Abstract

This work presents a comparative study on different biomass feedstock gasification in a fluidized bed using air. This work aims to study the effect of different biomass fuel types on the gasification performance in a fluidized bed, using kinetic hydrodynamic model results and similar experimental results. The feedstocks used in this study are sawdust pellets, Napier Grass, Portuguese Peach Stone, Chinese Coal /rice straw, solid waste wood, rice straw and olive kernels. The theoretical results were obtained from the kinetic-hydrodynamic simulation of the fluidized bed. The theoretical results were compared with published experimental results. The results showed that the syngas contents are strongly affected by the gasification temperature, equivalence ratio, and fuel characteristics. Increasing ER increases the char burning rate to produce more H2 even medium equivalence ratio (usually less than 0.36) and decreases again. CH4, CO, and H2 increased as temperature increased. From the fuel proximate analysis, the moisture contents affect the combustion reactions to generate more hydrogen. The lower H/C ratio gives greater heating value, as well as gives more concentrations of CO and CO2. In the case of using waste woody and rice straw, the significant increase of carbon monoxide (from 9% to 19%) and carbon dioxide (from 25% to 33.1%) is due to a higher C/O ratio in these biomasses analyses. The proximate analysis of feedstock and its contents from fixed carbons and volatiles matters affect strongly the producer gas concentrations, as a result, it’s LHV. The maximum relative error between model results and experimental results within range ±10.2%.

Highlights

  • THE gasification process consists of drying, pyrolysis, combustion, and char gasification

  • Li et al [2] performed an experimental study on syngas production by co-gasification of coal and biomass in a fluidized bed

  • The rice husk gasification process, in a bubbling fluidized bed gasifier, was investigated using a kinetic model that comprises with hydrodynamics model

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Summary

INTRODUCTION

THE gasification process consists of drying, pyrolysis, combustion, and char gasification. Li et al [2] performed an experimental study on syngas production by co-gasification of coal and biomass in a fluidized bed. The authors reported that the contents of combustible gas increased with temperature, an increase of oxygen concentration has a positive effect on gas quality and gasification result, but has a negative effect on gas yield. The rice husk gasification process, in a bubbling fluidized bed gasifier, was investigated using a kinetic model that comprises with hydrodynamics model. The main aim of this work is to theoretical studying the effect of biomass fuel type on the gasification performance in a fluidized bed. The results of the mathematical model were verified by comparing its results with the experimental results of similar works

MATHEMATICAL MODELLING
16 Syngas analyzer 17 Produced syngas
Reaction mechanism of the kinetic sub-model
Assumptions and initial conditions of the kinetic model
Discretization of the numerical solution
Numerical solution procedure
FEEDSTOCK SPECIFICATIONS
Effect of equivalence ratio on syngas composition
Effect of operating temperature on syngas composition
Effect of feedstock type on the syngas heating value
Effect of feedstock type on the cold gas efficiency
CONCLUSIONS
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