Multi-scale Modelling of Methanol Synthesis Reactors
dc.contributor.author | Hastadi, Kemal Faza | |
dc.contributor.supervisor | Vishnu Pareek | en_US |
dc.contributor.supervisor | Tejas Bhatelia | en_US |
dc.contributor.supervisor | Milin Shah | en_US |
dc.date.accessioned | 2024-08-12T02:17:26Z | |
dc.date.available | 2024-08-12T02:17:26Z | |
dc.date.issued | 2024 | en_US |
dc.identifier.uri | http://hdl.handle.net/20.500.11937/95681 | |
dc.description.abstract |
Decarbonizing the global energy mix relies on efficiently converting carbonaceous feedstocks like CH4 and CO2, with methanol playing a pivotal role. Methanol serves as a versatile chemical feedstock, energy storage solution, and precursor to clean fuels. Synthesizing methanol involves CO, CO2, and H2 conversion over a copper-based catalyst in a packed bed reactor (PBR). This thesis adopts a multi-scale approach, optimizing reactor design, catalyst properties, and refining kinetic models to enhance methanol synthesis efficiency. | en_US |
dc.publisher | Curtin University | en_US |
dc.title | Multi-scale Modelling of Methanol Synthesis Reactors | en_US |
dc.type | Thesis | en_US |
dcterms.educationLevel | PhD | en_US |
curtin.department | WASM: Minerals, Energy and Chemical Engineering | en_US |
curtin.accessStatus | Fulltext not available | en_US |
curtin.faculty | Science and Engineering | en_US |
curtin.contributor.orcid | Hastadi, Kemal Faza [0000-0003-0595-5853] | en_US |
dc.date.embargoEnd | 2026-08-06 |