MODELLING OF A PACKED BED REACTOR FOR DRY REFORM OF METHANE

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Autor(es): dc.creatorPontifícia Universidade Católica do Paraná-
Autor(es): dc.creatorPontifícia Universidade Católica do Paraná - Departamento de Engenharia Química-
Autor(es): dc.creatorPontifícia Universidade Católica do Paraná-
Autor(es): dc.creatorDouglas Mayer Rieger-
Autor(es): dc.creatorEmerson Martim-
Autor(es): dc.creatorJair Rosário do Nascimento Junior-
Data de aceite: dc.date.accessioned2025-09-01T11:41:36Z-
Data de disponibilização: dc.date.available2025-09-01T11:41:36Z-
Data de envio: dc.date.issued2024-11-12-
Data de envio: dc.date.issued2024-11-12-
Data de envio: dc.date.issued2018-03-14-
Fonte completa do material: dc.identifierhttps://hdl.handle.net/1884/92946-
Fonte: dc.identifier.urihttp://educapes.capes.gov.br/handle/1884/92946-
Descrição: dc.descriptionIn the present article, the mathematical modeling of a fixed bed reactor to produce synthesis gas (mixture of hydrogen and carbon monoxide) through the dry reforming reaction of natural gas was performed. This product is an important intermediary of the petrochemical industry, being used as reagent in the production of a vast amount of chemicals, fuels and solvents. Reforming with carbon dioxide (dry reforming) has a significant environmental bias, as it uses two of the largest greenhouse-enhancing agents to produce products of interest to the chemical industry. Thus, an adiabatic bed-type reactor (with Ni/Al2O3 as catalyst) was modeled in order to trace the conversion, temperature and pressure profiles in the equipment and to size it. The three ordinary differential equations of the mass, temperature and pressure balances were simultaneously solved by the numerical method of Euler (in Microsoft Excel), resulting in an equipment with 3 ton of catalyst and a minimum length of 3.15 m.-
Formato: dc.formatapplication/pdf-
Formato: dc.formatapplication/pdf-
Relação: dc.relationIII Simpósio Paranaense de Modelagem, Simulação e Controle de Processos (SIMPROC 2018)-
Título: dc.titleMODELLING OF A PACKED BED REACTOR FOR DRY REFORM OF METHANE-
Tipo de arquivo: dc.typelivro digital-
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