Coupling hydrothermal carbonization and anaerobic digestion for sewage digestate management: Influence of hydrothermal treatment time on dewaterability and bio-methane production. (1st March 2021)

• Record Type: Journal Article
• Authors: Ahmed, Mostafa; Andreottola, Gianni; Elagroudy, Sherien; Negm, Mohamed Shaaban; Fiori, Luca
• Is Part Of: Journal of environmental management. Volume 281(2021)
• Publication Date: 2021-03-01
• Subjects: Hydrothermal carbonization -- Sewage digestate -- Sludge dewaterability -- Biochemical methane potential -- Sludge management; Environmental policy -- Periodicals; Environmental management -- Periodicals; Environment -- Periodicals; Ecology -- Periodicals; 363.705
• DOI: 10.1016/j.jenvman.2020.111910
• Languages: English
• ISSNs: 0301-4797

Abstract

Abstract: Hydrothermal carbonization (HTC) technology is addressed in the framework of sewage digestate management. HTC converts digestate into a stabilized and sterilized solid (the hydrochar) and a liquor (HTCL) rich in organic carbon. This study aims to optimize the HTC operating parameters, namely the treatment time, in terms of hydrochar production, HTC slurry dewaterability, HTCL bio-methane yields in anaerobic digestion (AD), and process energy consumption. Digestate slurry was processed through HTC at different treatment times (0.5, 1, 2 and 3 h) at 190 °C, and the dewaterability of the treated slurries was addressed through capillary suction time and centrifuge lab-testing. In addition, biochemical methane potential (BMP) tests were conducted for HTCL under mesophilic conditions. Results show that by increasing the HTC treatment time the dewaterability was further improved, ammonium concentration in HTCL increased, and methane potential of HTCL decreased. 0.5 h HTCL had the highest bio-methane potential of 142 ± 3 mL CH4 /g COD yet the treatment time was not sufficient for improving the slurry's dewaterability. HTC treatment time of 1 h at 190 °C was identified as the optimum trade-off for improved dewaterability and utilisation of HTCL for biogas production. 1 h HTCL bio-methane potential can cover around 25% of the HTC and AD thermal and electrical energy needs without considering the eventual use of the hydrochar as a biofuel. Graphical abstract: Image 1 Highlights: Sewage digestate to HTC (190 °C; 0.5, 1, 2, 3 h) and HTC liquor (HTCL) to AD. From 0.5 to 1 h HTC duration: hydrochar dewaterability increased by a factor of 7. CH4 production by HTCLs AD: 142 and 84 mL/gCOD for 0.5 and 3 h HTC respectively. Trade-off for dewaterability and biogas production: 1 h HTC duration. HTCL methane potential can cover around 25% of HTC and AD energy needs.