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Licensed Unlicensed Requires Authentication Published by De Gruyter March 23, 2023

Process configuration of combined ozonolysis and anaerobic digestion for wastewater treatment

  • Benton Otieno ORCID logo EMAIL logo , Mervyn Khune , John Kabuba and Peter Osifo
From the journal Physical Sciences Reviews

Abstract

Industrial activities and increased human population have made wastewater streams not entirely amenable to conventional treatment methods. Anaerobic digestion (AD) can treat such wastewaters with the advantage of bioresource recovery. However, the presence of solids and recalcitrant compounds in most wastewater streams may affect the AD process. Thus, combining AD with advanced oxidation processes (AOPs) such as ozonolysis is necessary. Ozonolysis can improve the biodegradability of wastewater substrates or eliminate biorecalcitrant pollutants that escape the AD process. This study combined ozonolysis with AD to treat waste activated sludge (WAS) and distillery wastewater (DWW). When applied as a pre-treatment, ozonolysis caused the rigid cell walls in WAS to rupture and solubilised the extracellular polymeric substances (EPS), leading to increased biodegradability. For the DWW, ozonolysis pre-treatment reduced the biorecalcitrant aromatic compounds to simple aliphatic compounds, thereby increasing biodegradability. In the ensuing anaerobic process, the WAS pre-treatment improved TSS and COD reductions and a 230% increase in cumulative biogas production. For the DWW, the ozonolysis pre-treatment did not significantly impact COD reduction or biogas production; however, ozonolysis as a post-treatment removed the color causing biorecalcitrant melanoidins from the anaerobically digested effluent and solubilised the sludge (TSS) washed out from the AD unit. Therefore, the AD-ozonolysis process configuration depends on the substrate being treated. Ozonolysis is best applied pre-AD for WAS treatment and post-AD for DWW.


Corresponding author: Benton Otieno, Research Centre for Renewable Energy and Water, Vaal University of Technology, Vanderbijlpark, South Africa; and Department of Chemical Engineering, Vaal University of Technology, Vanderbijlpark, South Africa, E-mail:

  1. Author contributions: All the authors have accepted responsibility for the entire content of this submitted manuscript and approved submission.

  2. Research funding: The research of this article was supported by the German Academic Exchange Service (DAAD) within the framework of the climap Africa programme with funds from the Federal Ministry of Education and Research and the Water Research Commission (WRC, Project no. C2020/2021-00426) of South Africa.

  3. Conflict of interest: There are no competing or conflicts of interest to declare.

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Received: 2022-11-03
Accepted: 2023-01-31
Published Online: 2023-03-23

© 2023 Walter de Gruyter GmbH, Berlin/Boston

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