Abstract
Despite the fact that H2 and H2O are always present in the gas atmosphere of a blast furnace shaft, their role in the solution-loss reactions of coke has not been thoroughly examined. This study focuses on how H2 and H2O affect the reaction behavior and whether a strong correlation can be found between reactivity in the conditions of the CRI test (Coke Reactivity Index) and various simulated blast furnace shaft gas atmospheres. Partial replacement of CO/CO2 with H2/H2O was found to significantly increase the reactivity of all seven coke grades at 1373 K (1100 °C). H2 and H2O, however, did not have a significant effect on the threshold temperature of gasification. The reactivity increasing effect was found to be temperature dependent and clearly at its highest at 1373 K (1100 °C). Mathematical models were used to calculate activation energies for the gasification, which were notably lower for H2O gasification compared to CO2 indicating the higher reactivity of H2O. The reactivity results in gas atmospheres with CO2 as the sole gasifying component did not directly correlate with reactivity results in gases also including H2O, which suggests that the widely used CRI test is not entirely accurate for estimating coke reactivity in the blast furnace.
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Acknowledgments
This research is a part of the Systems Integrated Metal Processes (SIMP) research program coordinated by the Finnish Metals and Engineering Competence Cluster (FIMECC). The Finnish Funding Agency for Technology and Innovation (TEKES) and RENEPRO project funded by Interreg Nord are acknowledged for funding this work. Mr. Tommi Kokkonen with the University of Oulu is acknowledged for his technical support.
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Manuscript submitted September 3, 2015.
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Haapakangas, J., Suopajärvi, H., Iljana, M. et al. Coke Reactivity in Simulated Blast Furnace Shaft Conditions. Metall Mater Trans B 47, 2357–2370 (2016). https://doi.org/10.1007/s11663-016-0677-y
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DOI: https://doi.org/10.1007/s11663-016-0677-y