TY - JOUR
T1 - Modeling and simulation of a continuous biomass hydrothermal carbonization process
AU - Gómez, Jaime
AU - Corsi, Giancarlo
AU - Pino-Cortés, Ernesto
AU - Díaz-Robles, Luis A.
AU - Campos, Valeria
AU - Cubillos, Francisco
AU - Pelz, Stefan K.
AU - Paczkowski, Sebastian
AU - Carrasco, Samuel
AU - Silva, Javier
AU - Lapuerta, Magín
AU - Pazo, Amparo
AU - Monedero, Esperanza
N1 - Publisher Copyright:
© 2019, © 2019 Taylor & Francis Group, LLC.
PY - 2020/6/2
Y1 - 2020/6/2
N2 - This work evaluates a continuous biomass hydrothermal carbonization process through modeling and steady state simulation using the UniSim Design process simulator. The reactive process was divided into four stages: biomass hydrolysis, intermediate compounds degradation, aromatics formation, and polymerization process, which make it possible to obtain the solid product or hydrochar. Pure biomass types and their mixtures were compared, considering hydrochar and carbon yields, H/C, and O/C ratios, and their deviation from the batch process. The results of hydrochar yield indicated that biomass with high cellulose content can perform satisfactorily in the proposed model. In addition, the possibility of carrying out the process in reactive stages together with the recirculation of liquid product, allowed a greater yield with respect to the batch process. It is concluded that the proposed model improves the characteristics of the obtained hydrochar compared to its crude biomass, achieving lower proportions of hydrogen and oxygen in the solid product.
AB - This work evaluates a continuous biomass hydrothermal carbonization process through modeling and steady state simulation using the UniSim Design process simulator. The reactive process was divided into four stages: biomass hydrolysis, intermediate compounds degradation, aromatics formation, and polymerization process, which make it possible to obtain the solid product or hydrochar. Pure biomass types and their mixtures were compared, considering hydrochar and carbon yields, H/C, and O/C ratios, and their deviation from the batch process. The results of hydrochar yield indicated that biomass with high cellulose content can perform satisfactorily in the proposed model. In addition, the possibility of carrying out the process in reactive stages together with the recirculation of liquid product, allowed a greater yield with respect to the batch process. It is concluded that the proposed model improves the characteristics of the obtained hydrochar compared to its crude biomass, achieving lower proportions of hydrogen and oxygen in the solid product.
KW - Biomass
KW - Computer simulation
KW - Hydrochar
KW - Hydrothermal carbonization
UR - http://www.scopus.com/inward/record.url?scp=85066613521&partnerID=8YFLogxK
U2 - 10.1080/00986445.2019.1621858
DO - 10.1080/00986445.2019.1621858
M3 - Article
AN - SCOPUS:85066613521
SN - 0098-6445
VL - 207
SP - 751
EP - 768
JO - Chemical Engineering Communications
JF - Chemical Engineering Communications
IS - 6
ER -