Gasification conversion and char reactivity of rubber seed shell and high density polyethylene mixtures using steam Co-Gasification process
Due to the recent surge of global energy demand and the fear of climate change, an extensive attention from worldwide in seeking for cleaner alternative means of renewable energy and this has been a topic of interest widely. With the abundance supply of biomass and plastic waste generated annually a...
| Main Authors: | , , , , , |
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| Format: | Journal Article |
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The Italian Association of Chemical Engineering
2014
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| Online Access: | http://hdl.handle.net/20.500.11937/69802 |
| _version_ | 1848762138308378624 |
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| author | Chin, Bridgid Yusup, S. Al Shoaibi, A. Kannan, P. Srinivasakannan, C. Sulaiman, S. |
| author_facet | Chin, Bridgid Yusup, S. Al Shoaibi, A. Kannan, P. Srinivasakannan, C. Sulaiman, S. |
| author_sort | Chin, Bridgid |
| building | Curtin Institutional Repository |
| collection | Online Access |
| description | Due to the recent surge of global energy demand and the fear of climate change, an extensive attention from worldwide in seeking for cleaner alternative means of renewable energy and this has been a topic of interest widely. With the abundance supply of biomass and plastic waste generated annually and finding an effective method in utilizing these wastes, leads to a notion of using these wastes in the co-gasification process. Although there are studies on co-gasification of biomass and waste mixtures, limited studies focused on the understanding of the char reactivity and gasification conversion of this mixture. Hence, an experimental study on steam co-gasification of rubber seed shell and high density polyethylene mixtures in argon atmosphere is carried out using thermogravimetric (TGA) approach under non-isothermal condition. This work presents the surface physical morphology of rubber seed shell (RSS), high density polyethylene (HDPE), and its mixtures. Furthermore, the char conversion and char reactivity of RSS, HDPE, and their mixtures at different proportions are investigated in both pyrolysis and gasification process. The argon gas is supplied at a flowrate of 100 mL min-1and the steam is generated from superheater at 383 K whilst injected at flowrate of 3000 µL h-1into the TGA system. |
| first_indexed | 2025-11-14T10:42:48Z |
| format | Journal Article |
| id | curtin-20.500.11937-69802 |
| institution | Curtin University Malaysia |
| institution_category | Local University |
| last_indexed | 2025-11-14T10:42:48Z |
| publishDate | 2014 |
| publisher | The Italian Association of Chemical Engineering |
| recordtype | eprints |
| repository_type | Digital Repository |
| spelling | curtin-20.500.11937-698022018-09-19T06:11:50Z Gasification conversion and char reactivity of rubber seed shell and high density polyethylene mixtures using steam Co-Gasification process Chin, Bridgid Yusup, S. Al Shoaibi, A. Kannan, P. Srinivasakannan, C. Sulaiman, S. Due to the recent surge of global energy demand and the fear of climate change, an extensive attention from worldwide in seeking for cleaner alternative means of renewable energy and this has been a topic of interest widely. With the abundance supply of biomass and plastic waste generated annually and finding an effective method in utilizing these wastes, leads to a notion of using these wastes in the co-gasification process. Although there are studies on co-gasification of biomass and waste mixtures, limited studies focused on the understanding of the char reactivity and gasification conversion of this mixture. Hence, an experimental study on steam co-gasification of rubber seed shell and high density polyethylene mixtures in argon atmosphere is carried out using thermogravimetric (TGA) approach under non-isothermal condition. This work presents the surface physical morphology of rubber seed shell (RSS), high density polyethylene (HDPE), and its mixtures. Furthermore, the char conversion and char reactivity of RSS, HDPE, and their mixtures at different proportions are investigated in both pyrolysis and gasification process. The argon gas is supplied at a flowrate of 100 mL min-1and the steam is generated from superheater at 383 K whilst injected at flowrate of 3000 µL h-1into the TGA system. 2014 Journal Article http://hdl.handle.net/20.500.11937/69802 10.3303/CET1439114 The Italian Association of Chemical Engineering fulltext |
| spellingShingle | Chin, Bridgid Yusup, S. Al Shoaibi, A. Kannan, P. Srinivasakannan, C. Sulaiman, S. Gasification conversion and char reactivity of rubber seed shell and high density polyethylene mixtures using steam Co-Gasification process |
| title | Gasification conversion and char reactivity of rubber seed shell and high density polyethylene mixtures using steam Co-Gasification process |
| title_full | Gasification conversion and char reactivity of rubber seed shell and high density polyethylene mixtures using steam Co-Gasification process |
| title_fullStr | Gasification conversion and char reactivity of rubber seed shell and high density polyethylene mixtures using steam Co-Gasification process |
| title_full_unstemmed | Gasification conversion and char reactivity of rubber seed shell and high density polyethylene mixtures using steam Co-Gasification process |
| title_short | Gasification conversion and char reactivity of rubber seed shell and high density polyethylene mixtures using steam Co-Gasification process |
| title_sort | gasification conversion and char reactivity of rubber seed shell and high density polyethylene mixtures using steam co-gasification process |
| url | http://hdl.handle.net/20.500.11937/69802 |