Abstract
In situ catalytic fast pyrolysis can be used to produce
partially upgraded bio-oils. This process, however,
suffers from rapid catalyst deactivation caused by coke
formation, which necessitates the use of continuous
catalyst regeneration. This can be achieved by using a
circulating fluidized-bed reactor. In such a reactor, one
key operational variable is the catalyst-to-biomass (C/B)
ratio, which influences the extent of the catalytic
reactions that take place. In this study, woody biomass
is pyrolyzed in a pilot-scale circulating fluidized-bed
reactor system using a HZSM-5 zeolite with varying C/B
ratios. The C/B ratio influences the overall product
distribution, the elemental distribution, and the
characteristics of the liquid products. An increase of
the C/B ratio enhances the conversion of pyrolysis vapors
but this does not result in a continuous improvement in
bio-oil quality. The C/B ratio is, nevertheless, a factor
that can be used to optimize the catalytic fast pyrolysis
process.
| Original language | English |
|---|---|
| Pages (from-to) | 94-103 |
| Journal | Energy Technology |
| Volume | 5 |
| Issue number | 1 |
| DOIs | |
| Publication status | Published - 2017 |
| MoE publication type | A1 Journal article-refereed |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
-
SDG 7 Affordable and Clean Energy
Keywords
- biofuels
- biomass
- bio-oil
- catalytic fast pyrolysis
- zeolites
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