The purpose of this study is to evaluate the reducing power of the atmosphere in a cupola for partially reduced ore used for cupola charge under ordinary cupola operating conditions. An experimental melt was carried out in a 2 ton water-cooled hot blast cupola of 540mm diameter at the tuyere level, using a hot blast temperature of 510°C. The blast rate of 42.5 Nm
3/min was controlled with an air-volume controller-recorder. Under an operating condition of a charge composed of 80% sponge iron and 20% pig iron, using coke rate of 40%, the combustion rate of 0.29 in the cupola was obtained and the average metal temperature was 1,460°C. In setting up the equations and the material balance, 33 Kmols of carbon per ton of iron produced are gasified at the tuyeres with a moist blast. The sum of the chemical reaction of the indirect reduction of FeO and solution loss is the same with the direct reduction of FeO. Accordingly, the final results are stoichiometrically the same irrespective of whether the carbon is gasified by reacting with CO
2 gas or with solid FeO. Above the tuyere, 4.9 Kmols of carbon are gasified with oxygen from the charge. A net ton of iron produced contains about 6.97 Kmols of FeO and about 0.62 Kmols of Fe
2O
3 by calculating from analysis values of FeO or Fe
2O
3 and the recovery rate of sponge iron charged. Therefore, calculation for direct reduction ratio is possible and the value obtained was 55.4%. Therefore, the changes in the composition of the gas stream in the cupola can be calculated. As shown in Fig.1, bosh gas is converted to shaft gas which in turn is converted to top gas. The reducing power of the atmosphere gas in the cupola in which FeO is reduced to metallic iron, can be evaluated with the value of CO/CO
2 ratio which exceeds the equilibrium of iron oxides in CO and CO
2 gaseous mixtures. A CO/CO
2 ratio of 2.85 in the bosh gas would mean the less reducing power of the cupola atmosphere. To maintain the reducing power of the bosh gas, a CO/CO
2 ratio of at least 7 should be maintained in consideration of gas-solid equilibrium. Accordingly, a higher coke rate or a limited blast rate to maintain the reducing power and to satisfy the heat requirement is necessary in cupola operating conditions.
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