Abstract

This study focuses on modelling and simulation of horizontal moving bed/grate wood chip combustor. A standalone finite volume based 2-D steady state Euler–Euler Computational Fluid Dynamics (CFD) model was developed for packed bed combustion. Packed bed combustion of a medium scale biomass combustor, which was retrofitted from wood log to wood chip feeding for Tea drying in Sri Lanka, was evaluated by a CFD simulation study. The model was validated by the experimental results of an industrial biomass combustor for a hot air generation system in tea industry. Open-source CFD tool; OpenFOAM was used to generate CFD model source code for the packed bed combustion and simulated along with an available solver for free board region modelling in the CFD tool. Height of the packed bed is about 20 cm and biomass particles are assumed to be spherical shape with constant surface area to volume ratio. Temperature measurements of the combustor are well agreed with simulation results while gas phase compositions have discrepancies. Combustion efficiency of the validated hot air generator is around 52.2 %.

Highlights

  • Tea industry in Sri Lanka is significant

  • The packed bed top surface temperature value was obtained by the steady state Computational Fluid Dynamics (CFD) simulation results and that value can used as boundary conditions to simulate free board region

  • Packed bed model simulation starts to converge at second iteration and third iteration results have been used as packed bed conditions at steady state

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Summary

Introduction

Tea industry in Sri Lanka is significant. Ceylon Tea is popular all over the world for its quality since for a long time and Sri Lanka is third largest Tea exporter in the world. In this study, packed bed and free board were considered as separate CFD models. A model was developed in OpenFOAM for packed bed combustion of wood chips and free board is simulated using reactingFoam solver in OpenFOAM.

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