Treatment of cheese whey by a cross-flow anaerobic membrane bioreactor

Biological and filtration performance

Journal Article (2019)
Author(s)

Recep Dereli (Istanbul Technical University, TU Delft - Sanitary Engineering)

F. P. van der Zee (Veolia Water Technologies)

Izzet Ozturk (Istanbul Technical University)

J.B. van Lier (TU Delft - Sanitary Engineering)

Research Group
Sanitary Engineering
Copyright
© 2019 R.K. Dereli, F. van der Zee, Izzet Ozturk, J.B. van Lier
DOI related publication
https://doi.org/10.1016/j.envres.2018.09.021
More Info
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Publication Year
2019
Language
English
Copyright
© 2019 R.K. Dereli, F. van der Zee, Izzet Ozturk, J.B. van Lier
Research Group
Sanitary Engineering
Bibliographical Note
Green Open Access added to TU Delft Institutional Repository ‘You share, we take care!’ – Taverne project https://www.openaccess.nl/en/you-share-we-take-care Otherwise as indicated in the copyright section: the publisher is the copyright holder of this work and the author uses the Dutch legislation to make this work public.@en
Volume number
168
Pages (from-to)
109-117
Reuse Rights

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Abstract

Whey, produced in large quantities during cheese production, is a rapidly fermentable high strength wastewater characterized by a high biodegradability and low alkalinity. In this study, a lab-scale cross-flow anaerobic membrane bioreactor was used to address the commonly experienced difficulties such as unstable reactor performance and unexpected biomass losses when treating whey wastewater with conventional anaerobic reactors. The anaerobic membrane bioreactor provided a stable treatment performance, i.e. more than 90% chemical oxygen demand removal, and moderate membrane fluxes between 8 and 11 L m−2 h−1 could be obtained, applying a low cross-flow velocity of about 0.5 m s−1. Short term critical flux tests revealed that higher fluxes up to 36 L m−2 h−1 are possible at elevated cross-flow velocities and/or reduced mixed liquor suspended solids concentrations. Sludge filterability indicated by capillary suction time and specific resistance to filtration deteriorated throughout the study. Chemical cleaning efficiency gradually decreased, indicating irreversible membrane fouling during long term operation.

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