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Economic feasibility and direct greenhouse gas emissions from different phosphorus recovery methods in Swedish wastewater treatment plants
Luleå University of Technology, Department of Engineering Sciences and Mathematics, Energy Science. Energy, Climate and Environment Program, Pollution Management Research Group, International Institute for Applied Systems Analysis - IIASA, Laxenburg, Austria.ORCID iD: 0000-0002-6141-7796
Energy, Climate and Environment Program, Pollution Management Research Group, International Institute for Applied Systems Analysis - IIASA, Laxenburg, Austria.
Energy, Climate and Environment Program, Pollution Management Research Group, International Institute for Applied Systems Analysis - IIASA, Laxenburg, Austria.
2024 (English)In: Sustainable Production and Consumption, ISSN 2352-5509, Vol. 49, p. 462-473Article in journal (Refereed) Published
Abstract [en]

Phosphorus (P) is a finite, non-renewable resource that is a critical component of fertilizers; therefore, recovering P from municipal wastewater can provide an alternative sustainable source of this nutrient. This work analyses economic impacts and greenhouse gas emissions of P recovery in Swedish municipal wastewater treatment plants. The study examines different scenarios, including P recovery technologies in individual plants and hubs, and considers various P-rich streams (supernatant, sludge, and ash) in plants, different plant sizes, and multiple sludge management strategies such as land application, incineration, and hydrochar production, under current market conditions. The goal is to identify and offer solutions tailored to local conditions, addressing both technical opportunities and strategies to reduce costs.

The results show varying recovery rates: 5 % from supernatant, 36–65 % from sludge, and 17 % from sludge ash relative to total P in wastewater. Despite technical feasibility, P recovery costs are not covered at current market prices of P, indicating a lack of financial incentive, especially for smaller treatment plants. The least expensive recovery method costs about 7 k€/t P for ash, compared to 30–187 k€/t P for supernatant, however with the latter coming with the co-benefit of mitigated greenhouse gas emissions. The emissions from studied plants range from 84 to 123 kt CO2 eq (CO2 equivalent) for supernatant, 94–141 kt CO2 eq for sludge, and 75–102 kt CO2 eq for ash among different P recovery methods. Comparatively, P recovery methods from supernatant showed the lowest emissions, while the lower emissions range for ash is due to the consideration of fewer plants. Developing hub networks and converting sludge into products like hydrochar are crucial for attracting investments, enhancing P recovery, and leveraging economies of scale. Results highlight the urgency for localized strategies and proactive policy interventions to reconcile economic and environmental objectives in P recycling. Furthermore, P recovery from wastewater treatment plants, although more resource-intensive than mineral fertilizer, promotes circularity in the food chain and mitigates the risk of eutrophication.

Place, publisher, year, edition, pages
Elsevier, 2024. Vol. 49, p. 462-473
Keywords [en]
Hub strategy, Phosphorus recovery, Sewage sludge management, Techno-economic analysis
National Category
Energy Engineering Other Environmental Engineering Water Engineering
Research subject
Energy Engineering
Identifiers
URN: urn:nbn:se:ltu:diva-108429DOI: 10.1016/j.spc.2024.07.007ISI: 001275403000001Scopus ID: 2-s2.0-85199048739OAI: oai:DiVA.org:ltu-108429DiVA, id: diva2:1886483
Funder
Swedish Research Council FormasBio4Energy
Note

Validerad;2024;Nivå 2;2024-08-01 (signyg);

Fulltext license: CC BY

Available from: 2024-08-01 Created: 2024-08-01 Last updated: 2024-08-01Bibliographically approved

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Bagheri, Marzieh

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