Citation:
Briongos, J. V., Taramona, S., Gómez-Hernández, J., Mulone, V., & Santana, D. (2021). Solar and biomass hybridization through hydrothermal carbonization. In Renewable Energy, 177, pp. 268-279
xmlui.dri2xhtml.METS-1.0.item-contributor-funder:
Comunidad de Madrid
Sponsor:
The authors wish to thank “Comunidad de Madrid” for its support to the ACES2030-CM Project (S2018/EMT-4319) through the Program of R&D activities between research groups in Technologies 2018, co-financed by European Structural Funds. Also, the authors wish to thank the research project INTECSOLARIS-CM-UC3M, funded by the call “Programa de apoyo a la realización de proyectos interdisciplinares de I + D para jóvenes investigadores de la Universidad Carlos III de Madrid 2019–2020” under the frame of the “Convenio Plurianual Comunidad de Madrid - Universidad Carlos III de Madrid”.
Project:
Comunidad de Madrid. S2018/EMT-4319 AT-2021
Keywords:
Continuous hydrothermal carbonization
,
Concentrated solar energy
,
Beam-down solar field
,
Twin-screw extruders
,
Organic wastes
Hydrothermal carbonization process can transform wet bio-wastes into value-added products. This work aims to hybridize a concentrating solar technology and a biomass reactor for the continuous and sustainable valorization of biomass. The novel technology propoHydrothermal carbonization process can transform wet bio-wastes into value-added products. This work aims to hybridize a concentrating solar technology and a biomass reactor for the continuous and sustainable valorization of biomass. The novel technology proposed integrates a linear beam-down solar field with a twin-screw reactor for continuous HTC process. The solar field consists of two reflections that concentrate linearly the sun energy on the ground, where the twin-screw reactor is placed. A mathematical model is proposed to solve both the heat transfer and HTC kinetics for a co-rotating twin-screw reactor. The incoming heat flux from the solar field (8-20 kW/m2), the reactor length (L/D = 30-60 where D is the diameter) and the rotating velocity of the screw (25-100 rpm) are the main variables used to process the biomass up to the desired severity factor. The simulation results of different lignocellulosic biomasses (loblolly pine, sugarcane bagasse, corn stover and rice husk) are validated against literature data. The developed model shows good agreement with experimental results shown in the literature. The proposed technology foresees hydrochar yields of 64-78% for severity factors of 4.2 and 5.3, respectively, in agreement to the experimental results of 63-70% shown in literature.[+][-]