Integrated resource recovery from aerobic granular sludge plants

Journal Article (2023)
Author(s)

T.M.S.M. Bahgat (Wetsus, European Centre of Excellence for Sustainable Water Technology, TU Delft - BT/Environmental Biotechnology)

P. Wilfert (TU Delft - BT/Environmental Biotechnology)

L. Korving (Wetsus, European Centre of Excellence for Sustainable Water Technology)

Mark M.C. van Loosdrecht (TU Delft - BT/Environmental Biotechnology)

Research Group
BT/Environmental Biotechnology
Copyright
© 2023 T.M.S.M. Bahgat, P.K. Wilfert, Leon Korving, Mark C.M. van Loosdrecht
DOI related publication
https://doi.org/10.1016/j.watres.2023.119819
More Info
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Publication Year
2023
Language
English
Copyright
© 2023 T.M.S.M. Bahgat, P.K. Wilfert, Leon Korving, Mark C.M. van Loosdrecht
Research Group
BT/Environmental Biotechnology
Volume number
234
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Abstract

The study evaluated the combined phosphorus, nitrogen, methane, and extracellular polymeric substances (EPS) recovery from aerobic granular sludge (AGS) wastewater treatment plants. About 30% of sludge organics are recovered as EPS and 25–30% as methane (≈260 ml methane/g VS) by integrating alkaline anaerobic digestion (AD). It was shown that 20% of excess sludge total phosphorus (TP) ends in the EPS. Further, 20–30% ends in an acidic liquid waste stream (≈600 mg PO4-P/L), and 15% in the AD centrate (≈800 mg PO4-P/L) as ortho-phosphates in both streams and is recoverable via chemical precipitation. 30% of sludge total nitrogen (TN) is recovered as organic nitrogen in the EPS. Ammonium recovery from the alkaline high-temperature liquid stream is attractive, but it is not feasible for existing large-scale technologies because of low ammonium concentration. However, ammonium concentration in the AD centrate was calculated to be 2600 mg NH4-N/L and ≈20% of TN, making it feasible for recovery. The methodology used in this study consisted of three main steps. The first step was to develop a laboratory protocol mimicking demonstration-scale EPS extraction conditions. The second step was to establish mass balances over the EPS extraction process on laboratory and demonstration scales within a full-scale AGS WWTP. Finally, the feasibility of resource recovery was evaluated based on concentrations, loads, and integration of existing technologies for resource recovery.