Abstract

The elaborate and appropriate design of blast furnace (BF) inner profile is indispensable. In practice, in this work, dumpiness, quantified by the ratio of belly diameter to effective height (RD–H), primarily determines the inner profile and significantly affects the BF performance. However, the effects of RD–H on BF operation are not investigated thoroughly, and an optimal range of RD–H is not yet proposed. In this work, a numerical study on this topic is presented to recommend an RD–H range for BF designers. This is achieved by using a recently developed 3D multi‐fluid BF process model based on a 380 m3 industrial BF. In the results, it is shown that both too slender and too dumpy BFs do not favor BF production. Excessively slender BF leads to a dramatic increase in gas pressure drop; however, the saving of coke or the improvement of productivity is insignificant. In contrast, excessively dumpy BF leads to a dramatic increase in coke rate and a significant decrease in productivity. Under the current conditions, the recommended dumpiness exists in the value of RD–H at around 0.35, where a low coke rate, low gas pressure drop, high productivity, and high thermal energy utilization are all ensured.

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