## Developing a thermochemical model for the iron blast furnace: rate of reduction of granular ferrous oxide by carbon monoxide in a packed bed |

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37 kilocalories analyses of effluent Arrhenius equation Bed By Hillary bed of oxide best value BLAST FURNACE Rate BuMines Rept Bureau of Mines calculated analyses calculated from equation carbon monoxide coefficients were determined Developing a Thermochemical effluent gas cover equation 9 Equilibrium composition equilibrium ratio experiments finite difference fraction of C02 gas and solids given by equation GOSUB granular ferrous oxide hematite Iron Blast Furnace iron oxide ith layer J1 TO J2 J2 LET J2 STEP J0 mathematical model moles oxygen moles per mole-minute observed and calculated Observed Calculated Deviation Oxide by Carbon oxygen density p r i n r packed bed partial pressure particle diameter percent C02 rate of flow rate of reaction rate of reduction reaction of granular reaction rate coefficient reducing gas Reduction of Granular reduction of iron reduction of wustite Smith and McKewan squares of deviation stage of reduction sum of squares Thermochemical Model tion