Determination of biomass combustion rate in a domestic fixed bed boiler

Mariana Vale da Silva; Victor Ferreira; Carlos Pinho; Mariana Vale da Silva; Victor Ferreira; Carlos Pinho

doi:10.3934/energy.2021049

AIMS Energy

2021, Volume 9, Issue 5: 1067-1096. doi: 10.3934/energy.2021049

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Determination of biomass combustion rate in a domestic fixed bed boiler

1.
INEGI—Instituto de Ciência e Inovação em Engenharia Mecânica e Engenharia Industrial, Porto, Portugal
2.
CEFT—DEMEC—Faculdade de Engenharia da Universidade do Porto, Porto, Portugal

Received: 13 May 2021 Accepted: 29 September 2021 Published: 25 October 2021

This manuscript presents an experimental study on the combustion rate of biomass briquettes or logs in a domestic boiler, by monitoring the time decay of its mass and the temperature of the flame inside the boiler. Assuming close to steady state conditions, two combustion models were studied: the constant particle density-burning model and the constant particle diameter-burning model. For each model, the evolution of the global combustion resistance with the decay of the particle diameter was analyzed, and it was possible to conclude that the burning occurred approximately with constant particle size and that the heterogeneous C to CO reaction takes place at the surface of the inner carbonaceous core. The high values obtained for the Sherwood number revealed that there were significant convective effects inside the furnace and compare well with a previously developed Sherwood number correlation for a packed bed of active particles.
- biomass,
- briquettes,
- combustion rate,
- fixed bed,
- wood logs
Citation: Mariana Vale da Silva, Victor Ferreira, Carlos Pinho. Determination of biomass combustion rate in a domestic fixed bed boiler[J]. AIMS Energy, 2021, 9(5): 1067-1096. doi: 10.3934/energy.2021049

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Abstract

This manuscript presents an experimental study on the combustion rate of biomass briquettes or logs in a domestic boiler, by monitoring the time decay of its mass and the temperature of the flame inside the boiler. Assuming close to steady state conditions, two combustion models were studied: the constant particle density-burning model and the constant particle diameter-burning model. For each model, the evolution of the global combustion resistance with the decay of the particle diameter was analyzed, and it was possible to conclude that the burning occurred approximately with constant particle size and that the heterogeneous C to CO reaction takes place at the surface of the inner carbonaceous core. The high values obtained for the Sherwood number revealed that there were significant convective effects inside the furnace and compare well with a previously developed Sherwood number correlation for a packed bed of active particles.

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