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Waste and Biomass Valorization

, Volume 10, Issue 1, pp 187–195 | Cite as

Bio-Oil Production in Fluidized Bed Reactor at Pilot Plant from Sugarcane Bagasse by Catalytic Fast Pyrolysis

  • Jessi Osorio
  • Farid ChejneEmail author
Original Paper
  • 182 Downloads

Abstract

Fast pyrolysis of biomass produces a liquid with a diverse spectrum of compounds. This work describes impact of adding calcium oxide as a catalyst for fast catalytic pyrolysis of sugarcane bagasse in a fluidized bed reactor at pilot plant scale. The product distributions, bio-oil physical characteristics, and elemental analysis of products were determined. Rapid aging tests were performed on the oils at 80 °C to evaluate the impact of the catalyst on long term storage properties. Results showed that the presence of the catalyst (10 wt% loading) reduced the bio-oil oxygen content by 14%. The catalyst decreased the total bio-oil yield by 17 wt%, but reduced the water content in that oil and increased the gas yield. The presence of the catalyst did not affect the char yield. Over 150 compounds were identified by GC/MS and the distribution of the main functional groups was analyzed.

Keywords

Catalytic fast pyrolysis Biomass Bio-oil aging Lime 

Notes

Acknowledgements

The authors are grateful to National University of Colombia (DIME) and Colciencias for providing financial and logistical support to do this research. Special thanks to Brennan Pecha for invaluable comments to this paper.

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Copyright information

© Springer Science+Business Media B.V. 2017

Authors and Affiliations

  1. 1.Termodinámica aplicada y energías alternativas, Facultad de MinasUniversidad Nacional de Colombiasede MedellínColombia
  2. 2.Escuela de Procesos y EnergíaUniversidad Nacional de Colombiasede MedellínColombia

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