Abstract
Non-isothermal method was used to study gasification characteristics of three coal chars and one biomass char. Four chars were made from anthracite coal (A), bituminous coal (B), lignite coal (L), and wood refuse (W), respectively. The gasification process was studied by random pore model (RPM), unreacted core model (URCM) and volumetric model (VM). With an increase in metamorphic grade, the gasification reactivity of coal char decreased, and the gasification reactivity of biomass char was close to that of low metamorphic coal char. With an increase in heating rate, the gasification of all samples moved towards high temperature zone, and the whole gasification time decreased. It was concluded from kinetics analysis that the above-mentioned three models could be used to describe the gasification process of coal char, and the RPM fitted the best among the three models. In the RPM, the activation energies of gasification were 193.9, 225.3 and 202. 8 kJ/mol for anthracite coal char, bituminous coal char and lignite coal char, respectively. The gasification process of biomass char could be described by the URCM and VM, while the URCM performed better. The activation energy of gasification of wood refuse char calculated by the URCM was 282.0 kJ/mol.
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Abbreviations
- C :
-
Concentration of reaction gas
- E :
-
Apparent activation energy
- k :
-
Apparent reaction rate constant
- k o :
-
Pre-exponential factor
- L o :
-
Hole length
- m n :
-
Initial mass of sample
- m ∞ :
-
Final mass of sample
- m t :
-
Mass of sample at time t
- n :
-
Reaction order
- R :
-
Universal gas constant
- R 2 :
-
Correlation coefficient
- S o :
-
Specific surface area
- t :
-
Reaction time
- T :
-
Temperature
- T o :
-
Reaction starting temperature
- α:
-
Char gasification conversion rate
- f(α):
-
Function of mechanism of reaction kinetics
- β:
-
Heating rate
- δ:
-
Relative error
- εo:
-
Solid porosity
- ψ:
-
Parameter of particle structure.
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Xu, T., Wang, Gw., Zhang, Jl. et al. Non-isothermal study of gasification process of coal char and biomass char in CO2 condition. J. Iron Steel Res. Int. 24, 985–990 (2017). https://doi.org/10.1016/S1006-706X(17)30144-9
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DOI: https://doi.org/10.1016/S1006-706X(17)30144-9