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dc.contributor.authorHastadi, Kemal Faza
dc.contributor.supervisorVishnu Pareeken_US
dc.contributor.supervisorTejas Bhateliaen_US
dc.contributor.supervisorMilin Shahen_US
dc.date.accessioned2024-08-12T02:17:26Z
dc.date.available2024-08-12T02:17:26Z
dc.date.issued2024en_US
dc.identifier.urihttp://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.publisherCurtin Universityen_US
dc.titleMulti-scale Modelling of Methanol Synthesis Reactorsen_US
dc.typeThesisen_US
dcterms.educationLevelPhDen_US
curtin.departmentWASM: Minerals, Energy and Chemical Engineeringen_US
curtin.accessStatusFulltext not availableen_US
curtin.facultyScience and Engineeringen_US
curtin.contributor.orcidHastadi, Kemal Faza [0000-0003-0595-5853]en_US
dc.date.embargoEnd2026-08-06


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