Abstract

This study has focused on the evolution of kinetic parameters, i.e., Eapp and lnAapp and kinetic compensation effects (KCE) of char consumption and CO, CO₂, and H₂ formation during gasification of Collie coal char in varying gas environments (15%H₂O–Ar, 8%H₂O–Ar, and 0.4%O₂+8%H₂O–Ar). The instantaneous rate was obtained continuously during experiments by measuring the product gas composition using a quadrupole mass spectrometer. Observed variations of Eapp, lnAapp, and the extent of KCE suggest that the decrease in steam partial pressure from 15%H₂O to 8%H₂O surrounding the coal char particles appears to affect the path of CO₂ and H₂ formation from surface water-gas shift (WGS) reaction in 15%H₂O–Ar to char-H₂O heterogeneous reaction in 8%H₂O–Ar, at higher conversion (conversion >0.5). However, H₂ formation displays strong KCE and increased H₂ molar flux in 0.4%O₂+8%H₂O–Ar when compared to gasification of char with steam only (8%H₂O–Ar and 15%H₂O–Ar). In contrast, the introduction of 0.4%O₂ to 8%H₂O–Ar dominates the char gasification with only consumption of carbon active sites present on the char surface. That resulted in weak KCE for char consumption and decreased CO/CO₂ (molar flux ratio) compared to the gasification of char in 15%H₂O–Ar and 8%H₂O–Ar. Furthermore, the results indicate that the residual char obtained from the faster diffusion-controlled char-O₂ heterogeneous reaction in the 0.4%O₂+8%H₂O–Ar acts as an activated char precursor for subsequent kinetics-controlled char-H₂O heterogeneous reactions. This enhances the migration of H radicals generated from the H₂O molecule to the inner char matrix in 0.4%O₂+8%H₂O–Ar with an increased H₂ formation rate than gasification of char with steam only.

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