Mechanistic Investigation into Bed Agglomeration during Biomass Fast Pyrolysis in a Fluidized-Bed Reactor
This paper demonstrates that during the pyrolysis of mallee leaf (355-500 µm) in a fluidized-bed reactor (bed materials: silica sand, 125-355 µm) at 300-700 °C, bed agglomeration takes place due to the formation of char-char and/or char-sand agglomerates connected by carbon-enriched necks. There are...
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| Format: | Journal Article |
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American Chemical Society
2012
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| Online Access: | http://hdl.handle.net/20.500.11937/42541 |
| _version_ | 1848756448076496896 |
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| author | Burton, A. Wu, Hongwei |
| author2 | Andrzej Szlek |
| author_facet | Andrzej Szlek Burton, A. Wu, Hongwei |
| author_sort | Burton, A. |
| building | Curtin Institutional Repository |
| collection | Online Access |
| description | This paper demonstrates that during the pyrolysis of mallee leaf (355-500 µm) in a fluidized-bed reactor (bed materials: silica sand, 125-355 µm) at 300-700 °C, bed agglomeration takes place due to the formation of char-char and/or char-sand agglomerates connected by carbon-enriched necks. There are two types of bed agglomeration: one formed due to solvent-soluble organic matter which dissembles upon solvent washing and the other due to solvent-insoluble organic matter produced from biomass pyrolysis. The yield of each type of bed agglomeration is broadly proportional to the yield of thecorresponding type of organic matter in the bed samples. The total yield of bed agglomeration decreases with increasing pyrolysis temperature, from 16.5% at 300 °C to 9.5% at 500 °C and 1.8% at 700 °C. The distribution of the two types of bed agglomeration is also strongly temperature dependent. At low temperatures (e.g., 300 °C), bed agglomeration is dominantly contributed by those formed by solvent-insoluble organic matter. As pyrolysis temperature increases, bed agglomeration due tosolvent-soluble organic matter becomes increasingly important and reaches a maximum at 500 °C. At pyrolysis temperatures above 600 °C, there is a drastic reduction in the bed agglomeration formed by solvent-soluble organic matter due to thermal cracking so that bed agglomeration is again dominantly formed by solvent-insoluble organic matter. Overall, bed agglomeration during biomass pyrolysis in a fluidized-bed reactor is due to the production of sticky agents, including both partially molten pyrolyzing biomass particles and the organic matter (both solvent- soluble and -insoluble) produced from biomass pyrolysis reactions. |
| first_indexed | 2025-11-14T09:12:21Z |
| format | Journal Article |
| id | curtin-20.500.11937-42541 |
| institution | Curtin University Malaysia |
| institution_category | Local University |
| last_indexed | 2025-11-14T09:12:21Z |
| publishDate | 2012 |
| publisher | American Chemical Society |
| recordtype | eprints |
| repository_type | Digital Repository |
| spelling | curtin-20.500.11937-425412017-09-13T14:26:49Z Mechanistic Investigation into Bed Agglomeration during Biomass Fast Pyrolysis in a Fluidized-Bed Reactor Burton, A. Wu, Hongwei Andrzej Szlek This paper demonstrates that during the pyrolysis of mallee leaf (355-500 µm) in a fluidized-bed reactor (bed materials: silica sand, 125-355 µm) at 300-700 °C, bed agglomeration takes place due to the formation of char-char and/or char-sand agglomerates connected by carbon-enriched necks. There are two types of bed agglomeration: one formed due to solvent-soluble organic matter which dissembles upon solvent washing and the other due to solvent-insoluble organic matter produced from biomass pyrolysis. The yield of each type of bed agglomeration is broadly proportional to the yield of thecorresponding type of organic matter in the bed samples. The total yield of bed agglomeration decreases with increasing pyrolysis temperature, from 16.5% at 300 °C to 9.5% at 500 °C and 1.8% at 700 °C. The distribution of the two types of bed agglomeration is also strongly temperature dependent. At low temperatures (e.g., 300 °C), bed agglomeration is dominantly contributed by those formed by solvent-insoluble organic matter. As pyrolysis temperature increases, bed agglomeration due tosolvent-soluble organic matter becomes increasingly important and reaches a maximum at 500 °C. At pyrolysis temperatures above 600 °C, there is a drastic reduction in the bed agglomeration formed by solvent-soluble organic matter due to thermal cracking so that bed agglomeration is again dominantly formed by solvent-insoluble organic matter. Overall, bed agglomeration during biomass pyrolysis in a fluidized-bed reactor is due to the production of sticky agents, including both partially molten pyrolyzing biomass particles and the organic matter (both solvent- soluble and -insoluble) produced from biomass pyrolysis reactions. 2012 Journal Article http://hdl.handle.net/20.500.11937/42541 10.1021/ef300406k American Chemical Society restricted |
| spellingShingle | Burton, A. Wu, Hongwei Mechanistic Investigation into Bed Agglomeration during Biomass Fast Pyrolysis in a Fluidized-Bed Reactor |
| title | Mechanistic Investigation into Bed Agglomeration during Biomass Fast Pyrolysis in a Fluidized-Bed Reactor |
| title_full | Mechanistic Investigation into Bed Agglomeration during Biomass Fast Pyrolysis in a Fluidized-Bed Reactor |
| title_fullStr | Mechanistic Investigation into Bed Agglomeration during Biomass Fast Pyrolysis in a Fluidized-Bed Reactor |
| title_full_unstemmed | Mechanistic Investigation into Bed Agglomeration during Biomass Fast Pyrolysis in a Fluidized-Bed Reactor |
| title_short | Mechanistic Investigation into Bed Agglomeration during Biomass Fast Pyrolysis in a Fluidized-Bed Reactor |
| title_sort | mechanistic investigation into bed agglomeration during biomass fast pyrolysis in a fluidized-bed reactor |
| url | http://hdl.handle.net/20.500.11937/42541 |