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首页> 外文期刊>International Journal of Mineral Processing >A mathematical model of concentrate solids content for the wet drum magnetic separator
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A mathematical model of concentrate solids content for the wet drum magnetic separator

机译:湿鼓式磁选机精矿固体含量的数学模型

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摘要

Low concentrate density from wet drum magnetic separators in dense medium circuits can cause operating difficulties due to inability to obtain the required circulating medium density and, indirectly, high medium solids losses. The literature is almost silent on the processes controlling concentrate density. However, the common name for the region through which concentrate is discharged the squeeze pan gap-implies that some extrusion process is thought to be at work. There is no model of magnetics recovery in a wet drum magnetic separator, which includes as inputs all significant machine and operating variables. A series of trials, in both factorial experiments and in single variable experiments, was done using a purpose built rig which featured a small industrial scale (700 mm lip length, 900 mm diameter) wet drum magnetic separator. A substantial data set of 191 trials was generated in this work. The results of the factorial experiments were used to identify the variables having a significant effect on magnetics recovery. It is proposed, based both on the experimental observations of the present work and on observations reported in the literature, that the process controlling magnetic separator concentrate density is one of drainage. Such a process should be able to be defined by an initial moisture, a drainage rate and a drainage time, the latter being defined by the volumetric flowrate and the volume within the drainage zone. The magnetics can be characterised by an experimentally derived ultimate drainage moisture. A model based on these concepts and containing adjustable parameters was developed. This model was then fitted to a randomly chosen 80 percent of the data, and validated by application to the remaining 20 percent. The model is shown to be a good fit to data over concentrate solids content values from 40 percent solids to 80 percent solids and for both magnetite and ferrosilicon feeds.
机译:致密介质回路中湿鼓式磁选机的低浓缩物密度会导致操作困难,因为无法获得所需的循环介质密度,并且间接地会导致较高的介质固体损失。文献几乎没有提及控制精矿密度的过程。然而,挤压盘间隙通过其排出浓缩物的区域的通用名称意味着某些挤出工艺正在起作用。在湿鼓式磁选机中没有磁回收的模型,该模型包括所有重要的机器和操作变量作为输入。使用专用建造的钻机进行了析因实验和单变量实验的一系列试验,该钻机具有小型工业规模(700毫米唇长,900毫米直径)湿鼓磁选机。这项工作产生了191个试验的大量数据。阶乘实验的结果用于确定对磁回收率有显着影响的变量。基于当前工作的实验观察和文献报道的观察,提出控制磁选机浓缩物密度的过程是排水的一种。这样的过程应该能够由初始湿度,排水速率和排水时间来定义,后者由体积流量和排水区内的体积来定义。磁学可以通过实验得出的最终排水水分来表征。开发了基于这些概念并包含可调整参数的模型。然后将该模型拟合到随机选择的80%的数据中,并通过对其余20%的应用进行验证。结果表明,该模型非常适合精矿固体含量值(从40%固体含量到80%固体含量)以及磁铁矿和硅铁原料的数据。

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