4.4 Article

Environmental Life Cycle Assessment of Hydrothermal Carbonization of Sewage Sludge and Its Products Valorization Pathways

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WASTE AND BIOMASS VALORIZATION
卷 13, 期 9, 页码 3845-3864

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SPRINGER
DOI: 10.1007/s12649-022-01821-x

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Sewage sludge; Hydrothermal carbonization; Life cycle assessment; Anaerobic digestion; Phosphorus recovery

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This study compares the environmental performances of a Water Resources Recovery Facility (WRRF) and a hydrothermal carbonization (HTC) plant for sewage sludge treatment. Results show that the HTC-based scenarios exhibit improved performances, with a reduction of 98% in the Climate Change indicator. Anaerobic digestion further reduces impacts, while phosphorus recovery negatively affects most indicators.
This study is aimed at evaluating through Life Cycle Assessment (LCA) the environmental performances of an integrated system of an existing Water Resources Recovery Facility (WRRF) and a hypothetical hydrothermal carbonization (HTC) plant applied to the generated sewage sludge (SS). Beside the valorisation of the solid product (hydrochar, HC) as a fuel substituting lignite, the possibility to valorize also the liquid fraction (process water, PW) derived by the HTC, by anaerobic digestion to produce biogas, is here proposed and analysed. Additionally, phosphorus recovery from HC, prior its use, by acid leaching with nitric acid is also suggested and evaluated. Thus, four integrated scenarios, based on SS carbonization, are proposed and compared with the current SS treatment, based on composting outside of the WRRF (Benchmark scenario). The proposed scenarios, based on HTC, show improved performances with respect to the benchmark one, for thirteen of sixteen considered impact indicators. For the Climate Change (CC) indicator, the two HTC scenarios are able to reduce the impacts up to - 98%, with respect to the Benchmark. Further, the introduction of anaerobic digestion of PW proves to reduce impacts more than other configurations in eleven on sixteen impact categories. On the contrary, the introduction of phosphorus recovery process negatively affects the values for most of indicators. Thus, possible solutions to improve the integration of this process are outlined (e.g., the use of sulfuric acid instead of nitric one, or the application of a different ratio between solid and acidified solution during acid leaching of HC to recover phosphorus). [GRAPHICS] .

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