4.5 Article

Valorisation of lignocellulosic biomass investigating different pyrolysis temperatures

Journal

JOURNAL OF THE ENERGY INSTITUTE
Volume 93, Issue 5, Pages 1960-1969

Publisher

ELSEVIER SCI LTD
DOI: 10.1016/j.joei.2020.04.011

Keywords

Thermo-catalytic reforming; Pyrolysis; Biofuel; Sugarcane bagasse; Oat hulls

Categories

Funding

  1. EPSRC [EP/N021746/1]
  2. EPSRC [EP/N021746/1] Funding Source: UKRI

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Presently, sugarcane bagasse (SB) and oat hulls (OH) have a distinctive potential as a renewable source of biomass, due to its global availability, which is advantageous for producing liquid and gaseous fuels by thermochemical processes. Thermo-Catalytic Reforming (TCR) is a pyrolysis based technology for generating energy vectors (char, bio-oil and syngas) from biomass wastes. This work aims to study the conversion of SB and OH into fuels, using TCR in a 2 kg/h continuous pilot-scale reactor at different pyrolysis temperatures. The pyrolysis temperatures were studied at 400, 450 and 500 degrees C, while the subsequent reforming temperature remained constant at 500 degrees C. The bio-oil contained the highest calorific value of 33.4 and 33.5 MJ/kg for SB and OH, respectively at 500 degrees C pyrolysis temperature, which represented a notable increase compared to the raw material calorific value of SB and OH (16.4 and 16.0 MJ/kg, respectively), this was the result of deoxygenation reactions occurring. Furthermore, the increment of the pyrolysis temperature improved the water content, total acid number (TAN), viscosity and density of the bio-oil. The syngas and the biochar properties did not change significantly with the increase of the pyrolysis temperature. In order to use TCR bio-oil as an engine fuel, it is necessary to carry out some upgrading treatments; or blend it with fossil fuels if it is to be used as a transportation fuel. Overall, TCR is a promising future route for the valorisation of lignocellulosic residues to produce energy vectors. (C) 2020 Energy Institute. Published by Elsevier Ltd. All rights reserved.

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