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Numerical Simulation of Effects of Different Operational Parameters on the Carbon Solution Loss Ratio of Coke inside Blast Furnace

机译:不同操作参数对高炉内焦炭碳溶液损失比的影响数值模拟

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摘要

Carbon solution loss reaction of coke gasification is one of the most important reasons for coke deterioration and degradation in a blast furnace. It also affects the permeability of gas and fluids, as well as stable working conditions. In this paper, a three dimensional model is established based on the operational parameters of blast furnace B in Bayi Steel. The model is then used to calculate the effects of oxygen enrichment, coke oven gas injection, and steel scrap charging on the carbon solution loss ratio of coke in the blast furnace. Results show that the carbon solution loss ratio of coke gasification for blast furnace B is almost 20% since the results of a model are probably only indicative. The oxygen enrichment and the addition of steel scrap can reduce the carbon solution loss ratio with little effect on the working condition. However, coke oven gas injection increases the carbon solution loss ratio. Therefore, coke oven gas should not be injected into the blast furnace unless the quality of the coke is improved.
机译:焦化气化的碳溶液损失反应是高炉焦炭劣化和降解的最重要原因之一。它还影响气体和流体的渗透性,以及稳定的工作条件。在本文中,基于BACI钢的高炉B的操作参数建立了三维模型。然后使用该模型来计算氧气富集,焦炉气体注入和钢废料对高炉中焦炭碳溶液损失比的影响。结果表明,高炉B的焦炭气化的碳溶液损失比是近20%,因为模型的结果可能只是指示性。氧气富集和钢废料的添加可以降低碳溶液损失比对工作条件几乎没有影响。然而,焦炉气体注入增加了碳溶液损失比。因此,除非焦炭的质量得到改善,否则焦炉气体不应注入高炉中。

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