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Design and Fabrication of Fluidized Bed Pyrolysis System

Nur A. Fadhilah, Muhammad N. Islam, and Roslynna Rosli
Universiti Teknologi Brunei, Bandar Seri Begawan, Brunei Darussalam

Abstract— A fluidized bed pyrolysis system has been designed and fabricated for practical demonstration of the fluidization of biomass solid waste particles at optimal performance for bio-fuel production. The bed of this reactor was sand particles of average size 300μm and a density of 1.46g/cm3. Nitrogen gas was used as fluidizing fluid to maintain an inert atmosphere in the reactor. The major components of the system are: fluidized bed reactor, heating cylinder, cyclone, condenser and liquid collector. All the components have been successfully assembled for future experimental use. The height of the sand bed was 6.24 cm on a distributor with a mesh of 125 μm. According to hydrodynamic test, the minimum flow rate for the fluidization of the sand particles was 15 l/min; whereas, it was close to the theoretical value of 15.7 l/min when the optimum fluidization was expected. 

Index Terms—fluidized bed reactor, fast pyrolysis, biomass solid waste, bio-oil

Cite: Nur A. Fadhilah, Muhammad N. Islam, and Roslynna Rosli, "Design and Fabrication of Fluidized Bed Pyrolysis System," International Journal of Mechanical Engineering and Robotics Research, Vol. 9, No. 6, pp. 847-851, June 2020. DOI: 10.18178/ijmerr.9.6.847-851

Copyright © 2020 by the authors. This is an open access article distributed under the Creative Commons Attribution License (CC BY-NC-ND 4.0), which permits use, distribution and reproduction in any medium, provided that the article is properly cited, the use is non-commercial and no modifications or adaptations are made.