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A new approach for modelling and control of dephosphorization in BOF converter

机译:转炉转炉脱磷建模与控制的新方法

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In the BOF process, the accurate control of Phosphorous removal up to ultra-low values is very important to ensure a high quality of the end–product. This has proven to be associated with several challenges, leading to a preferred usage of high priced low P iron ores. Thus, in the scope of the European BOFdePhos project, important thermodynamic and kinetic aspects of the dephosphorisation reaction such as the effect of solid phases on Phosphorous distribution and lime dissolution in a foamy slag were investigated. It was found that BOF slags are heterogeneous during a large period of the blow and also at the end of blow in most cases. The type and amount of solid phases is strongly affected by temperature and minor oxides content such as MgO-, MnO- and Al2O3-content. The consideration of solid phases formation in the slag, especially the P dissolving C2S_C3P phase, is crucial for a successful modelling and control of dephosphorisation. However, most of the Phosphorous distribution equations available in the literature were developed for homogeneous slags. Thus, a new approach for thermodynamic modelling of the P-distribution between a heterogeneous slag and liquid iron covering the total blowing period in converter was developed and incorporated in a kinetic dephosphorisation model. It was found that while the P distribution in a fully liquid slag was a strong function of temperature, CaO- and FeO-content, the P distribution in a heterogeneous slag depended further on temperature but also on the amount of solid phase as well as the basicity of the liquid slag phase. Even though the C2S_C3P phase can dissolve high amount of Phosphorous, the P-dissolution in the solid phase in the industrial process is associated with strong kinetic limitations. New strategies for the enhancement of dephosphorization control in the BOF converter, focusing on using the potential of the solid phase in removing Phosphorous, were developed.
机译:在转炉过程中,精确控制除磷率至超低值对于确保最终产品的高质量非常重要。事实证明,这伴随着若干挑战,导致高价低磷铁矿石的首选使用。因此,在欧洲BOFdePhos项目的范围内,研究了脱磷反应的重要热力学和动力学方面,例如固相对泡沫渣中磷分布和石灰溶解的影响。已经发现,在大部分吹气期间以及在吹气结束时,BOF炉渣都是不均匀的。固相的类型和数量受温度和少量氧化物含量(例如MgO-,MnO-和Al2O3-含量)的强烈影响。考虑炉渣中固相的形成,特别是溶解P的C2S_C3P相,对于成功进行脱磷的建模和控制至关重要。但是,文献中可用的大多数磷分布方程都是针对均质炉渣开发的。因此,开发了一种新的热力学建模方法,该方法可以对转炉中总吹炼期的非均质炉渣和液态铁之间的P分布进行热力学建模,并将其纳入动力学脱磷模型。已发现,虽然全液态炉渣中的P分布是温度,CaO和FeO含量的强函数,但非均质炉渣中的P分布还取决于温度,还取决于固相量以及熔渣的含量。液态渣相的碱度。即使C2S_C3P相可以溶解大量的磷,但工业过程中固相中的P溶解仍具有很强的动力学限制。开发了新的策略来增强BOF转炉的脱磷控制,重点是利用固相去除磷的潜力。

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