Baolin Hou, Haiying Zhang, Hongzhong Li, et al. Determination of the intrinsic kinetics of iron oxide reduced by carbon monoxide in an isothermal differential micro-packed bed[J]. Chinese Journal of Chemical Engineering, 2015, (6): 974-980.
DOI:
Baolin Hou, Haiying Zhang, Hongzhong Li, et al. Determination of the intrinsic kinetics of iron oxide reduced by carbon monoxide in an isothermal differential micro-packed bed[J]. Chinese Journal of Chemical Engineering, 2015, (6): 974-980.DOI: 10.1016/j.cjche.2015.01.006.
Determination of the intrinsic kinetics of iron oxide reduced by carbon monoxide in an isothermal differential micro-packed bed
The intrinsic kinetics of iron oxide reduced by carbon monoxide is evaluated by a method of online measuring concentration of off-gas in an isothermal differential micro-packed bed. Under the conditi
on of getting away from the influence of gas diffusion and gas–solid heat transfer and mass transfer
the reaction of Fe
2
O
3
to Fe
3
O
4
Fe
3
O
4
to FeO and FeO to Fe in the process of single reaction can be clearly distinguished from each other
and the relevant activation energy is characterized to be 75.4
74.4
and 84.0 kJ·mol
-1
respectively. Therefore
the change of surface area in the reaction process due to losing oxygen could be easily calculated by combining it with pre-exponential parameters of Arrhenius equations. In conclusion
these kinetic parameters are verified by the experimental data for the process of ore reduced by carbon monoxide in a packed bed.
Abstract
The intrinsic kinetics of iron oxide reduced by carbon monoxide is evaluated by a method of online measuring concentration of off-gas in an isothermal differential micro-packed bed. Under the condition of getting away from the influence of gas diffusion and gas-solid heat transfer and mass transfer
the reaction of Fe
2
O
3
to Fe
3
O
4
Fe
3
O
4
to FeO and FeO to Fe in the process of single reaction can be clearly distinguished from each other
and the relevant activation energy is characterized to be 75.4
74.4
and 84.0 kJ·mol
-1
respectively. Therefore
the change of surface area in the reaction process due to losing oxygen could be easily calculated by combining it with pre-exponential parameters of Arrhenius equations. In conclusion
these kinetic parameters are verified by the experimental data for the process of ore reduced by carbon monoxide in a packed bed.
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