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Modeling Concept for Intensive Reacting Submerged Gas Injection a Case Study of a Peirce-Smith Converter

机译:深度反应下注气的建模概念-以Peirce-Smith转化器为例

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A mathematical modeling concept has been developed to simulate the reactive gas injection of a Peirce-Smith converter. The concept is capable of calculating the cross-sectional time-averaged flow and temperature field of gas and melt and the concentration field of gas composition with the aid of a commercial Computation Fluid Dynamic (CFD) solver. The concept is based on the two-fluid model in which heat, mass and momentum transfer coupling is carried out by combining the interfacial area concentration and the flow regime concepts. The present limitations of CFD were found to set many restrictions on formulating a completed analysis of the fluid dynamics of the studied reactor and CFD calculations were supplemented with physical and simplified heat and mass balance modeling. A CFD analysis was carried out for four separate short periods of time on a typical converter cycle. The modeling concept predicted that flow conditions may change considerable during a single converter cycle. Currently used tools, based on the input power of gas injection and non-dimensional groups, cannot predict this variation, even though the general trends of these correlations agree with the mathematical modeling concept.
机译:已经开发出数学建模概念来模拟Peirce-Smith转换器的反应性气体注入。该概念能够借助商用计算流体动力学(CFD)求解器来计算气体和熔体的截面平均时间流和温度场以及气体成分的浓度场。该概念基于双流体模型,在该模型中,热,质量和动量传递耦合是通过结合界面面积浓度和流态概念来进行的。发现CFD的当前局限性为制定完整的被研究反应堆流体动力学分析提供了许多限制,并且CFD计算得到了物理和简化的热量与质量平衡模型的补充。在一个典型的转换器周期内,在四个单独的短时间内进行了CFD分析。建模概念预测,在单个转换器周期内,流量条件可能会发生相当大的变化。当前使用的基于注气和无量纲组输入功率的工具无法预测这种变化,即使这些相关关系的总体趋势与数学建模概念一致。

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