Abstract
A series of experiments was conducted to study the effect of temperature and feed rate on physicochemical properties and yield of bio-oil. The experiments were performed in a helical screw fluidized bed reactor and about 150-gram palm shell (PS) was pyrolyzed in each run at 275 °C/min heating rate. The first set of experiments was conducted at temperature ranging from 400 to 650 °C without using any inert gas for fluidization. While the second set of experiments were performed at feed rates ranging from 3 to 25 g/min in order to investigate the effects of feed rate on pyrolytic products. Results showed that the bio-oil yield was increased with the increase in temperature and feed rate due to the enhanced biomass volatilization. In a similar vein to this, a greater extent in oxygenates cracking was also noted in the bio-oil. A maximum liquid yield of about 72.84 wt% was obtained at 500 °C, while 72.92 wt% liquid yield was obtained with 25 g/min feed rate. The HHV of bio-oil was also increased from 38.52 to 43.13 MJ/kg when pyrolysis temperature was increased from 400 to 650 °C.
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Acknowledgements
The authors thank GSP-MOHE, University of Malaya for funding this study through the project number MO008-2015. This work is also supported by Xiamen University Malaysia Research Fund (Grant No: XMUMRF/2021-C7/IENG/0032).
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Qureshi, K.M., Lup, A.N.K., Khan, S. et al. Effect of temperature and feed rate on pyrolysis oil produced via helical screw fluidized bed reactor. Korean J. Chem. Eng. 38, 1797–1809 (2021). https://doi.org/10.1007/s11814-021-0842-0
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DOI: https://doi.org/10.1007/s11814-021-0842-0