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Application of Model Predictive Control in a Dynamic System: An Application to BOF Steelmaking Process

机译:模型预测控制在动态系统中的应用:对BOF炼钢过程的应用

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The mechanism and the kinetics of oxidation reactions in the BOF are very intriguing and still not clearly understood. Prior to this work, a slag-droplet model based on multi-component mixed transport control theory was proposed in which it was assumed that the metal droplets ejected from the jet impact zone carry a thin layer of FeO on the surface and that the droplets were the main mechanism of transporting FeO to the top slag. Calcined lime was assumed to dissolve in the bulk slag through a normal process of formation of dicalcium silicate around lime particles, as also proven by laboratory experiments. In a subsequent work, the examination of morphology of the skull formed on the lance surface showed that the spherical droplets rich in FeO (>90% FeO) are ejected from the jet impact zone and they dissolve CaO and MgO (up to approximately 10 mass%). Since it is now confirmed that FeO rich droplets are ejected from the jet impact zone, it becomes necessary to consider the possibility of decarburization occurring in the region directly below the jet impact area. It is difficult to verify the contribution of decarburization occurring in the zone directly below the area of jet impact from that occurring in the ejected metal droplets and the decarburization taking place at the bulk slag-metal interface. If the decarburization must occur in the region directly below the jet impact zone then the contribution of droplets to the decarburization (after being ejected from a decarburized volume or surface) will be much smaller because they will be ejected from a region which is already decarburized. Also because of the presence of FeO on the surface of droplets the carbon content of metal on the surface of the droplets will be minimal (even though the bulk droplet may have a higher carbon content). In this paper, an attempt has been made to develop a model to understand the mechanism of oxidation reactions in BOF and predict the relative contributions of different possible mechanisms of decarburization, specially in the region of the turbulent zone(s) (the six different zones inside the bulk metal in the case of a six-nozzle tip which are termed in this paper as "reaction zone"). The dynamic reaction zone model thus developed is equally and more effectively successful in explaining and accounting for almost all the practically observed features of the BOF process including: the dynamic changes in the FeO content of slag, decarburization rate in different periods of a blow, evolution of slag composition, pattern of evolution of waste gas flow rate, effect of scrap size and retained slag on dynamic changes in metal and slag composition as well as on decarburization rate, and the evolution of bath temperature profile. One can estimate the reaction zone temperature. The reaction zone concept is also able to demonstrate how the limited oxygen supply in the reaction zone makes it appear as if the decarburization is a zero order reaction in the main blow period.
机译:BOF中氧化反应的机制和动力学非常有趣,仍未清楚地清楚地理解。在本作工作之前,提出了一种基于多组分混合传输控制理论的渣液模型,其中假设从喷射冲击区喷射的金属液滴在表面上携带薄的FEO,并且液滴是将Feo运输到顶部炉渣的主要机制。假设煅烧的石灰通过在石灰颗粒周围形成二巯基硅酸钙的正常过程中溶解体渣中,也通过实验室实验证明。在随后的工作中,检查在喷枪表面上形成的头骨的形态表明,富含FeO(> 90%Feo)的球形液滴从喷射冲击区喷射,它们溶解CaO和MgO(高达约10质量%)。由于现在证实了Feo富液滴从喷射冲击区喷射,因此需要考虑在喷射冲击区域的直接发生在区域中发生脱碳的可能性。难以验证在喷射冲击区域直接在喷射的金属液滴中发生的区域的区域中发生脱碳的贡献,以及在散装渣 - 金属界面处发生的脱碳。如果脱碳必须在射流冲击区域直接发生在地区,则液滴与脱碳(从脱碳体积或表面喷射后)的贡献将要小得多,因为它们将从已经脱碳的区域中喷射。同样由于在液滴表面上存在Feo,液滴表面上的金属的碳含量将是最小的(即使散装液滴可能具有更高的碳含量)。在本文中,已经尝试制定模型以了解BOF中的氧化反应机制,并预测不同可能机制的脱碳机制的相对贡献,特别是湍流区(S)区域(六种不同的区域)在六喷嘴尖端的情况下散装金属内部被称为“反应区”)。如此开发的动态反应区模型同样更有效地成功地解释和核算了BOF过程的几乎所有实际观察到的特征,包括:渣的FEO含量,脱碳率在吹的不同时期的动态变化,进化炉渣组合物,废气流量的演化模式,废料尺寸的影响和保留渣在金属和渣组合物的动态变化以及脱碳速率,以及浴温谱的演变。可以估计反应区温度。反应区概念也能够证明反应区中有限的氧气供应如何使其看起来好像脱碳是主要吹气时期的零级反应。

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