TY - JOUR
T1 - High-grade bio-oil produced from coconut shell
T2 - A comparative study of microwave reactor and core-shell catalyst
AU - Wei, Xiaocui
AU - Xue, Xiangfei
AU - Wu, Liu
AU - Yu, Haozhe
AU - Liang, Jie
AU - Sun, Yifei
N1 - Publisher Copyright:
© 2020 Elsevier Ltd
PY - 2020/12/1
Y1 - 2020/12/1
N2 - The quality of bio-oil can be improved by conducting biomass pyrolysis either over a core-shell hierarchical zeolite catalyst or in a microwave reactor. However, there is a lack of comparative studies on the individual effects of each factor (e.g., catalysts, reactors) on bio-oil production. In this regard, the catalytic pyrolysis of coconut shell in a fixed-bed reactor and in a microwave reactor using the conventional ZSM-5 and core-shell hierarchical ZSM-5@SBA-15 catalysts was evaluated. With an emphasize on the production of hydrocarbons and phenols, the comparative effect of the core-shell catalyst and microwave reactor was demonstrated. The core-shell catalyst had the dual effect of regulating the bio-oil yield and composition. Compared to conventional ZSM-5 (25) with a SiO2/Al2O3 ratio of 25, the core-shell ZSM-5 (25)@SBA-15 not only increased the bio-oil yield by at least 40%, but also approximately doubled the production of hydrocarbons, irrespective of the reactor type. In contrast, the microwave reactor played a greater role in regulating the bio-oil composition. Irrespective of the catalyst used, the fixed-bed reactor tended to generate phenolic-rich bio-oil, while the microwave reactor sharply reduced the phenol selectivity by at least doubling that for aromatics.
AB - The quality of bio-oil can be improved by conducting biomass pyrolysis either over a core-shell hierarchical zeolite catalyst or in a microwave reactor. However, there is a lack of comparative studies on the individual effects of each factor (e.g., catalysts, reactors) on bio-oil production. In this regard, the catalytic pyrolysis of coconut shell in a fixed-bed reactor and in a microwave reactor using the conventional ZSM-5 and core-shell hierarchical ZSM-5@SBA-15 catalysts was evaluated. With an emphasize on the production of hydrocarbons and phenols, the comparative effect of the core-shell catalyst and microwave reactor was demonstrated. The core-shell catalyst had the dual effect of regulating the bio-oil yield and composition. Compared to conventional ZSM-5 (25) with a SiO2/Al2O3 ratio of 25, the core-shell ZSM-5 (25)@SBA-15 not only increased the bio-oil yield by at least 40%, but also approximately doubled the production of hydrocarbons, irrespective of the reactor type. In contrast, the microwave reactor played a greater role in regulating the bio-oil composition. Irrespective of the catalyst used, the fixed-bed reactor tended to generate phenolic-rich bio-oil, while the microwave reactor sharply reduced the phenol selectivity by at least doubling that for aromatics.
KW - Bio-oil
KW - Catalytic pyrolysis
KW - Coconut shell
KW - Microwave-assisted pyrolysis
KW - Zeolites
UR - https://www.scopus.com/pages/publications/85090195806
U2 - 10.1016/j.energy.2020.118692
DO - 10.1016/j.energy.2020.118692
M3 - 文章
AN - SCOPUS:85090195806
SN - 0360-5442
VL - 212
JO - Energy
JF - Energy
M1 - 118692
ER -