Biochar-integrated reactive filtration of wastewater for P removal and recovery, micropollutant catalytic oxidation, and negative CO 2 e: Life cycle assessment and techno-economic analysis

Life cycle assessment (LCA) and techno-economic analysis (TEA) models are developed for a tertiary wastewater treatment system that employs a biochar-integrated reactive filtration (RF) approach. This innovative system incorporates the utilization of biochar (BC) either in conjunction with or indepe...

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Veröffentlicht in:Water environment research 2023-12, Vol.95 (12), p.e10962
Hauptverfasser: Taslakyan, Lusine, Baker, Martin C, Strawn, Daniel G, Möller, Gregory
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Sprache:eng
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Zusammenfassung:Life cycle assessment (LCA) and techno-economic analysis (TEA) models are developed for a tertiary wastewater treatment system that employs a biochar-integrated reactive filtration (RF) approach. This innovative system incorporates the utilization of biochar (BC) either in conjunction with or independently of iron-ozone catalytic oxidation (CatOx)-resulting in two configurations: Fe-CatOx-BC-RF and BC-RF. The technology demonstrates 90%-99% total phosphorus removals, adsorption of phosphorus to biochar for recovery, and >90% destructive removal of observed micropollutants. In this work, we conduct an ISO-compliant LCA of a 49.2 m /day (9 gpm) field pilot-scale Fe-CatOx-BC-RF system and a 1130 m /day (0.3 MGD) water resource recovery facility (WRRF)-installed RF system, modeled with BC addition at the same rate of 0.45 g/L to quantify their environmental impacts. LCA results indicated that the Fe-CatOx-BC-RF pilot system is a BC dose-dependent carbon-negative technology at -1.21 kg CO e/m , where biochar addition constitutes a -1.53 kg/m CO e beneficial impact to the process. For the WRRF-installed RF system, modeled with the same rate of BC addition, the overall process changed from 0.02 kg CO e/m to a carbon negative -1.41 kg CO e/m , demonstrating potential as a biochar dose-dependent negative emissions technology. Using the C 100-year carbon accounting approach rather than C reduces these CO e metrics for the process by about 25%. A stochastic TEA for the cost of water treatment using this combinatorial P removal/recovery, micropollutant destructive removal, and disinfection advanced technology shows that at scale, the mean cost for treating 1130 m /day (0.3 MGD) WRRF secondary influent water with Fe-CatOx-BC-RF using the C metric is US$0.18 ± US$0.01/m to achieve overall process carbon neutrality. Using the same BC dose in an estimation of a 3780 m /day (1 MGD) Fe-CatOx-BC-RF facility, the carbon neutral cost of treatment is reduced further to US$0.08 ± $0.01 with added BC accounting for US$0.03/m . Overall, the results demonstrate the potential of carbon negativity to become a water treatment performance standard as important and attainable as pollutant and pathogen removal. PRACTITIONER POINTS: Life cycle assessment (LCA) of a pilot scale tertiary biochar water treatment process with or without catalytic ozonation at a WRRF shows a carbon negative global warming potential of -1.21-kg CO2e/m3 while removing 90%-99% TP and >90% of detected micropolluta
ISSN:1061-4303
1554-7531
DOI:10.1002/wer.10962