Improvement of MBBR-MBR Performance by the Addition of Commercial and 3D-Printed Biocarriers

Moving bed biofilm reactor combined with membrane bioreactor (MBBR-MBR) constitute a highly effective wastewater treatment technology. The aim of this research work was to study the effect of commercial K1 biocarriers (MBBR-MBR K1 unit) and 3D-printed biocarriers fabricated from 13X and Halloysite (...

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Main Authors: Dimitra C. Banti, Petros Samaras, Eleni Kostopoulou, Vassiliki Tsioni, Themistoklis Sfetsas
Format: Article
Language:English
Published: MDPI AG 2023-07-01
Series:Membranes
Subjects:
Online Access:https://www.mdpi.com/2077-0375/13/8/690
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author Dimitra C. Banti
Petros Samaras
Eleni Kostopoulou
Vassiliki Tsioni
Themistoklis Sfetsas
author_facet Dimitra C. Banti
Petros Samaras
Eleni Kostopoulou
Vassiliki Tsioni
Themistoklis Sfetsas
author_sort Dimitra C. Banti
collection DOAJ
description Moving bed biofilm reactor combined with membrane bioreactor (MBBR-MBR) constitute a highly effective wastewater treatment technology. The aim of this research work was to study the effect of commercial K1 biocarriers (MBBR-MBR K1 unit) and 3D-printed biocarriers fabricated from 13X and Halloysite (MBBR-MBR 13X-H unit), on the efficiency and the fouling rate of an MBBR-MBR unit during wastewater treatment. Various physicochemical parameters and trans-membrane pressure were measured. It was observed that in the MBBR-MBR K1 unit, membrane filtration improved reaching total membrane fouling at 43d, while in the MBBR-MBR 13X-H and in the control MBBR-MBR total fouling took place at about 32d. This is attributed to the large production of soluble microbial products (SMP) in the MBBR-MBR 13X-H, which resulted from a large amount of biofilm created in the 13X-H biocarriers. An optimal biodegradation of the organic load was concluded, and nitrification and denitrification processes were improved at the MBBR-MBR K1 and MBBR-MBR 13X-H units. The dry mass produced on the 13X-H biocarriers ranged at 4980–5711 mg, three orders of magnitude larger than that produced on the K1, which ranged at 2.9–4.6 mg. Finally, it was observed that mostly extracellular polymeric substances were produced in the biofilm of K1 biocarriers while in 13X-H mostly SMP.
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spelling doaj.art-db05fab87bb04775a3b0202964bf5eed2023-11-19T02:07:26ZengMDPI AGMembranes2077-03752023-07-0113869010.3390/membranes13080690Improvement of MBBR-MBR Performance by the Addition of Commercial and 3D-Printed BiocarriersDimitra C. Banti0Petros Samaras1Eleni Kostopoulou2Vassiliki Tsioni3Themistoklis Sfetsas4QLAB Private Company, Research & Development, Quality Control and Testing Services, 57008 Thessaloniki, GreeceDepartment of Food Science and Technology, School of Geotechnical Sciences, International Hellenic University, 57400 Thessaloniki, GreeceQLAB Private Company, Research & Development, Quality Control and Testing Services, 57008 Thessaloniki, GreeceQLAB Private Company, Research & Development, Quality Control and Testing Services, 57008 Thessaloniki, GreeceQLAB Private Company, Research & Development, Quality Control and Testing Services, 57008 Thessaloniki, GreeceMoving bed biofilm reactor combined with membrane bioreactor (MBBR-MBR) constitute a highly effective wastewater treatment technology. The aim of this research work was to study the effect of commercial K1 biocarriers (MBBR-MBR K1 unit) and 3D-printed biocarriers fabricated from 13X and Halloysite (MBBR-MBR 13X-H unit), on the efficiency and the fouling rate of an MBBR-MBR unit during wastewater treatment. Various physicochemical parameters and trans-membrane pressure were measured. It was observed that in the MBBR-MBR K1 unit, membrane filtration improved reaching total membrane fouling at 43d, while in the MBBR-MBR 13X-H and in the control MBBR-MBR total fouling took place at about 32d. This is attributed to the large production of soluble microbial products (SMP) in the MBBR-MBR 13X-H, which resulted from a large amount of biofilm created in the 13X-H biocarriers. An optimal biodegradation of the organic load was concluded, and nitrification and denitrification processes were improved at the MBBR-MBR K1 and MBBR-MBR 13X-H units. The dry mass produced on the 13X-H biocarriers ranged at 4980–5711 mg, three orders of magnitude larger than that produced on the K1, which ranged at 2.9–4.6 mg. Finally, it was observed that mostly extracellular polymeric substances were produced in the biofilm of K1 biocarriers while in 13X-H mostly SMP.https://www.mdpi.com/2077-0375/13/8/690MBBR-MBRbiofilm3D-printed biocarriersKaldnes K1 biocarriers13X-halloysite biocarriersmembrane fouling
spellingShingle Dimitra C. Banti
Petros Samaras
Eleni Kostopoulou
Vassiliki Tsioni
Themistoklis Sfetsas
Improvement of MBBR-MBR Performance by the Addition of Commercial and 3D-Printed Biocarriers
Membranes
MBBR-MBR
biofilm
3D-printed biocarriers
Kaldnes K1 biocarriers
13X-halloysite biocarriers
membrane fouling
title Improvement of MBBR-MBR Performance by the Addition of Commercial and 3D-Printed Biocarriers
title_full Improvement of MBBR-MBR Performance by the Addition of Commercial and 3D-Printed Biocarriers
title_fullStr Improvement of MBBR-MBR Performance by the Addition of Commercial and 3D-Printed Biocarriers
title_full_unstemmed Improvement of MBBR-MBR Performance by the Addition of Commercial and 3D-Printed Biocarriers
title_short Improvement of MBBR-MBR Performance by the Addition of Commercial and 3D-Printed Biocarriers
title_sort improvement of mbbr mbr performance by the addition of commercial and 3d printed biocarriers
topic MBBR-MBR
biofilm
3D-printed biocarriers
Kaldnes K1 biocarriers
13X-halloysite biocarriers
membrane fouling
url https://www.mdpi.com/2077-0375/13/8/690
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AT elenikostopoulou improvementofmbbrmbrperformancebytheadditionofcommercialand3dprintedbiocarriers
AT vassilikitsioni improvementofmbbrmbrperformancebytheadditionofcommercialand3dprintedbiocarriers
AT themistoklissfetsas improvementofmbbrmbrperformancebytheadditionofcommercialand3dprintedbiocarriers