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논문 기본 정보

자료유형
학술저널
저자정보
Hoang Vu Ly (Kyung Hee University) Jinsoo Kim (Kyung Hee University) Seung-Soo Kim (Kangwon National University) Hee Chul Woo (Pukyong National University) Suk Soon Choi (Semyung University)
저널정보
한국청정기술학회 청정기술 청정기술 제26권 제1호
발행연도
2020.3
수록면
79 - 87 (9page)

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초록· 키워드

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The bio-oil produced from the fast pyrolysis of lignocellulosic biomass contains a high amount of oxygenates, causing variation in the properties of bio-oil, such as instability, high acidity, and low heating value, reducing the quality of the bio-oil. Consequently, an upgrading process should be recommended ensuring that these bio-oils are widely used as fuel sources. Catalytic fast pyrolysis has attracted a great deal of attention as a promising method for producing upgraded bio-oil from biomass feedstock. In this study, the fast pyrolysis of tulip tree was performed in a bubbling fluidized-bed reactor under different reaction temperatures, with and without catalysts, to investigate the effects of pyrolysis temperature and catalysts on product yield and bio-oil quality. The system used silica sand, ferric oxides (Fe₂O₃ and Fe₃O₄), and H-ZSM-5 as the fluidized-bed material and nitrogen as the fluidizing medium. The liquid yield reached the highest value of 49.96 wt% at 450 ℃, using Fe₂O₃ catalyst, compared to 48.45 wt% for H-ZSM-5, 47.57 wt% for Fe₃O₄ and 49.03 wt% with sand. Catalysts rejected oxygen mostly as water and produced a lower amount of CO and CO₂, but a higher amount of H₂ and hydrocarbon gases. The catalytic fast pyrolysis showed a high ratio of H₂/CO than sand as a bed material.

목차

Abstract
1. Introduction
2. Experimental
3. Results and discussion
4. Conclusions
References

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UCI(KEPA) : I410-ECN-0101-2020-505-000534678