakScopus
dc.language.isoen
dc.relation.ispartofJournal of Membrane Science
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı
dc.rightsinfo:eu-repo/semantics/closedAccess
dc.subjectFactorial Designen_US
dc.subjectMembrane Distillationen_US
dc.subjectOsmotic Agenten_US
dc.subjectOsmotic Distillationen_US
dc.subjectTemperatureen_US
dc.titleThe use of factorial design for modeling membrane distillation
dc.typeArticle

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