4.7 Article

Valorization of swine manure for a circular approach through hydrothermal carbonization

Journal

BIOMASS & BIOENERGY
Volume 168, Issue -, Pages -

Publisher

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.biombioe.2022.106689

Keywords

Swine manure; Hydrothermal carbonization; Hydrochar; Biogas production; Energy balance

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In recent years, concentrated swine farms have caused environmental and economic problems for manure management. This study evaluates the use of hydrothermal carbonization to treat swine manure and utilize the liquid streams for fertigation and the hydrochar for biogas production. The results show that HTC greatly improves the dewaterability of swine manure and allows for the recovery of nutrients for fertigation. The proposed scheme of on-site HTC and off-site AD is energy efficient and has the potential to cover a significant portion of the required energy for the processes.
In recent years, swine farming has changed from small to concentrated farms, posing environmental and eco-nomic problems for manure management and disposal. Considering this background, this work evaluates innovative scenarios where swine manure (SM) is treated through hydrothermal carbonization (HTC) in view of utilizing the liquid streams for on-site fertigation and the hydrochar for off-site biogas production through anaerobic digestion (AD). The scheme proposed (on-site HTC and off-site AD) allows to avoid nitrogen and phosphorus leaching risks associated with the direct use on land of the raw manure, and in addition allows for energy recovery through biogas production. HTC was performed at 190 degrees C for 1 h at three different SM dry matter concentrations, expressed as total solids (TS). After HTC, the dewaterability of SM strongly improved, above all for thickened SM samples (10% and 15% TS). The soluble chemical oxygen demand greatly increased confirming the hydrolysis speed up of the HTC. Phosphorus contained in the SM accumulated in the hydrochar while total Kjeldahl nitrogen decreased in HTC liquor, resulting suited for fertigation. AD tests revealed a sig-nificant biogas potential of the hydrochar. The scenario with 15% TS SM fed to the HTC system resulted the most energy efficient, when considering both the energy input to the HTC process and the energy output from AD; in the case when HTC and AD were both carried out on-site, the proposed scheme would allow covering 42% of the energy required for the coupled processes.

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