Abstract

Our earlier study showed significant differences in average particle velocity between simulation and experimental results for devolatilizing biomass particles in an idealised entrained flow reactor [N. Guo et al., Fuel, 2020]. This indicates that the simulations do not accurately describe the physicochemical transformations and fluid dynamic processes during devolatilization. This article investigates the reasons for these discrepancies using time-resolved analyses of the experimental data and complementary modelling work. The experiments were conducted in a downdraft drop-tube furnace with optical access, which uses a fuel-rich flat flame (CH4O2CO2) to heat the particles. Gas flow was characterized using particle image velocimetry, equilibrium calculations and thermocouple measurements. High-speed images of devolatilizing Norway spruce (Picea Abies) particles were captured and analysed using time-resolved particle tracking velocimetry methods. The data were used to estimate the balance of forces and fuel conversion. Thrust and “rocket-like” motions were frequently observed, followed by quick entrainment in the gas flow. Rocketing particles were, on average, smaller, more spherical and converted faster than their non-rocketing counterparts. These differences in conversion behaviour could be captured by a particle-size dependent, 0-D devolatilization model, corrected for non-isothermal effects. The results from this investigation can provide a basis for future modelling and simulation work relevant for pulverized firing technologies.

Highlights

  • The benefits of biomass as a CO2-neutral energy source [1] have led to a renewed interest in industrial applications during the last decades to mitigate the global warming problem [2,3]

  • Biomass fuels are compatible with existing large-scale energy conversion technologies, such as pulverized suspension firing

  • The particle velocity vectors that are superimposed on the images have been determined with particle tracking velocimetry (PTV) and indicate the velocity magnitude

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Summary

Introduction

The benefits of biomass as a CO2-neutral energy source [1] have led to a renewed interest in industrial applications during the last decades to mitigate the global warming problem [2,3]. Biomass fuels are compatible with existing large-scale energy conversion technologies, such as pulverized suspension firing. Suspension firing is relevant in biofuel production technologies, such as entrained flow gasification, and technologies for CO2 emission reduction, such as oxy-fuel combustion [4,5]. The unique properties of biomass, e.g. much higher reactivity, non-spherical particle morphology, and different ash composition than fossil fuels, create a need for further investigation before they can be implemented on a global scale [6]. Particles undergo a rapid conversion that can be separated into the following three stages: drying, de- Nomenclature A : area, m2.

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