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The activation energy was calculated using the Coats–Redfern integral method. Here, the coal–oxygen combustion reaction was viewed as a first-order reaction. According to the Arrhenius law, the reaction rate of coal combustion can be calculated based on the following equation:

where k denotes the coal–oxygen reaction rate constant, A denotes the frequency factor, E denotes the activation energy (kJ/mol), T denotes the reaction temperature (K), and R denotes the gas constant (R = 8.314 J/(mol⋅K)).

The mass conversion rate during the coal–oxygen reaction process was calculated as follows:

where α denotes the mass conversion rate during the coal combustion process, m0 is the mass of the coal sample at the start of the TGA experiment, mt is the mass of the coal sample in the reaction equipment at moment t (after the start of the TGA experiment), and m is the mass of the coal sample in the reaction equipment at the end of the TGA experiment. The reaction rate was calculated as follows:

where k denotes the chemical reaction rate and t is the time.

Then, an integral operation was performed with the Coats–Redfern approximation, yielding the following equations:

Considering the general reaction temperature range and the activation energy (E), the E/RT was ≥ 1, and 1–2RT/E ~ 1. For n = 1, Eq. (8) could be rewritten as follows:

The above equation was employed to calculate the kinetic parameters of the coal–oxygen reaction in the coal samples. A diagram was generated considering 1n[1n(1 − α)/T2] for the vertical axis and 1/T for the horizontal axis. A linear fitting was then performed on the diagram, and the activation energy was determined according to the slope of the fitting line.

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