Abstract
Bio-based hydrocarbons derived from biomass pyrolysis is an important supplement to the fossil resources. The inhomogeneous temperature of catalytic bed is one of the important reasons for catalyst deactivation. Chem-CaO@SiC catalyst was synthesized for the conversion of waste cooking oil (WCO) to bio-based hydrocarbons in this paper. Compared with the catalyst prepared from physical mixing, the catalyst prepared by chemical reaction was performed better in maintaining the bio-oil yield and increasing the relative content of hydrocarbons in bio-oil. Catalyst characterization showed that CaO was well supported on the SiC-powder surface. Then the effects of SiC-ball bed temperature and CaO loading rate on product yield and distribution were investigated. Also, the deoxygenation pathway was discussed. More polycyclic aromatics were produced when the SiC-ball bed temperature was 550 °C and above. And the composite catalyst could inhibit the formation of PAHs. The bio-oil yield increased and high heating value of gas products decreased with the decrease SiC-to-CaO ratio, and more energy from the WCO flowed into bio-oil. The catalyst remained 0.622 times of the initial activity after 5 cycles.
Original language | English (US) |
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Article number | 125683 |
Journal | Energy |
Volume | 263 |
DOIs | |
State | Published - Jan 15 2023 |
Bibliographical note
Funding Information:This project was financially supported by the National Natural Science Foundation of China (No. 52166015 ), The Jiangxi Provincial Natural Science Foundation ( 20212ACB215007 ), The Major Discipline Academic and Technical Leaders Training Program of Jiangxi Province ( 20204BCJ23011 ), The Centrally Guided Local Science Technology Special Project ( 20202ZDB01012 ).
Publisher Copyright:
© 2022 Elsevier Ltd
Keywords
- CaO
- Composite catalyst
- Hydrocarbon
- Pyrolysis
- Renewable energy
- Waste cooking oil