Reactor design and techno-economic analysis for chemical looping hydrogen production
This project describes several aspects of process design for chemical looping hydrogen production technology. Multi-dimensional model of the reactor system is represented through dynamic simulations, demonstrating optimum conversions under isothermal operation. The optimal conditions are then utiliz...
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| Format: | Thesis |
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Curtin University
2023
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| Online Access: | http://hdl.handle.net/20.500.11937/94807 |
| _version_ | 1848765929438052352 |
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| author | Kataria, Priyam |
| author_facet | Kataria, Priyam |
| author_sort | Kataria, Priyam |
| building | Curtin Institutional Repository |
| collection | Online Access |
| description | This project describes several aspects of process design for chemical looping hydrogen production technology. Multi-dimensional model of the reactor system is represented through dynamic simulations, demonstrating optimum conversions under isothermal operation. The optimal conditions are then utilized for developing a reactor design capable of exhibiting gas-solid reactions. A techno-economic assessments is further conducted, which highlights profitability and efficiency of the proposed system compared to the conventional Steam Methane Reforming. |
| first_indexed | 2025-11-14T11:43:03Z |
| format | Thesis |
| id | curtin-20.500.11937-94807 |
| institution | Curtin University Malaysia |
| institution_category | Local University |
| last_indexed | 2025-11-14T11:43:03Z |
| publishDate | 2023 |
| publisher | Curtin University |
| recordtype | eprints |
| repository_type | Digital Repository |
| spelling | curtin-20.500.11937-948072024-04-10T02:13:20Z Reactor design and techno-economic analysis for chemical looping hydrogen production Kataria, Priyam This project describes several aspects of process design for chemical looping hydrogen production technology. Multi-dimensional model of the reactor system is represented through dynamic simulations, demonstrating optimum conversions under isothermal operation. The optimal conditions are then utilized for developing a reactor design capable of exhibiting gas-solid reactions. A techno-economic assessments is further conducted, which highlights profitability and efficiency of the proposed system compared to the conventional Steam Methane Reforming. 2023 Thesis http://hdl.handle.net/20.500.11937/94807 Curtin University restricted |
| spellingShingle | Kataria, Priyam Reactor design and techno-economic analysis for chemical looping hydrogen production |
| title | Reactor design and techno-economic analysis for chemical looping hydrogen production |
| title_full | Reactor design and techno-economic analysis for chemical looping hydrogen production |
| title_fullStr | Reactor design and techno-economic analysis for chemical looping hydrogen production |
| title_full_unstemmed | Reactor design and techno-economic analysis for chemical looping hydrogen production |
| title_short | Reactor design and techno-economic analysis for chemical looping hydrogen production |
| title_sort | reactor design and techno-economic analysis for chemical looping hydrogen production |
| url | http://hdl.handle.net/20.500.11937/94807 |