Xiangyong Zheng, Feng Wang, Jianjiang Wang, Bo Wei, Kunpeng Liu, Shan Wang, Rui Ma, Lijuan Chen, Maierhaba Abudoureheman
Xinjiang high‑chlorine coal has abundant reserves, but its high chlorine content causes slagging, ash deposition and equipment corrosion during pyrolysis, limiting its large-scale utilization. This study investigated the effects of particle size (54–200 μm) and heating rate (10–30 °C/min) on the pyrolysis characteristics and kinetics of Shaerhu coal (SEH) using TG-DTG analysis, the Coats-Redfern method and model-free methods. SEH pyrolysis involved three stages, with weight loss peaks near 100 °C, 450 °C and 715 °C. SHE's peak mass loss rate temperature was 10–30 °C lower than other low-rank coals. Larger particles significantly increased the weight loss rate, peaking at 0.1164 %/°C for 150–200 μm. Higher heating rates shifted DTG curves upper right, reduced mass loss rates and increased thermal hysteresis. C-R method indicated that in Stage I, higher heating rates raised activation energy ( E ). In Stage II, particle size influenced E more than heating rate. In Stage III, larger particles had lower E (19.51–34.09 kJ·mol −1 reduction from 54–76 to 150–200 μm). Model-free methods showed consistent E trends, but generally Friedman > FWO > KAS. A notable E decrease occurred at 0.8 conversion for 54–76 μm particles, while 150–200 μm particles declined gradually from 220 kJ·mol -1 after 0.4 conversion. • The pyrolysis kinetic of Xinjiang high- Chlorine coal was first calculated. • SEH's peak mass loss rate temperature is 10–30 °C lower than other low-rank coals. • The peak weight loss rate increases with raising particle size by 24.5–26 %. • The degree of thermal hysteresis increases with the decrease of particle size. • The effects of particle size and heating rate on E are various at different stages.