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Sewage sludge treatment in a thermophilic membrane reactor (TMR): factors affecting foam formation

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Abstract

Foam formation in the excess sludge treatment facilities of biological wastewater treatment plants (WWTPs) may represent a critical issue as it could lead to several operative problems and reduce the overall plant performance. This trouble also affects a novel technology recently proposed for sludge minimization, the thermophilic membrane reactor (TMR), operating with alternate aeration/non-aeration cycles. This technology, which has proven to be extremely resilient and suitable for treating industrial wastewater of different nature, demonstrated a high potential also as a solution for integrating existing WWTPs, aiming at the “zero sludge production.” In this work, an experimental study was conducted with a TMR pilot plant (fed daily with thickened sewage sludge) by adjusting the duration of aeration/non-aeration alternate cycles. Extracellular polymeric substance (EPS) concentration (and its soluble and bound fractions) has been monitored along with foaming power indices. The results highlight that foaming can be correlated to the presence of soluble protein fraction of EPS. Moreover, EPS production seems to be reduced by increasing the duration of the non-aeration cycles: optimal operating conditions resulted 2 h of aeration followed by 6 h of non-aeration. These conditions allow to obtain an EPS concentration of 500 mg L−1 with respect to 2300 mg L−1 measured at the beginning of experimental work.

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Abbreviations

ATAD:

Autothermal thermophilic aerobic digestion

COD:

Chemical oxygen demand

CV:

Coefficient of variation

EPS:

Extracellular polymeric substance

EPSb :

Bound extracellular polymeric substance

EPSb,c :

Carbohydrate fraction of bound extracellular polymeric substance

EPSb,p :

Protein fraction of bound extracellular polymeric substance

FP:

Foaming power index calculated as consumed sample per liter of supplied air

FP2:

Foaming power index calculated as foam volume produced per liter of supplied air

MBR:

Membrane bioreactor

R 2 :

Coefficient of determination

SMP:

Soluble microbial products

SMPc :

Carbohydrate fraction of soluble microbial products

SMPp :

Protein fraction of soluble microbial products

TMR:

Thermophilic membrane reactor

TN:

Total nitrogen

TP:

Total phosphorus

TS:

Total solids

UF:

Ultrafiltration

UM:

Unit of measurement

VS:

Volatile solids

WWTP:

Wastewater treatment plant

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Acknowledgments

The authors wish to thank Idroclean Spa (Casirate d’Adda, BG, Italy) for technical and financial support to the research.

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Correspondence to Maria Cristina Collivignarelli.

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The authors declare that they have no conflict of interest.

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This article does not contain any studies with human participants or animals performed by any of the authors.

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Informed consent was obtained from all individual participants included in the study.

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Responsible editor: Angeles Blanco

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Collivignarelli, M.C., Castagnola, F., Sordi, M. et al. Sewage sludge treatment in a thermophilic membrane reactor (TMR): factors affecting foam formation. Environ Sci Pollut Res 24, 2316–2325 (2017). https://doi.org/10.1007/s11356-016-7983-4

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  • DOI: https://doi.org/10.1007/s11356-016-7983-4

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