Applicability of Scaling Approach for Analysis of Pyrolysis and Gasification of Porous Structures Composed of Solid Fuel Particles

Table 2

Parameters of the pyrolysis approximations obtained with the three kinetic models.

S/F agent	𝑇 (°C)	RPM				GM				VM
		𝑅^2	𝜓	𝑘0 (s^−1)	𝐸𝑎 (J/Mol)	𝑅^2	FF	𝑘0 (s^−1)	𝐸𝑎 (J/Mol)	𝑅^2	𝑘0 (s^−1)	𝐸𝑎 (J/Mol)
1.875	767	0.996	0.56	84	90023	0.995	0.33	82	90069	0.994	9367	130000
	830	0.992	2.34	55	90024	0.991	0.33	63	90067	0.986	5381	130000
	913	0.985	0.1	75	90020	0.967	0.33	58	90062	0.984	4508	130000
3.2	795	0.985	0.1	108	90021	0.969	0.33	686	108012	0.986	1485	113000
	876	0.993	10.42	30	90024	0.976	0.33	385	108037	0.935	790	113000
	906	0.994	7.41	40	90023	0.975	0.33	430	108032	0.935	868	113000
Argon	788	0.979	45.08	504	114000	0.963	0.33	507	104528	0.938	950	109000
	833	0.944	3.29	501	114000	0.964	0.85	452	104532	0.881	451	109002
	917	0.996	11.19	310	114499	0.996	0.84	425	104532	0.916	418	109004