Abstract
This paper summarises the long development work done at
VTT for gas clean-up for various synthesis applications.
The development work has covered the most challenging and
costly steps in biomass gasification based processes:
high-temperature gas filtration and reforming of
hydrocarbon gases and tars. The tar content of product
gas is one of the main factors defining the temperature
window in which the hot-gas filter can be operated, which
in the case of fluidized-bed gasification is at 350-500
°C. Research is ongoing to achieve higher and thus more
economical operation temperatures. Optimal operation of a
catalytic reformer can be achieved by using a staged
reformer where zirconia-based catalysts are used as a
pre-reformer layer before nickel and/or precious
metal-based catalyst stages. The temperature of the
reformer is optimally increased in subsequent stages from
600 up to 1,000 °C. According to the techno-economic
analysis, increasing the hot-gas filtration temperature
by 300 °C or methane conversion in the reformer from 55
to 95 % both lead to about 5 % reduction the liquid fuel
production cost
Original language | English |
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Pages (from-to) | 357-370 |
Journal | Biomass Conversion and Biorefinery |
Volume | 4 |
Issue number | 4 |
DOIs | |
Publication status | Published - 2014 |
MoE publication type | A1 Journal article-refereed |
Keywords
- Biomass
- gasification
- hot gas filtration
- tar reforming
- gas clean-up
- techno-economic evaluation