During the process of staged coal conversion, secondary fragmentation of coal char in fluidized bed reactors causes fluctuations in bed pressure drop. The resulting fine particles are easily entrained by gas flow to downstream sections, complicating separation processes and exacerbating environmental pollution. This study systematically investigated the influence of coal pyrolysis heating rates on char fragmentation propensity during secondary reactions. Slow-heated char (SHC) and rapid-heated char (RHC) were prepared using a tubular furnace and Joule-heating reactor, respectively. Results demonstrate that SHC fragments more readily than RHC, attributed to heating rate-dependent volatile release during primary pyrolysis that governs pore structure development. SHC exhibits a high specific surface area, small pore size, and high porosity characteristics, with a specific surface area of 91.873 m2/g and an average pore size of 2.954 nm, whereas RHC has a significantly lower specific surface area of only 4.092 m2/g and an average pore size of 9.530 nm. Through an innovative method converting RGB images to quantitative temperature distribution maps, we found that the core heating rate of SHC particles during secondary reactions is significantly lower than that of RHC, with thermal equilibration times of 1300 and 400 ms, respectively. This leads to steeper internal temperature gradients and higher thermal stresses in slow-heated chars. Consequently, SHC exhibits a maximum fragmentation probability of 81% in oxygen and carbon dioxide mixed atmospheres. This research provides a theoretical foundation for optimizing coal staged conversion processes and reactor design.
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