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Hemijska industrija 2011 Volume 65, Issue 2, Pages: 131-138
https://doi.org/10.2298/HEMIND101129074I
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Microfiltration of wheat starch suspensions using multichannel ceramic membrane

Ikonić Bojana B.
Zavargo Zoltan Z.
Jokić Aleksandar I. ORCID iD icon (Faculty of Technology, University of Novi Sad, Novi Sad, Serbia)
Šereš Zita I. ORCID iD icon
Vatai Gyula N.
Peruničić Mihailo B.

This work investigates influence of different process parameters such as transmembrane pressure, flow rate and concentration of wheat starch suspension on the average permeate flux and permeate flux decline. Used membrane in all experiments was 19 channels ceramic membrane with 0.2 μm pore size. Experimental results were analyzed using response surface methodology. It is observed that the significant average permeate flux enhancement of 200% was achieved by the increase of the transmembrane pressure, while the increase of flow rate and concentration affected the increase in average permeate flux in the range of 40-100%. Permeate flux decline was almost independent of the transmembrane pressure, but the increase of the flow rate, as well as the decrease of the concentration led to decrease of permeate flux decline in the range of 20-50%.

Keywords: cross-flow microfiltration, starch suspension, full factorial design, response surface methodology

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