Mechanisms governing the “gasification to char oxidation transition” in counter-current flame propagation in packed beds: insights from single-particle experiments

Abstract

Mechanisms governing the gasification to combustion regime transition in counter-current packed bed biomass systems are investigated in the current work. Single-particle experiments are performed with different oxidizer streams (air, mixtures of O₂/CO₂) to bring out the role of the extinction of the envelope non-premixed “volatiles” flame and simultaneous volatile-char combustion at the stagnation point on the transition to char oxidation in packed beds. Results indicate that for O₂ fractions lower than 23% (w/w), the transition is governed by the extinction of the envelope diffusion flame. At higher O₂ fractions, typically >32% (w/w), simultaneous volatile-char oxidation at the stagnation point drives the transition to char combustion. The strain rates computed at “gasification to char combustion transition” from earlier studies with air and O₂ fractions ≤23% (w/w) in the oxidizer streams coincide with the strain rates obtained at the transition from classical envelope flame to a wake flame with single particles. Velocities at which simultaneous oxidation of volatiles and char was observed at the stagnation point with single particles subjected to oxidizer streams with O₂ ≥ 32% (w/w) matches with the velocities at transition in the packed beds from the earlier studies. Simultaneous volatile-char oxidation and decrease in reaction zone thickness from a few particles to one particle diameter observed post-transition in packed beds support the theory.

Keywords:

• Thermo-chemical conversion
• ligno-cellulosic biomass
• extinction strain rate
• non-premixed “volatiles” flame
• packed bed
• counter-current flame propagation