TY - JOUR
T1 - Characterization of hydrochar and process water from the hydrothermal carbonization of Refuse Derived Fuel
AU - Nobre, Catarina
AU - Alves, Octávio
AU - Durão, Luís
AU - Şen, Ali
AU - Vilarinho, Cândida
AU - Gonçalves, Margarida
N1 - This work was supported by the CITRI, S.A. project I&DT no 24878. And by FCT - Fundacao para a Ciencia e Tecnologia, through grant SFRH/BD/111956/2015 and within the R&D Units Project Scope UIDP/04077/2020.
PY - 2021/2/1
Y1 - 2021/2/1
N2 - In this study, hydrothermal carbonization (HTC) was used as a thermochemical conversion process to upgrade Refuse Derived Fuel (RDF). The effect of process temperature (250 °C, 275 °C and 300 °C), residence time (30 min and 120 min), and RDF-to-water ratio (1:15 and 1:5) on the main characteristics of the produced hydrochars and process waters was assessed. The HTC process yielded hydrochars with enhanced fuel properties when compared to the original feedstock, namely higher carbon content and heating value. The hydrochars also presented reduced oxygen and ash contents. The hydrochar produced at 300 °C for 120 min presented the lowest ash content (3.3 wt%, db) whereas the highest heating value was found for the hydrochar obtained at 275 °C for 120 min (28.1 MJ/kg, db). The HTC process was also responsible for a significant reduction in chlorine concentration, showing dechlorination efficiencies between 69.2 and 77.9%. However, the HTC process generated acidic process waters with high COD values (maximum 27.2 gO2/L), which need to be further managed or valorized. Energy calculations were also performed, revealing that lower water amounts, lower temperatures, and longer residence times, represent optimal conditions for higher hydrochar yields and consequently good process efficiencies.
AB - In this study, hydrothermal carbonization (HTC) was used as a thermochemical conversion process to upgrade Refuse Derived Fuel (RDF). The effect of process temperature (250 °C, 275 °C and 300 °C), residence time (30 min and 120 min), and RDF-to-water ratio (1:15 and 1:5) on the main characteristics of the produced hydrochars and process waters was assessed. The HTC process yielded hydrochars with enhanced fuel properties when compared to the original feedstock, namely higher carbon content and heating value. The hydrochars also presented reduced oxygen and ash contents. The hydrochar produced at 300 °C for 120 min presented the lowest ash content (3.3 wt%, db) whereas the highest heating value was found for the hydrochar obtained at 275 °C for 120 min (28.1 MJ/kg, db). The HTC process was also responsible for a significant reduction in chlorine concentration, showing dechlorination efficiencies between 69.2 and 77.9%. However, the HTC process generated acidic process waters with high COD values (maximum 27.2 gO2/L), which need to be further managed or valorized. Energy calculations were also performed, revealing that lower water amounts, lower temperatures, and longer residence times, represent optimal conditions for higher hydrochar yields and consequently good process efficiencies.
KW - Alternative solid fuel
KW - Hydrochar
KW - Hydrothermal carbonization
KW - Process water
KW - Refuse Derived Fuel
UR - http://www.scopus.com/inward/record.url?scp=85097719554&partnerID=8YFLogxK
U2 - 10.1016/j.wasman.2020.11.040
DO - 10.1016/j.wasman.2020.11.040
M3 - Article
C2 - 33333468
AN - SCOPUS:85097719554
SN - 0956-053X
VL - 120
SP - 303
EP - 313
JO - Waste Management
JF - Waste Management
ER -