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Utilizing anaerobic substrate distribution for growth of aerobic granular sludge in continuous-flow reactors.
Haaksman, Viktor A; van Dijk, Edward J H; Al-Zuhairy, Salah; Mulders, Michel; Loosdrecht, Mark C M van; Pronk, Mario.
Afiliação
  • Haaksman VA; Delfluent Services, Peuldreef 4, Den Hoorn, 2635 BX, The Netherlands. Electronic address: v.a.haaksman@tudelft.nl.
  • van Dijk EJH; Royal HaskoningDHV, Laan 1914 35, Amersfoort, 3800 AL, The Netherlands.
  • Al-Zuhairy S; Delfluent Services, Peuldreef 4, Den Hoorn, 2635 BX, The Netherlands.
  • Mulders M; Delfluent Services, Peuldreef 4, Den Hoorn, 2635 BX, The Netherlands.
  • Loosdrecht MCMV; Department of Biotechnology, Delft University of Technology, Van der Maasweg 9, Delft, 2629 HZ, The Netherlands.
  • Pronk M; Department of Biotechnology, Delft University of Technology, Van der Maasweg 9, Delft, 2629 HZ, The Netherlands; Royal HaskoningDHV, Laan 1914 35, Amersfoort, 3800 AL, The Netherlands. Electronic address: m.pronk@tudelft.nl.
Water Res ; 257: 121531, 2024 Jun 15.
Article em En | MEDLINE | ID: mdl-38701553
ABSTRACT
The development of continuous flow reactors (CFRs) employing aerobic granular sludge (AGS) for the retrofit of existing wastewater treatment plants (WWTPs) using a continuous-flow activated sludge (CFAS) system has garnered increasing interest. This follows the worldwide adoption of AGS technology in sequencing batch reactors (SBRs). The better settleability of AGS compared to AS allows for process intensification of existing wastewater treatment plants without the difficult conversion of often relatively shallow CFRs to deeper AGS-SBRs. To retrofit existing CFAS systems with AGS, achieving both increased hydraulic capacity and enhanced biological nutrient removal necessitates the formation of granular sludge based on the same selective pressures applied in AGS-SBRs. Previous efforts have focussed mainly on the selective wasting of flocculent sludge and retaining granular sludge to drive aerobic granulation. In this study a pilot-scale CFR was developed to best mimic the implementation of the granulation mechanisms of full-scale AGS-SBRs. The pilot-scale reactor was fed with pre-settled municipal wastewater. We established metrics to assess the degree to which the proposed mechanisms were implemented in the pilot-scale CFR and compared them to data from full-scale AGS-SBRs, specifically with respect to the anaerobic distribution of granule forming substrates (GFS). The selective pressures for granular sludge formation were implemented through inclusion of anaerobic upflow selectors with a water depth of 2.5 meters, which yielded a sludge with properties similar to AGS from full-scale SBRs. In comparison to the CFAS system at Harnaschpolder WWTP treating the same pre-settled wastewater, a more than twofold increase in volumetric removal capacity for both phosphorus and nitrogen was achieved. The use of a completely mixed anaerobic selector, as opposed to an anaerobic upflow selector, caused a shift in EBPR activity from the largest towards the smallest size class, while nitrification was majorly unaffected. Anaerobic selective feeding via bottom-feeding is, therefore, favorable for the long-term stability of AGS, especially for less acidified wastewater. The research underlines the potential of AGS for enhancing the hydraulic and biological treatment capacity of existing CFAS systems.
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Texto completo: 1 Coleções: 01-internacional Base de dados: MEDLINE Assunto principal: Esgotos / Eliminação de Resíduos Líquidos / Reatores Biológicos Idioma: En Revista: Water Res Ano de publicação: 2024 Tipo de documento: Article

Texto completo: 1 Coleções: 01-internacional Base de dados: MEDLINE Assunto principal: Esgotos / Eliminação de Resíduos Líquidos / Reatores Biológicos Idioma: En Revista: Water Res Ano de publicação: 2024 Tipo de documento: Article